coccooco 2222 based refrigeration systems · advansor offers refrigeration systems (compressor...

47
CO CO CO CO based refrigeration systems based refrigeration systems based refrigeration systems based refrigeration systems CO CO CO CO 2 2 2 based refrigeration systems based refrigeration systems based refrigeration systems based refrigeration systems for heating and cooling for heating and cooling for heating and cooling for heating and cooling Århus Århus Århus Århus 14. maj 2009 14. maj 2009 14. maj 2009 14. maj 2009 Kim G. Christensen Kim G. Christensen Kim G. Christensen Kim G. Christensen

Upload: others

Post on 19-Jun-2020

10 views

Category:

Documents


0 download

TRANSCRIPT

COCOCOCO based refrigeration systems based refrigeration systems based refrigeration systems based refrigeration systems COCOCOCO2222 based refrigeration systems based refrigeration systems based refrigeration systems based refrigeration systems for heating and coolingfor heating and coolingfor heating and coolingfor heating and cooling

ÅrhusÅrhusÅrhusÅrhus14. maj 200914. maj 200914. maj 200914. maj 2009

Kim G. ChristensenKim G. ChristensenKim G. ChristensenKim G. Christensen

About ADVANSOR www.advansor.dk� ADVANSOR is specialized in CO2-technologies within the fields of

refrigeration and heat pumps

� ADVANSOR has 8 employees and a turnover of 3 mill. euro

� ADVANSOR develops, manufacturers and sell projects within� Combined Heating and PowerCombined Heating and PowerCombined Heating and PowerCombined Heating and Power� Process industryProcess industryProcess industryProcess industry� Food industryFood industryFood industryFood industry� SupermarketsSupermarketsSupermarketsSupermarkets

� Our products are:� Heat pumps Heat pumps Heat pumps Heat pumps 20202020----1000 kW1000 kW1000 kW1000 kW� Chillers / ACChillers / ACChillers / ACChillers / AC----systemssystemssystemssystems 80808080----400 kW400 kW400 kW400 kW� Supermarket refrigerationSupermarket refrigerationSupermarket refrigerationSupermarket refrigeration 6/15 6/15 6/15 6/15 –––– 50/250 kW50/250 kW50/250 kW50/250 kW� Light commercialLight commercialLight commercialLight commercial 100100100100----1000 kW1000 kW1000 kW1000 kW� Costumer specified productsCostumer specified productsCostumer specified productsCostumer specified products Engineering, design, production of series of 5Engineering, design, production of series of 5Engineering, design, production of series of 5Engineering, design, production of series of 5----10 units 10 units 10 units 10 units

� We work closely together with partners and suppliers and have cooperation with Danish associations, private research institutes and universities, EPA and the Ministry of Transport and Energy as well as the Danish Industry

Markedsmæssige træk for CO2-køleanlæg

� HFC - lovgivning: Max 10 kg HFC pr kreds – i praksis begrænsning på 30-60 kW for luftkølede aggregater

� Andre naturlige kølemidler� giftige eller brændbaregiftige eller brændbaregiftige eller brændbaregiftige eller brændbare� tørkøleropstillinger med forhøjet energiforbrugtørkøleropstillinger med forhøjet energiforbrugtørkøleropstillinger med forhøjet energiforbrugtørkøleropstillinger med forhøjet energiforbrug

� CO2 påtænkt at lukke hullet optil større kaskadeanlæg � området mellem 30området mellem 30området mellem 30området mellem 30----400 kW400 kW400 kW400 kW

CO2-konkurrenter (transkritisk)

� Knudsen/ PVN (Danmark)

� Green and Cool (Sverige)

� Linde/ Carrier (Tyskland)

� Fischer (Tyskland)

� Dresdner Kühlanlagenbau (Tyskland)

� Costan (Italien)

� Enex (Italien)

� Blue Wave (Italien)� området mellem 30området mellem 30området mellem 30området mellem 30----400 kW400 kW400 kW400 kW

� Blue Wave (Italien)

Primære markeder

� Supermarkeds køl (Nordeuropa)

� Industriel køl/ frys (dx)

� Varmepumper (høje temperaturer)

� comBINE anvendelser

� Aircondition (chillere og dx)

ADVANSOR’s products

compHEAT: CHP – combined heat and powerAdvansor develops heat pump solutions dedicated to power

plants operated by either gas motor or gas turbines.

