diapositivas de aga

7212019 Diapositivas de Aga

httpslidepdfcomreaderfulldiapositivas-de-aga 171

EMERSONProcess ManagementCONO SUR amp Brazil

Mediciones fiscales

de

Gas Natural



Oil and Gas Flow Measurement Market

OIL

GAS

LPG

LNG PROCESS

PIPELINEQUALITYGAS

JETTY UNLOADING TRANSPORT

PIPELINE

REFINING amp PETROCHEMICAL PROCESSING

BULKSTORAGETERMINAL

MARKETING

TERMINAL

CITY GATES

POWER PLANTS

INDUSTRIALPLANTS

RESIDENTIAL

PRODUCTIONPROCESSING

TRANSMISSION DISTRIBUTION

TRANSPORTATION



Transportadora

Generacioacuten

Termoeleacutectrica

Residencial

Industrial

Comercial

PlantaDe

Procesamiento

ProduccioacutenOffshore

ProduccioacutenOn-shore

Distribuidora

Mercado de Gas



Medicioacuten fiscal de Transferencia deCustodia

Cuando un proveedor entregaun producto a un cliente ocurreuna transaccioacuten econoacutemica

Para asegurar un intercambio

justo de bienes una medicioacutenexacta es critica en la operacioacuten

El equipamiento de medicioacuten es

la caja registradora de estatransaccioacuten



CromatoacutegrafoEnergiacutea yComposicioacutenz=AGA 8Pcal=API 145

Flow ComputerFiscal API 211 y 212Caacutelculo de volumen (AGA 3711)Caacutelculo de energiacutea (API 145)

Caacutelculo de compresibilidad (AGA 8)

$$$$$= Volumen Energeacutetico

APLICACIOacuteN DE TRANSFERENCIACUSTODIADA DE GAS

Click Here

AGA 11

AGA 9

AGA 3

AGA 7

PT

[ ]

[ ]

3

3

3

Base3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=



Estandards de la Industria del Gas

American Gas Association AGA 3 - Placas Orificio

AGA 7 - Turbina Axial

AGA 5 - Caacutelculos Energeacuteticos

AGA 8 - Caacutelculos de Supercompresibilidad

AGA 9 - Ultrasoacutenico

AGA 10 - VOS (Calculada vs Medida) -

AGA 11 - Medidores Coriolis ( Sep 2003 )

API 143 ISO 5167 (Placa Orificio)



Tipos de Medidores de Gas

Armadura con Placa de Orificio AGA Reporte Nro 3 API MPM Capiacutetulo 143 ISO 5167

Medidor de Turbina

AGA Reporte Nro 7

Medidor Ultrasoacutenico

AGA Reporte Nro 9

Medidor Coriolis AGA Reporte Nro 11



Mediciones Fiscales

PozosUSP

Compresioacuten

Produccioacuten NGL

EndulzamientoAminasGlycolDew Point

Compresioacuten

Transmisioacuten

60 BAR



Hidrocarbonos

El Carbono tiene valencia 4 (puede ganar 4 electrones elHidrogeno tiene Valencia 1 con lo cual puede ganar unelectron asiacute se forma el Metano



Moleacuteculas Gas Natural Cromatografiacutea

Component Range (mole)

Methane 65 to 100

Ethane 0 to 20

Propane 0 to 10

N-Butane 0 to 5

Iso-Butane 0 to 5

N-Pentane 0 to 1

Iso-Pentane 0 to 1

Neo-Pentane 0 to 1

Hexane+ 0 to 07Nitrogen 0 to 20

Carbon Dioxide 0 to 20



Moleacuteculas Gas Natural Livianos

Metano (CH4) 89-99

Etano (C2H6) lt 3

Dioacutexido de Carbono (CO2)lt2

Nitrogeno(N2)lt2



Moleacuteculas Gas Natural Medianos

Propane (C3) menor 2

Butanos (C4iC4) menor 5

Pentanos (C5iC5nC5) menor 5

Gas25degC

Liq25degC



Moleacuteculas Gas Natural Pesados ySuperios (C6+)

Hexanos (C6 e isoacutemeros)

Heptanos (C7 e isoacutemeros)

Octanos (C8 e isoacutemeros)

Nonanos (C9+ e isoacutemeros)

