india cement tool-final

7/24/2019 India Cement Tool-final

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Calculating GHG Emissions from the Indian Cement Industry.Version1.0. April 2005. Developed by The Energy and Resources InstituteTERI! and the "orld Resources Institute "RI! and copyrighted.

Available at ###.ghgprotocol.org.

User Agreement

By using the Spreadsheets and associated materials in any manner, theUser agrees to the following terms of this agreement:

Copyright: The Spreadsheets and associated guidance were developedby TER and !R, and are copyrighted" The User ac#nowledges thesecopyrights"

$c#nowledgement: The User agrees to ac#nowledge TER and !Rfor their role in developing the Spreadsheets whenever the User authorsreports or publications based in whole or in part on the use of theSpreadsheets"%isclaimer: The use of these tools is not a guarantee of an accurate orcomplete greenhouse gas emissions inventory" To develop a high &ualityinventory, it is essential to plan an inventory &uality system that includessuitable internal and e'ternal reviews, and accuracy chec#s for activitydata, emissions factors, and emissions calculations"


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thodology ased upon I!CC guidelines:"he #$C%& CO2 !rotocol

elines

methodology ased on )%E!A climate*ise program

6orld Resources institute (6RI)

!/ 0treet, NE (0uite !!)

70

Tel# (%!%) 8%$ 8'!!a*# (%!%) 8%$ 8'!

ttention# .r 9an:a;


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tors &or various &uels used in the plant e.g coal' lignite' #aste &uels' 9!.

eration!' direct &iring &or drying' etc.

level.

ny level.

ous &uels used internationally.

ctors.

r)boo).

a ce$ent $anu&acturting plant. These #or)sheets should be used a&ter studying inblished by "RI"/D that gives in detail the +,+ accounting and reporting principles

s the ce$entclin)er $anu&acturing plants in using the various #or)sheets that &ollo# in

lant and other basic data related to production that is used &or esti$ating the 2e$issions.

ci&ic e$ission &actors &or 2 e$ission due to calcination o& li$estone! that #ill be used

cination o& ra# $aterials.

the &uel burnt in the )ilnprecalcinator as #ell as in other stationary co$bustion

ious co$pany o#ned vehicles including ;uarry e;uip$ent.

ns accruing &ro$ the electricity purchased &ro$ the grid.

ns accruing &ro$ the clin)er purchased &ro$ other &acilitiesplants.

he ce$ent process ra# $aterials! and &uel co$bustion.

r India &or process' co$bustion' electricity etc.! that can be used in absence o&.


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Annual

0


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Annual

Buarterly

@onthly


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@g content FHG

a a$ount FtonnesG

@g a$ount FtonnesG

0te3 %b# Raw 1aterial = %

Ra# $aterial consu$ed oal ash! FtonnesGa content FHG

@g content FHG

a a$ount FtonnesG

@g a$ount FtonnesG

add data &or ra# $aterials and &uels 8 4 n' as appropriate!

0te3 %c# Total o4 raw 1aterials

Total ra# $aterial consu$ed FtonnesG

Average a content FHG

Average @g content FHG

Total a a$ount FtonnesGTotal @g a$ount FtonnesG

Ft 2G

Ft 2G

Ft 2G

E$ission &actor' uncorrected F)g 2t cliG

F)g 2t cliG

Dust E1issions

D lost FtonnesG

Degree o& calcination o& D H

r

Notes#

tep 8b7 Average clin)er production &actor &or your plant ($8)g clin)er!

0te3 "# C>%e1issions 4ro1 raw 1aterial calcination

bsolute C>%e1issions

3ncorrected 2e$issions' based on a4

and @g content o& clin)er

orrection &or i$ports o& a and @g via ra#$aterials etc.orrected' direct

2e$issions

03eci4ic C>%e1issions 3er ton o4 clin:er

E$ission &actor' corrected &or a4 and @gi$ports

03eci4ic C>%e1issions 4actor o4 CAD

E$ission &actor' calculated based upon the

degree o& calcination o& )iln dust Ft 2t DG

J)g 2t DK

1. 3nder the section' Dust E$issions' use a de&ault value o& ?0H &or degreepreheater' in case actual value is not )no#n.