The heat pump produces hot water up to 90°C which enables

direct pipe connection to the external pipe work with no

interference with the motor and piping.

compBINE: Combined heating and coolingCombined heating and cooling - produce hot water up to 100°C

and get ice water for free or counter wise. Advansor’s product

line is highly suitable in connection with pasteurisation, CIP

systems and other application in food industry where coinciding

demands for heating and cooling exist. Combined heating and

cooling saves both capital investment and energy cost.cooling saves both capital investment and energy cost.

compFORT: Chiller applications and AC systemsAdvansor offers highly compact air cooled chillers and AC

systemsin the range from 100 to 400 kW. With natural

refrigerant, no toxic risk and no flammability this is a safe and

economical feasible choice.

compSUPER: Refrigeration applicationsAdvansor offers refrigeration systems (compressor rack’s) for

supermarkets and other commercial/ industrial applications.

The units work with as the only refrigerant. Main focus are

placed on reliability, ease of service and low energy

consumption.

Characteristics of CO2

Benefits:

� Environmentally friendly refrigerant (ODP = 0, GWP = 1)

� Smaller pipe dimensions

� Better efficiency of compressors

� Better heat transfer

Safety issues:

� Group L1 – no flammability and no toxicity

� No restriction regarding installation and use – easy to install

CO2

� No restriction regarding installation and use – easy to install

� Temperature/ pressure: -55 -> +31°C (5.5 -> 73 bar)

� Heavier than air

Challenges :

� High pressures (120 bar)

� Standstill pressure

� Use of safety valves

� Separation of oil and liquid from CO2 gas

� Energy efficiency / price

Transcritical versus subcritical operation

60

70

80

90

100

110

120

130

140

T [

°C]

0,0

017

0,0

1

0,0

19

0,0

34

CarbonDioxideOverhedet gas

Transkritisk:Ingen faseskifte ved varmeafgivelseIngen faseskifte ved varmeafgivelseIngen faseskifte ved varmeafgivelseIngen faseskifte ved varmeafgivelse[T, p] er indbyrdes uafhængige[T, p] er indbyrdes uafhængige[T, p] er indbyrdes uafhængige[T, p] er indbyrdes uafhængigeTryk for optimal COPTryk for optimal COPTryk for optimal COPTryk for optimal COPGod afkøling vigtig for optimal COPGod afkøling vigtig for optimal COPGod afkøling vigtig for optimal COPGod afkøling vigtig for optimal COPpinch point skal undgås i vekslerenpinch point skal undgås i vekslerenpinch point skal undgås i vekslerenpinch point skal undgås i vekslerenSubkritisk: ”business as usual”

FordeleFordeleFordeleFordelesmå dimensioner

materiale valg

Transition:

-1,60 -1,40 -1,20 -1,00 -0,80-10

0

10

20

30

40

50

60

s [kJ/kg-K]

T [

°C]

60 bar

35 bar

18,7 bar

70 bar

0,2 0,4 0,6 0,8

Superkritisk fluid

Transition:Anlægget kører i de 2 driftsformerAnlægget kører i de 2 driftsformerAnlægget kører i de 2 driftsformerAnlægget kører i de 2 driftsformer

styring

anlæggets udformning

Fundamental concerns

� High pressure components – stand-still pressure� Leak tight system� Oil management� Noise and vibration� Water in the system

� System design and choice of components� Availability of components� Reliability of components� Reliability of components� All systems/ components tested before going into the market

… heavy tests for 1 year

� Controllers (Danfoss, industrial PLC – Simens/ Beckhoff)

� Energy consumption� PED and approval by Notified Body� Education of installers and technicians� Prices that can bring the technology to the market

Fundamental design and considerations � High pressure side/ low pressure side – 120 and 40/25 bar