Total C6+lt1 o dew-point



Moleacuteculas Gas Natural Otros

O2 ppm Oxygen

H2O lt 01 Agua

SO2 amp H2Slt100-2ppmSulfhydric

CO ppm

Gases Nobles ArHeNeXe ppm

CH3SH ppm Methil Mercaptanoodorizacioacuten



La cromatografiacutea actual se basa en la separacioacuten decomponentes l ivianos de pesados por la diferencia

en el tiempo de traacutensito de cada uno de ellos

Principio de funcionamiento de lacromatografiacutea gaseosa

P i i i d f i i d l



Los componentes livianos tendraacuten el menor tiempode traacutensito


P i i i d f i i t d l



Los componentes medianos tendraacuten un t iempo detraacutensito intermedio





Los componentes pesados poseen el mayor tiempode traacutensito




Cromatoacutegrafo Baacutesico

Detector Columna

Muestra

He

Amplificacioacuten

AD CPU

Cromatoacutegrafo baacutesico

Registrador

80 +- 5ordmC



Cromatoacutegrafo Daniel



Combustioacuten Gas Natural

CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt

Gas Natural + Aire(Oxigeno) = Dioxido de Carbono + Agua + Energia



El poder calor iacutefico permite determinar el voluacutemen enrgeacutetico a 9300 Kcalm3

[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=

Gas Natural perdidas por incertidumbre

[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=

Un error de 50 Kcal que representa un error de 05 en 9000KCalm3

produce un error en caudal de 43000m3 en 8000Km3

A 14 u$s1MMBTU 43010m3 representau$sday 2400

G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3

API 145 GPA 2172 Caacutelculo deenergiacutea y caacutelculo de densidad





Instalacioacuten Tiacutepica



Ley de los Gases

PV=nRT Ecuacioacuten ldquoidealrdquo

PV=ZnRT Ecuacioacuten ldquoRealrdquoP=presioacuten

V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number

Ley De Charles Ley de Boyle

Correccioacuten por Presioacuten y Temperatura



=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV

Correccioacuten por Presioacuten y Temperaturaa condiciones base

Paiacutes

Tbase Pbase

Argentina 15 ordmC 101325 kPa

15 ordm C 101325 kPa

0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)

Condiciones dereferencia

Europa

EEUU



bullMetano=80 a 99

bullNitroacutegeno=01 a 5

bullDioacutexido de Carbono=01 a 5

bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2

bullPentanos=001 a 1

bullHexanos y superiores=0001 1

bullOtrosH2H2SCOO2He Ar

Composicioacuten tiacutepica de Gas Natural

F t Z AGA 8 Meacutet d G



Factor Z AGA 8 Meacutetodo Grueso0ltPlt1200PSIA32ltTlt130ordmF

Metodo Gross IbullGr

bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2

F t Z AGA 8 Meacutet d d t ll d



bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3

bullC6+=0 to Dew Point

bullWater VaporH2H2SCOO2He Ar

bullPoder caloriacutefico y densidad

Factor Z AGA 8 Meacutetodo detallado0ltPlt40000PSIG-200ltTlt760ordmF

Caracteriacutesticas de un Medidor de



Caracteriacutesticas de un Medidor de Armadura con Placa de Orificio

Incertidumbre+- 100 (086 )

Rango de Caudales3 a 1 o 8 a 1

stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP

elevacioacuten Diferenciahh

π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22

Para cantildeeria circular

Simplificando

La energia se mantiene constante a lo largode la cantildeeriacutea

C=Coeficiente de descarga

B lli



Bernoulli Algunas aplicaciones

C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22



Volumetric Flow Rate

[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3



Norma AGA 3Introduccioacuten preliminar

Se define la relacioacuten betha como

650350 ltlt= β β PD

OD

micro

ρ=

DvRe

Se define como nuacutemero de Reynolds a

Haga click aquiacute

Rgt3000

Rlt2300

Norma AGA 3




bullC=depende de β de Reynolds y de la distancia entre tomas de presioacuten ydiametro de cantildeeriacutea tiende a 06 pero depende de la configuracioacuten -

bullK=depende de la presioacuten Area de orificio y beta-

bullCorner taps se usa en Europa

bullFlange Taps es el mas usado en America

Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3



Norma AGA 3Caacutelculo de Voluacutemen

FlowFlowrel

wFlows2

BaseBase1BaseBaseTZGhPZd C NYEQ =

TPDP

Expresados a 1 Atm y15ordmC

3

Cordm15ATM1

3

Base h

m

h

m

Q ==

coeff _ eargdisch _ plate _ OrificeC

ansionexp _ GasY

convert _ units N

factor _ aproach _ VelE

base

1

Base

Base

=

=

=

=

29D 5D



Dimensiones recomendadas



Principio de funcionamiento del Portaplaca



Orifice Plate Dimensions



Ejemplo de Armadura Senior



Acondicionador de flujo

AGA 3 - 2000 solo acepta 19 tubos conceacutentricos de igual tamantildeo

AGA 3 - 2000 no acepta

Disentildeo con bandas laterales de terminacioacuten 19 tubos de disentildeo exagonal