� Standstill pressure for receiver Standstill pressure for receiver Standstill pressure for receiver Standstill pressure for receiver –––– 90 bar (refrigerant stays on the system)90 bar (refrigerant stays on the system)90 bar (refrigerant stays on the system)90 bar (refrigerant stays on the system)� Tightness = hermetic solutions

� Welded carbon steel, semihermetic compressorsWelded carbon steel, semihermetic compressorsWelded carbon steel, semihermetic compressorsWelded carbon steel, semihermetic compressors� Conical treads, metal seal, no elastomersConical treads, metal seal, no elastomersConical treads, metal seal, no elastomersConical treads, metal seal, no elastomers

� Advanced oil management � Oil coolingOil coolingOil coolingOil cooling� Oil separator with filter (99.98 % oil separation), Oil level controlOil separator with filter (99.98 % oil separation), Oil level controlOil separator with filter (99.98 % oil separation), Oil level controlOil separator with filter (99.98 % oil separation), Oil level control

� Noise and vibrations� Flexible hoses, vibrations shoes, supports of pipingFlexible hoses, vibrations shoes, supports of pipingFlexible hoses, vibrations shoes, supports of pipingFlexible hoses, vibrations shoes, supports of piping� Low velocities and no sharp edges and continuous optimizationLow velocities and no sharp edges and continuous optimizationLow velocities and no sharp edges and continuous optimizationLow velocities and no sharp edges and continuous optimization� Low velocities and no sharp edges and continuous optimizationLow velocities and no sharp edges and continuous optimizationLow velocities and no sharp edges and continuous optimizationLow velocities and no sharp edges and continuous optimization

� System design for high reliability� Integrated oil cooling, liquid separator and suction gas heat exchangerIntegrated oil cooling, liquid separator and suction gas heat exchangerIntegrated oil cooling, liquid separator and suction gas heat exchangerIntegrated oil cooling, liquid separator and suction gas heat exchanger� Suction gas filters, filter driers to remove water from the systemSuction gas filters, filter driers to remove water from the systemSuction gas filters, filter driers to remove water from the systemSuction gas filters, filter driers to remove water from the system

� System design (for low energy consumption)� Optimized compressor design and oOptimized compressor design and oOptimized compressor design and oOptimized compressor design and optimized gasptimized gasptimized gasptimized gas----cooler designcooler designcooler designcooler design� Adiabatic humidification of the gasAdiabatic humidification of the gasAdiabatic humidification of the gasAdiabatic humidification of the gas----cooler, heat recovery is integrated on requestcooler, heat recovery is integrated on requestcooler, heat recovery is integrated on requestcooler, heat recovery is integrated on request

� Safety issues - The system is CE-marked from the manufacturer� All design specifications are satisfied All design specifications are satisfied All design specifications are satisfied All design specifications are satisfied

Mechanical: MD(98/37/EC) / PED(97/23/EC) / EN378 / EN13480 / EN13445Mechanical: MD(98/37/EC) / PED(97/23/EC) / EN378 / EN13480 / EN13445Mechanical: MD(98/37/EC) / PED(97/23/EC) / EN378 / EN13480 / EN13445Mechanical: MD(98/37/EC) / PED(97/23/EC) / EN378 / EN13480 / EN13445Electrical: LVD(06/95/EC) / EMC(89/336/EC) / EN60204Electrical: LVD(06/95/EC) / EMC(89/336/EC) / EN60204Electrical: LVD(06/95/EC) / EMC(89/336/EC) / EN60204Electrical: LVD(06/95/EC) / EMC(89/336/EC) / EN60204----1111

� Pressostats and safety valvesPressostats and safety valvesPressostats and safety valvesPressostats and safety valves

Systems for supermarkets – trends of development

Design of systems

� Calculation of the cycle

� Calculation of pressure drop

� Design of piping

� Compressor calculation

� Design of condenser

ηis,HT = 0,6614 [-]

ηis,LT = 0,5 [-]

λHT = 0,7459 [-]

λLT = 0,8 [-]

Pm = 35 [Bar]

te,HT = -10 [°C]

te,LT = -35 [°C]

tgk,ud = 32 [°C]

VHT = 35,37 [m3/h]

VLT = 9,379 [m3/h]

Pgk,ud = 90 [Bar]

compSUPER

WHT = 41,07 [kW]

WLT = 3,601 [kW]

Other

Other

Low temp.Medium temp.

Evap. temp.

Super heat

Epsilon ihx

Capacity

te,HT = -10 [°C] te,LT = -35 [°C]

toh,HT = 10 [K] toh,LT = 10 [K]

QHT = 60 [kW] QLT = 15 [kW]

εHT = 0,01 [-] εLT = 0,1 [-]

Advansor A/S, 04-02-2008

QHT,komp = 78,6

2xTCS373=2x12,6=25,2 m3/h

SCC250=3,86

Qc = 119,7

SCC300=5,3

SCC380=8,47

U = 400 [V] I = 70,86 [A]

Wtotal = 44,68

COPtotal = 1,68 [-]

SCC180=2,89

SCC350=6,75

SCC250+350=10,6m3

IHT = 65,15

ILT = 5,711

t2 = 117,7 [°C]

t2 = 117,7 [°C]

TCS362/4 + TCS362 = 16,1 m3/h

t1 = 0,5052 [°C]

dTunuse = 0

Qohf = 0,01225 [kW]

Quk = 0 [kW]

T16,2 = 50

Tgk,ud2 = 32

t16 = 50,19 [°C]

t15 = -24,97 [°C]

Optimal COP

Fixed pressure

� Design of condenser

� Design of valves (ICMT/ ETS)

� Receiver size

� Oil management

� PI + BOM

� SolidWorks for the construction

Installation og operation

� Turn-key project from Advansor� Compressor rackCompressor rackCompressor rackCompressor rack� CondenserCondenserCondenserCondenser� Evaporators, valves and controllersEvaporators, valves and controllersEvaporators, valves and controllersEvaporators, valves and controllers

� Installation� Connection of pipes for condenser (steel)Connection of pipes for condenser (steel)Connection of pipes for condenser (steel)Connection of pipes for condenser (steel)� Connection of evaporators (cupper pipes)Connection of evaporators (cupper pipes)Connection of evaporators (cupper pipes)Connection of evaporators (cupper pipes)� Connection of evaporators (cupper pipes)Connection of evaporators (cupper pipes)Connection of evaporators (cupper pipes)Connection of evaporators (cupper pipes)� Programming of controllers and electrical wiringProgramming of controllers and electrical wiringProgramming of controllers and electrical wiringProgramming of controllers and electrical wiring

� Start-up� Leak test, pressure test and evacuationLeak test, pressure test and evacuationLeak test, pressure test and evacuationLeak test, pressure test and evacuation� Installation of filters and driers + filling of oilInstallation of filters and driers + filling of oilInstallation of filters and driers + filling of oilInstallation of filters and driers + filling of oil� Filling of CO2 gas and filling of CO2 liquidFilling of CO2 gas and filling of CO2 liquidFilling of CO2 gas and filling of CO2 liquidFilling of CO2 gas and filling of CO2 liquid� StartStartStartStart----up of MT and LTup of MT and LTup of MT and LTup of MT and LT

Service and maintanance

� User manual

� Service description� OilOilOilOil� Filers and driersFilers and driersFilers and driersFilers and driers� CO2 level and oil levelCO2 level and oil levelCO2 level and oil levelCO2 level and oil level� Service of semi hermetic compressorsService of semi hermetic compressorsService of semi hermetic compressorsService of semi hermetic compressors� Service of heat exchangersService of heat exchangersService of heat exchangersService of heat exchangers� Service of heat exchangersService of heat exchangersService of heat exchangersService of heat exchangers

� General procedure� PumpPumpPumpPump----down to receiverdown to receiverdown to receiverdown to receiver� Relief of gasRelief of gasRelief of gasRelief of gas� Fulfillment of maintenanceFulfillment of maintenanceFulfillment of maintenanceFulfillment of maintenance� Evacuation, pressurization with CO2 and restartEvacuation, pressurization with CO2 and restartEvacuation, pressurization with CO2 and restartEvacuation, pressurization with CO2 and restart