7 tubos conceacutentricos

Universal Meter Tube with Vane



MAX 46 BETA


AGA 1992

AGA 2000



Acondicionador de flujo - Profiler reg

Universal Meter Tube with Profiler



MAX 67 BETA

Universal Meter Tube with ProfilerFlow conditioner

Profiler Flow conditioner Installation




Norma AGA 7



ncalibracioacute _ datoK

m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=

Norma AGA 7En turbinas

10D3D

PTQflow



Caracteriacutesticas de un Medidorde Turbina

Linealidad +- 100 (+- 05 )

Repetibilidad +- 01

Rango de Caudales 20 a 1



Trineo de medicioacuten con Turbinas

Norma AGA 9



Norma AGA 9En ultrasoacutenicos

Frecuenci _ o _ Digital _ DatoQFlow

=

20D o 5+FP+10D 5D

PT

Qflow



Caracteriacutesticas de un MedidorUltrasoacutenico

Linealidad +- 050 con Dry Calibration

Linealidad +- 010 con Flow Calibration

Rango de Caudales

100 a 1



Principio de Funcionamiento

Ultrasoacutenico Multipath de Gas




)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2

Transducer 1v = L 2x

(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2

v=velocidad de flujo

c=velocidad del sonido

t 1 =tiempo de traacutensito upstream t 2 = tiempo de transito downstream

2

Q = vA

Custody Metering Your Cash



Custody Metering ndash Your CashRegister

FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$

Compressibility(AGA8)

Energy (GPA2172 or

ISO6976)

5D5D 10D

Custody Metering ndash Your Cash




FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV



Instalacioacuten Ultrasoacutenico seguacuten AGA 9

10 I h C t d S i S i



10-Inch Custody SeniorSonic

Norma AGA 7



Norma AGA 7En turbinas y ultrasoacutenicos

=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs

factor _ bilityercompresisupsF

factor _ litycompresibiZZS

=

=

=

Resuacutemen de especificacioacuten de performance




Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16

P e r c e n t E r r o r

qmin qmaxqt

Repeatability plusmn02 (qi ge qt)

Large meter error limit +07

Large meter error limit -07

Small meter error limit +10

Small meter error limit -10

Expanded error limit +14 (qi lt qt)

Expanded error limit -14 (qi lt qt)

Repeatability plusmn04 (qi lt qt)

Zero flow reading lt004 ftsec (for each path)

Maximum peak-to-peak error 07 (qi ge qt)

qt le 01qmax

Figure 1 from AGA 9

Comparacioacuten AGA 9 vs ISO 17089






Medidor Coriolis para Gas - AGA 11






Medidor Coriolis para Gas - Ejemplo

Norma AGA 11



o a GEn coriolis

baseaire _densidad)air (

baselativaRe _DensidadGr

Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=

No Pressure amp Temperature correction neededto compute Mass

Caacutelculo de Energiacutea




[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=

El voluacutemen expresado de esta manera implicaque cada m3 de gas produce 9300 KCAL

Vaacutelido solo coriolis

Flow Computer



pEn custody Transfer Requisitos

bullAPI 211 y 212

bullNormas AGA ISO API

bull840 horas de registros histoacutericos de Datos y calidad

bull35 diacuteas de almacenamiento histoacuterico de datos y calidadbull240 Eventos y alarmas

bullPassword y niveles de acceso

bullRemote communications

bullTotales (diarios y horarios no reseteables)