Energy consumption for simple single stage

By Transkritisk

[MWh]

Subkritisk [MWh] Besparelse,

transkritisk [%]

Stockholm 64,1 68,0 6

København 65,5 69,1 5

Amsterdam 70,6 72,0 2

Berlin 72,9 72,9 0

Paris 76,6 74,5 -3Paris 76,6 74,5 -3

Lyon 80,8 77,0 -5

Madrid 89,1 82,2 -8

Marseille 91,9 83,1 -11

Barcelona 93,1 83,1 -12

Rom 95,0 85,0 -12

Reference: DTU, Technical University of Denmark (IPU)

Energy consumption (booster vs. cascade) (-20%)

compSUPER S 2x2 (20x10 kW) - FAKTA

4

5

6

7

8

9

10

11

Jan Feb Mar Apr Maj Juni Juli Aug Sept Okt Nov Dec

En

erg

ifo

rbru

g [

kW

h/

h]

Max CO2 - trans

Mid CO2 - trans

Min CO2 - trans

Max CO2 - kaskade

Mid CO2 - kaskade

Min CO2 - kaskade

Max R134a

Mid R134a

Min R134a

compSUPER S 2x2B

Kapacitet: 20-40 kW (frekvensomformer)

Anlægget: LxHxW = 1600x2100x780 mm

Vægt: 1000 kg

compSUPER S 2x2B til Gate Gourmet -inddækket

compSUPER XL 4x3 (70x25 kW)

Indendørsopstilling:

Anlægget: LxHxW = 3350x1895x780 mm

Rammer kan adskilles:

Køl: LxHxW = 2450x1895x780 mm

Frost: LxHxW = 2450x1895x780 mm

Receiver: LxHxW = 900x1895x780 mm

Vægt: 1650 kg

compSUPER XL 4x3B - SuperBrugsen

Benefits from compSUPER XL

� Reliability� Optimized oil management systemOptimized oil management systemOptimized oil management systemOptimized oil management system� Protection against excessive pressureProtection against excessive pressureProtection against excessive pressureProtection against excessive pressure� Pressure management during electrical Pressure management during electrical Pressure management during electrical Pressure management during electrical

cutcutcutcut----outoutoutout� Documented componentsDocumented componentsDocumented componentsDocumented components

� Energy consumption� Software tools of optimizationSoftware tools of optimizationSoftware tools of optimizationSoftware tools of optimization� Software tools of optimizationSoftware tools of optimizationSoftware tools of optimizationSoftware tools of optimization� Optimized controlsOptimized controlsOptimized controlsOptimized controls� Selection of componentsSelection of componentsSelection of componentsSelection of components� Documented lowest energy Documented lowest energy Documented lowest energy Documented lowest energy

consumptionconsumptionconsumptionconsumption� Optimized layout

� 3D design of all racks3D design of all racks3D design of all racks3D design of all racks� Optimized for lo production cost and Optimized for lo production cost and Optimized for lo production cost and Optimized for lo production cost and

low service costlow service costlow service costlow service cost

compSUPER XL 4x3B

� LT capacity:

� 45 kW at 45 kW at 45 kW at 45 kW at ----30303030°°°°CCCC� 3 x Bitzer HC compressors3 x Bitzer HC compressors3 x Bitzer HC compressors3 x Bitzer HC compressors

� MT capacity:� 80 kW at 80 kW at 80 kW at 80 kW at ----10101010°°°°CCCC� 4 x Bitzer TC compressors4 x Bitzer TC compressors4 x Bitzer TC compressors4 x Bitzer TC compressors

� MP-Receiver: 130 liter, featuring� system pump down system pump down system pump down system pump down � 90 bar design pressure90 bar design pressure90 bar design pressure90 bar design pressure

� Design pressures:� Design pressures:� 25/40/120 bar25/40/120 bar25/40/120 bar25/40/120 bar

� Individual compressor� Oil management systemOil management systemOil management systemOil management system� saftety pressure switchsaftety pressure switchsaftety pressure switchsaftety pressure switch

� Air cooled gas cooler� 35 dBa 10 m35 dBa 10 m35 dBa 10 m35 dBa 10 m� Optimised high pressure and sub Optimised high pressure and sub Optimised high pressure and sub Optimised high pressure and sub

cooling controlcooling controlcooling controlcooling control

compSUPER S 1x0/ 2x0Small medium temperature applications

T_e = -15->+10°°°°C

Capacities: 10-80 kW

Kapacitet: 40 kW (frekvensomformer)

Anlægget: LxHxW = 1200x1500x780 mm

Vægt: 300 kg

Kapacitet: 80 kW (frekvensomformer)

Anlægget: LxHxW = 2000x1500x780 mm

Vægt: 450 kg

Partial heat recovery from CO2 – refrigeration systems

40

60

80

100

120

Try

kg

as [

C]

15%

20%

25%

30%

35%

40%

45%

An

del

af

Q_c d

er

gen

vin

des

Trykgastemperatur

Andel VGV af Q_c

0

20

40

COP_NH3 COP_propan COP_CO2

Try

kg

as [

C]

0%

5%

10%

15%

An

del

af

Q_c d

er

gen

vin

des

T_e = -10C

eta_is = 0,65

T_c = 20C

T_VGV = 22C

Partiel varmegenvinding - systemudformning

+25C+50C

Heat recovery

unitAir cooled condenser

High pressure valve

Valve for gas-by-pass

Min. temp. = 25°CValve closes at 25°C

Control valve and

pump on water side

T2

P2

Fans

F1

T3

T1

30

40

50

60

70

80

Tem

pera

ture

- w

ate

r, a

ir,

refr

igera

nt

[°C

]

tvand[i]

Heat recovery unit

mdot;ref=0,3 [kg/s]

Pgk=65 [bar]

mdot;luft=6 [kg/s]

mdot;vand=0,3 [kg/s] tgk;ind=90 [°C]

tluft;ind=14 [°C]

tluft;ud=22 [°C]

tvand;ind=25 [°C]

tvand;ud=50 [°C]

tref;intermidiate=29,57 [ ]

Intermidiate pressure receiver

246810121416182022242628303234363840424446485052545658606264666870727476788082848688909294969810010

20

Enthaly steps [0=ref entrance/ 100 ref exit]

Tem

pera

ture

- w

ate

r, a

ir,

refr

igera

nt

[°C

]

50%50%

Aircooled condenser

Qluft=48,5 [kW] Qvand=31,5 [kW]

AVGV=12,99 [m 2̂]

UAVGV=2,598 [kW * m 2̂]

� Høj effektivitet under VGV� Kold udeluft udnyttes i kondensator til underkølingKold udeluft udnyttes i kondensator til underkølingKold udeluft udnyttes i kondensator til underkølingKold udeluft udnyttes i kondensator til underkøling

� Styring/ design væsentlig for at undgå kondensering, kogning,

� Design væsentlig for at undgå pinch problemer

Køleanlæg med fuld varmegenvinding: Transkritisk varmepumpedrift

50

60

70

80

90

Tem

pera

ture

- w

ate

r, a

ir, re

frig

era

nt [°

C]

tvand[i]

mdot;ref=0,5 [kg/s]Pgk=75 [bar]

mdot;luf t=2,6 [kg/s]

mdot;vand=0,55 [kg/s]tgk;ind=110 [°C]

tluf t;ind=10 [°C]tluf t;ud=15 [°C]

tvand;ind=10 [°C]tvand;ud=60 [°C]

tref ;intermidiate=29,57 [ ]tvgv;ud=32,15 [ ]

24681012141618202224262830323436384042444648505254565860626466687072747678808284868890929496981000

10

20

30

40

Enthaly steps [0=ref entrance/ 100 ref exit]

Tem

pera

ture

- w

ate

r, a

ir, re

frig

era

nt [°

C]

Heat recovery unitAircooled condenser

Qluf t=14,3 [kW]Qvand=115,5 [kW]

mdot;luf t=2,6 [kg/s]

AVGV=16,68 [m 2̂]UAVGV=10,01 [kW * m 2̂]