Click Here



Gas Chain

Sweetening Glycol LiquidRecovery

Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation

H2O Liquid ProductsC2C3C4

C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2

Otras aplicaciones de nuestros productos en



GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98

ProductoIntermedioC2H6 =25C3H8=25C4H10=35C5+=15

Centrales Termoeleacutectricas




Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea

a xEficienci Energiacutea Energiacutea

h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe

Perdida monetaria por error de



pmedicioacuten en planta de 600MW

64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd

diacuteausd DailyLoss

error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



Oil and Gas Flow Measurement Market

OIL

GAS

LPG

LNG PROCESS

PIPELINEQUALITYGAS

JETTY UNLOADING TRANSPORT

PIPELINE

REFINING amp PETROCHEMICAL PROCESSING

BULKSTORAGETERMINAL

MARKETING

TERMINAL

CITY GATES

POWER PLANTS

INDUSTRIALPLANTS

RESIDENTIAL

PRODUCTIONPROCESSING

TRANSMISSION DISTRIBUTION

TRANSPORTATION



Transportadora

Generacioacuten

Termoeleacutectrica

Residencial

Industrial

Comercial

PlantaDe

Procesamiento



Distribuidora

Mercado de Gas
















Click Here

AGA 11

AGA 9

AGA 3

AGA 7

PT

[ ]

[ ]

3

3

3

Base3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=
















Medidor de Turbina

AGA Reporte Nro 7


AGA Reporte Nro 9




Mediciones Fiscales

PozosUSP

Compresioacuten

Produccioacuten NGL


Compresioacuten

Transmisioacuten

60 BAR



Hidrocarbonos






Methane 65 to 100

Ethane 0 to 20

Propane 0 to 10

N-Butane 0 to 5

Iso-Butane 0 to 5

N-Pentane 0 to 1

Iso-Pentane 0 to 1

Neo-Pentane 0 to 1






Metano (CH4) 89-99

Etano (C2H6) lt 3


Nitrogeno(N2)lt2







Gas25degC

Liq25degC












O2 ppm Oxygen

H2O lt 01 Agua


CO ppm








P i i i d f i i d l


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



Transportadora

Generacioacuten

Termoeleacutectrica

Residencial

Industrial

Comercial

PlantaDe

Procesamiento



Distribuidora

Mercado de Gas
















Click Here

AGA 11

AGA 9

AGA 3

AGA 7

PT

[ ]

[ ]

3

3

3

Base3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=
















Medidor de Turbina

AGA Reporte Nro 7


AGA Reporte Nro 9




Mediciones Fiscales

PozosUSP

Compresioacuten

Produccioacuten NGL


Compresioacuten

Transmisioacuten

60 BAR



Hidrocarbonos






Methane 65 to 100

Ethane 0 to 20

Propane 0 to 10

N-Butane 0 to 5

Iso-Butane 0 to 5

N-Pentane 0 to 1

Iso-Pentane 0 to 1

Neo-Pentane 0 to 1






Metano (CH4) 89-99

Etano (C2H6) lt 3


Nitrogeno(N2)lt2







Gas25degC

Liq25degC












O2 ppm Oxygen

H2O lt 01 Agua


CO ppm








P i i i d f i i d l


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==
















Click Here

AGA 11

AGA 9

AGA 3

AGA 7

PT

[ ]

[ ]