Driftskonditioner med partiel/fuld varmegenvinding (VGV) – eksempel 100 kW køl

� Køleanlæg� Min. kondenseringstrykstyringMin. kondenseringstrykstyringMin. kondenseringstrykstyringMin. kondenseringstrykstyring� COP 5,9 ved Pc= 52 bar, UK3COP 5,9 ved Pc= 52 bar, UK3COP 5,9 ved Pc= 52 bar, UK3COP 5,9 ved Pc= 52 bar, UK3� 30 kW VGV kapacitet30 kW VGV kapacitet30 kW VGV kapacitet30 kW VGV kapacitet� Effektoptag 20,3 kWEffektoptag 20,3 kWEffektoptag 20,3 kWEffektoptag 20,3 kW

� VGV mode60

70

80

90

100

110

120

130

T [°

C]

0,0

017

0,0

1

0,0

19

0,0

34

0,0

63

m3/

kg

� VGV mode� COP 3,8 COP 3,8 COP 3,8 COP 3,8 � 80 bar/1580 bar/1580 bar/1580 bar/15ooooC ud af gaskølerC ud af gaskølerC ud af gaskølerC ud af gaskøler� 128 kW VGV 20C ud128 kW VGV 20C ud128 kW VGV 20C ud128 kW VGV 20C ud� Effektoptag 35 kWEffektoptag 35 kWEffektoptag 35 kWEffektoptag 35 kW

� Ekstra el-effekt: � 15 kW til ca 100 kW varme15 kW til ca 100 kW varme15 kW til ca 100 kW varme15 kW til ca 100 kW varme� ”6,7 effektfaktor til VGV””6,7 effektfaktor til VGV””6,7 effektfaktor til VGV””6,7 effektfaktor til VGV” -1,8 -1,6 -1,4 -1,2 -1 -0,8 -0,6

-20

-10

0

10

20

30

40

50

60

s [kJ/kg-K]

T [°

C]

60 b a r

35 ba r

18 ,7 ba r

70 b a r

0 ,2

0 ,4 0 ,6 0 ,8 CarbonDioxide

Varmegenvinding fra transkritiske CO2-anlæg

40

50

60

70

80

Te

mp

era

ture

- w

ate

r, a

ir,

refr

ige

ran

t [°

C]

Heat recovery unit

mdot;ref=0,5 [kg/s]

Pgk=22 [bar]

mdot;luft=1,364 [kg/s]

mdot;vand=0,8 [kg/s] tgk;ind=70 [°C]

tluf t;ind=10 [°C]

tluf t;ud=15 [°C]

tvand;ind=30 [°C]

tvand;ud=50 [°C]

tref;intermidiate=29,57 [ ]

tvgv;ud=32,15 [ ]

COP (R404A) = 1,8

COP (R744) = 2,4 (85 bar)

Higher discharge gas temp

Pinch point R404A

24681012141618202224262830323436384042444648505254565860626466687072747678808284868890929496981000

10

20

30

Enthaly steps [0=ref entrance/ 100 ref exit]

Te

mp

era

ture

- w

ate

r, a

ir,

refr

ige

ran

t [°

C]

tvand[i]

50%50%

Heat recovery unit

Aircooled condenser

Qluf t=7,5 [kW]

Qvand=67,2 [kW]

AVGV=13,62 [m 2̂]

UAVGV=8,174 [kW * m 2̂]

Pinch point R744

compFORT 4x54 (50-100 kW) - chiller

Indendørsopstilling:

Anlægget: LxHxW =

2500x1500x1100 mm

Kompakt design

Vægt: 1500 kg

Kondensator er placeret udendørs

Oversvømmet fordamper, intern

VV, oliestyring, HT-styring,

tørrefilter, sugefilter, smudsfilter

System lay-outs for AC

National arena in Copenhagen – AC with DX CO2Luftkonditionering: 3xcompFORT S 8x0

Anlægstype: Gas-by-pass, DX

Kapacitet: 3 x 300 kW

Fordampertemperatur: 7-8ºC

Lufttemperatur: 15ºC

Økonomi: 20% besparelse på installationen

Energibesparelse: ca. 15% sammenlignet med

de bedste HFC-chillerede bedste HFC-chillere

Industrielle applikationer - Måkestad

Køl og frys af frugt og grønt:

2xcompSUPER XL 6x3

Anlægstype: Booster med gas-by-pass, DX

Kapacitet: 2 x 150/50 kW

Fordampertemperatur: -10ºC/ -35ºC

Økonomi: 20% besparelse på installationen

Energibesparelse: ca. 20%

Sammenlignet med HFC kaskadeanlæg

Måkestad

Why CO2 in heat pumps

2,4

2,6

2,8

3,0

3,2

3,4

3,6

3,8

4,0

CO

P [

-] COP_NH3

COP_propan

COP_CO2

� Vand_ind = 30 °C

� T_e = 0 °C

� eta_komp = 0,65

2,0

2,2

2,4

50 60 70 80 90

Vandtemperatur ud [C]

Brugsvandsvarmepumper / industrivarmepumper

50

60

70

80

90

100

110

120

130

T [°C

]

0,0

017

0,0

1

0,0

19

0,0

34

0,0

63

m3/

kg

� Brugsvandvarmepumpe� Fordampning Fordampning Fordampning Fordampning ----10101010ooooC til 20C til 20C til 20C til 20ooooCCCC� Varmt vand op til 80Varmt vand op til 80Varmt vand op til 80Varmt vand op til 80----85858585ooooCCCC

� Afkøling af kølemiddel i gaskøleren er vigtigt

� Optimalt tryk i

COP 4,0

-1 ,7 -1,6 -1,5 -1,4 -1,3 -1,2 -1,1 -1 -0,9 -0,8-20

-10

0

10

20

30

40

50

s [kJ/kg-K]

T [°C

]

6 0 b a r

3 5 b a r

1 8 ,7 b a r

7 0 b a r

0 ,2

0 ,4 0 ,6 0 ,8 C arbonD ioxide

� Optimalt tryk i gaskøleren er vigtigt

� Intern varmeveklser er bl.a. redskab til høj udgangstemperatur på vandsiden

Fordampning: 0oC, Vand ind/ud= 10oC/ 80oC

Optimal drift af gaskøleren

0 4 8 12 16 2040

50

60

70

80

90

100

110

120

Tem

pera

ture

[°C

]

Refrigerant

WaterWater

0 4 8 12 16 2040

50

60

70

80

90

100

110

120

Tem

pera

ture

[°C

]

Refrigerant

WaterWater

120 bar, COP 3.8 105 bar, COP 3.4

� T_v_ind/ ud = 40/ 80oC, Fordampning 10oC

0 4 8 12 16 20

Step (Counter flow)

0 4 8 12 16 200

5

10

15

20

1600

1800

2000

2200

2400

2600

2800

3000

Step[i]

LM

TD

[i]

αα ααi[

i]

0 4 8 12 16 20

Step (Counter flow)

0 4 8 12 16 200

5

10

15

20

1600

1800

2000

2200

2400

2600

2800

3000

Step[i]

LM

TD

[i]

αα ααi[

i]

Varmepumpe – Lyckeby Stärkelse (SE)

280 kW varme, vand ind/ud: 30/70oC

compHEAT 4-IKV, layout: 1.000 kW heat production

Advantages with Advansor systems

� Safety

• Reliability

� Safety valves and pressostats

� CE marked in accordance with PED

� High level of documentation

� Education during first startup

� Tested and documented components

� Optimal control and surveillance – open platform (Danfoss)

� Protection against liquid slug and optimal oil management

� Pack control ensures stable suction pressure

� Pressure management during electrical cut-out (standstill pressure)

� Only CO2 as refrigerant – no brine or water circuits

� Simple design with DX configuration

� Easy installation with cobber pipes and AKV-valves

� With CO2 there no restriction regarding installation

� Low cost

� Low running cost � Lowest energy consumption

� Cheap refrigerant

� Easy and cheap installation

� Easy to service – low service cost

� Heat recover (100%)

� Free cooling