3

3

3

Base3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=
















Medidor de Turbina

AGA Reporte Nro 7


AGA Reporte Nro 9




Mediciones Fiscales

PozosUSP

Compresioacuten

Produccioacuten NGL


Compresioacuten

Transmisioacuten

60 BAR



Hidrocarbonos






Methane 65 to 100

Ethane 0 to 20

Propane 0 to 10

N-Butane 0 to 5

Iso-Butane 0 to 5

N-Pentane 0 to 1

Iso-Pentane 0 to 1

Neo-Pentane 0 to 1






Metano (CH4) 89-99

Etano (C2H6) lt 3


Nitrogeno(N2)lt2







Gas25degC

Liq25degC












O2 ppm Oxygen

H2O lt 01 Agua


CO ppm








P i i i d f i i d l


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==
















Medidor de Turbina

AGA Reporte Nro 7


AGA Reporte Nro 9




Mediciones Fiscales

PozosUSP

Compresioacuten

Produccioacuten NGL


Compresioacuten

Transmisioacuten

60 BAR



Hidrocarbonos






Methane 65 to 100

Ethane 0 to 20

Propane 0 to 10

N-Butane 0 to 5

Iso-Butane 0 to 5

N-Pentane 0 to 1

Iso-Pentane 0 to 1

Neo-Pentane 0 to 1






Metano (CH4) 89-99

Etano (C2H6) lt 3


Nitrogeno(N2)lt2







Gas25degC

Liq25degC












O2 ppm Oxygen

H2O lt 01 Agua


CO ppm








P i i i d f i i d l


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



Mediciones Fiscales

PozosUSP

Compresioacuten

Produccioacuten NGL


Compresioacuten

Transmisioacuten

60 BAR



Hidrocarbonos






Methane 65 to 100

Ethane 0 to 20

Propane 0 to 10

N-Butane 0 to 5

Iso-Butane 0 to 5

N-Pentane 0 to 1

Iso-Pentane 0 to 1

Neo-Pentane 0 to 1






Metano (CH4) 89-99

Etano (C2H6) lt 3


Nitrogeno(N2)lt2







Gas25degC

Liq25degC












O2 ppm Oxygen

H2O lt 01 Agua


CO ppm








P i i i d f i i d l


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



Hidrocarbonos






Methane 65 to 100

Ethane 0 to 20

Propane 0 to 10

N-Butane 0 to 5

Iso-Butane 0 to 5

N-Pentane 0 to 1

Iso-Pentane 0 to 1

Neo-Pentane 0 to 1






Metano (CH4) 89-99

Etano (C2H6) lt 3


Nitrogeno(N2)lt2







Gas25degC

Liq25degC












O2 ppm Oxygen

H2O lt 01 Agua


CO ppm








P i i i d f i i d l


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==





Methane 65 to 100

Ethane 0 to 20

Propane 0 to 10

N-Butane 0 to 5

Iso-Butane 0 to 5

N-Pentane 0 to 1

Iso-Pentane 0 to 1

Neo-Pentane 0 to 1






Metano (CH4) 89-99

Etano (C2H6) lt 3


Nitrogeno(N2)lt2







Gas25degC

Liq25degC












O2 ppm Oxygen

H2O lt 01 Agua


CO ppm








P i i i d f i i d l


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




Metano (CH4) 89-99

Etano (C2H6) lt 3


Nitrogeno(N2)lt2







Gas25degC

Liq25degC












O2 ppm Oxygen

H2O lt 01 Agua


CO ppm








P i i i d f i i d l


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==







Gas25degC

Liq25degC












O2 ppm Oxygen

H2O lt 01 Agua


CO ppm








P i i i d f i i d l


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==












O2 ppm Oxygen

H2O lt 01 Agua


CO ppm








P i i i d f i i d l


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==






P i i i d f i i d l


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==


















Detector Columna

Muestra

He

Amplificacioacuten

AD CPU


Registrador

80 +- 5ordmC







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==







CH4 + 2 O2 -gt CO2 + 2 H2O + 891 kJ

+ + +-gt





[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




[ ] [ ]

3

3

3

STD

3

m

KCal9300

m

KCal9300

m

KCalPCalmV

mV3

=


[ ][ ]

3

3

3

3

m

KCal9300

m

KCal50m8000000

m43010

=




G C



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



Analizador c

GPAPCal

lensl Dens

i

i

rArr

rArr

=

=

sum

sum

=

=

2145

ReDcRe

PCalcm

KCalPCal

n

1i

ii

n

1i

ii3









Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==








Ley de los Gases



V=Volumen

T=Temeperatura

Z=compresibilidad

R=cte

N=mole number





=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



=Flow

Base

Flow

Base

Base

FlowFlowBase

Z

Z

T

T

P

PVV


Paiacutes

Tbase Pbase



0 ordmC 101325 kPa

60 ordmF

14696 psi

(abs)

60 ordmF

1473 psi

(abs)


Europa

EEUU



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



bullMetano=80 a 99



bullEtano=01 a 10

bullPropano=01 a 5

bullButanos=001 a 2










bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==





bullHV

bullCO2

Metodo Gross II

bullGr

bullCO2

bullN2




bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



bullC1=45 a 100

bullN2=0 a 50

bullCO2=0 a 30

bullC2=0 a 30

bullC3=0 a 4

bullC4=0 a 1

bullC5=0 a 3











stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==






stacked transmitter

B lli



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



BernoulliEquations

2

2211

2112

12

4

2) _ (0

D A

AV AV Q

g

V V

g

PP


π

ρ

=

==

minus

+

minus

+minus=

PK Q

ACV Q

∆=

= 22


Simplificando



B lli




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




C=098

C=098

C=096

C=06

PKC Q ACV Q∆=

= 22




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




[ ]

absolutoceroC F

C F

F F T T

Z

GrT

PPK Q

PKC Q

T PV

M

_ 527367459

3281

67459

=degminus=degminus

+deg=deg

deg+deg=

∆=

∆=

Norma AGA 3



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



Norma AGA 3

Norma AGA 3






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==






OD

micro

ρ=

DvRe



Rgt3000

Rlt2300

Norma AGA 3








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==








Z TGr

PPC K Q

PKC Q

V

M

∆=

∆=

Norma AGA 3




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




FlowFlowrel

wFlows2


TPDP


3

Cordm15ATM1

3

Base h

m

h

m

Q ==


ansionexp _ GasY

convert _ units N


base

1

Base

Base

=

=

=

=

29D 5D























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==























MAX 46 BETA


AGA 1992

AGA 2000







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==







MAX 67 BETA






Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




Norma AGA 7




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




m

pulsosK

Hr

sec

3600Sec

pulsos

Freq Q

Factor

3factor

in

Flow

=

=


10D3D

PTQflow




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




Linealidad +- 100 (+- 05 )

Repetibilidad +- 01





Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




Norma AGA 9





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==





=

20D o 5+FP+10D 5D

PT

Qflow






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==






Rango de Caudales

100 a 1








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==








)Lx(vc

Lt

)Lx(vc

Lt

+=

minus

=

2

1

L Flow

X

D

Transducer 2


(t 1 -t 2 ) t 1 t 2

c =

L

2

(t 1 +t 2 )

t 1 t 2




2

Q = vA





FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




FILTER

FILTER

ActualVolumetric

Flow

GasComposition

StandardVolumetric

Flow

Energy

Flow

$$


Energy (GPA2172 or

ISO6976)

5D5D 10D





FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




FILTER

FILTER

CiC1C2C9+

$$

Z(AGA8)

5D5D 10D

sum=

=n

1i

iiPCalcPCal

9300

PCalVV B

m

KCal9300

3

=

F

B

F

B

B

FF

Z

Z

T

T

P

PV

factor

in

K

Pulse=FV








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==








Norma AGA 7




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




=

Flow

Base

Flow

Base

Base

Flow

FlowBaseZ

Z

T

T

P

PQQ

2

PV

PV

Flow

Base

Fs



=

=

=





Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




Flow Rate (qi)

-16

-14

-12

-10

-08

-06

-04

-02

-00

02

04

06

08

10

12

14

16


qmin qmaxqt











qt le 01qmax

Figure 1 from AGA 9














Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==













Norma AGA 11



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



o a GEn coriolis



Gr

Q

Q

Base

Base

Maacutesico

Base

=ρ

=

ρ=






[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




[ ]

[ ]

[ ] [ ]

[ ][ ]

3

3

m

KCal9300

3

3

m

KCal9300

3

3

3

Base

3

m

KCal9300

m

KCal

9300

kg

KCalPCalkgM

mV

m

KCal

9300

KCalEmV

m

KCal9300

m

KCalPCalmV

mV

3

3

3

=

==

=

=



Flow Computer




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




bullAPI 211 y 212







Click Here



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



Gas Chain


Fractionation

NGL Acid GasH2S

FlareInjection

Raw GasSweet Gas

Dehydratation


C5+

Dew

Point

GasTo

Sale

Amina

C6+

LiquidProducts

Mix of C2+and C3+

CO2




GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==



GasNatural

Waste=C5+

LPGC3=60

C4=40

Planta de NGL

p p planta de NGL

Gas SecoCH4 =98






Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




Power Plant

Eficiencia=06

1KCalh=1163Watts

MWatts Energiacutea

x

h

KCal x

KCal

hWatts Energiacutea


h

KCal

h

m

m

KCal

h

mQ Energiacutea

OUTPUT

OUTPUT

INPUT OUTPUT

m

Kcal INPUT

600

60000250860

1631

000250860500923009

00095

3

3

3

93003

=

=

=

==

==

Wobbe





64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==




64

1262164520050

50

2524cos

10518032Pr

130Pr

3506MMPower

10453354893930095000Power 3

3

3

3

Millonesusd Year

MMusd YearLoss

diacuteausd

diacutea MMusd


error

diacutea

MMusd Cost t Daily

husd Power ice

husd Cost

MMBTU

usd ice

h

BTU

ft

BTU

h

ft

m

KCal

h

m

h

KCal

Gas

Gas

=

==

=

==

==

=

=

==

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