2 3nder the section Dust E$issions' the D lost tonnes! is calculated basee$ission &ro$ your plant or dust e$ission nor$s speci&ied by the -ollution oloss can be arrived at using the under$entioned procedure7

tep 8a7 Actual dust e$ission average! or Dust e$ission nor$s speci&ied &or

your plant in $g($8!


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In case this &igure is not available' use a de&ault value o& 1.5 ($8 o& &lue gase

tep 8d7 alculate dust e$issions tonnes o& dust !

tep 8c7 alculate dust e$issions per )g clin)er produced $g dustreleased)g clin)er!


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100.1

>:.8

5


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0

0

0

0

0

0.00

0.00

00

0

0

0

0

0

0

?0.00

0.00

0

F$g($8G 150F($8g clin)erG 1.50

& calcination o& )iln dust leaving the

d upon the average actual dusttrol /oard &or your plant!. The dust


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tep 8

C

E1ission actor N / O 8P


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6or:sheet 4or calculating#

I13ortant notes 4or using this wor:sheet#

o$panies can esti$ate direct process e$issions &ro$ the calcination o& ra#

Colour code#

3ser entry7 Input data related to production activity

3ser entry7 Input data related to &uel usee$ission &actorstandard values or dat

3ser entry7 -hysical units

Auto calculated value7

6hich 1ethod do you 3lan to useB

Clin:er based 1ethodology# es

Ce1ent based 1ethodology# No

.ethod # Clin:er-RA0HEET# To Deter1ine Direct /ross Carbon Dio*ide E1

Clin:er-%e1issions 4ro1 clin:er 1anu4acturing

@ethod 17 This $ethod is based on the actual clin)er produced and it is reco$process based e$issions.The 2 e$issions #ill directly be calculated i& you h&actor in the previous #or)sheet.

@ethod 27 This $ethod is based on actual ce$ent production in the &acility andclin)er production is not available.

In both the $ethods' it is reco$$ended that actual plant speci&ic e$ission &actthe calculation tools.It is reco$$ended to use @ethod 1' i& the clin)er productio

De&ault calcination &actors can be used only i& plant speci&ic data is not availablplant speci&ic values and de&ault values should only be used i& plant speci&ic val

Clin:er 9roduction(tonnes)

Carbon Dio*ideE1ission actor 4or

clin:er(:g C>

%tonne

clin:er 3roduced)

CAD lost(tonnes)

olu$n /7 The carbon dio*ide e$ission &actor &or clin)er in )g toe$ission &actor is used here.3se the de&ault values o& )g

2to

based upon the location o& the plant! only in case the plant speci&

olu$n D7 The arbon Dio*ide e$ission &actor &or D in )g

e$ission &actor is used here. 3se a de&ault values as given in theavailable.


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aterials by either o& the &ollo#ing $ethods7

a &ro$ other #or) sheet

issions 4ro1 Ce1ent 9roduction

tep : tep 5

D E

AO/!1000OD!1000!

0 0

$ission 6actor and is given in units tonnes o& clin)er produced

usto$ process e$ission &actor is used here.

3rocess (only due to raw 1aterial calcination)

ended to use this $ethod &or calculating theave already calculated the custo$i%ed e$ission

should be used only in cases #here data on actual

rs custo$ process e$ission &actor! are used inn data is available.

.i$ilarly other input para$eters should also beues are not available.

Carbon Dio*ideE1issions actor 4or

CAD(:g C>

%tonnes CAD

lost)

Carbon Dio*ideE1issions(tonnes)

nne clin)er produced! as calculated in the #or)sheet custo$ processnne o& clin)er as given in the table o& the De&ault E$ission 6actor sheet

ic &igures are not available.

2tonne o& D e$itted! as calculated in the #or)sheet custo$ process

#or)sheet De&aults e$ission &actor in case custo$i%ed E6 are not


28/80

issions 4ro1 Ce1ent 9roduction

lin)er to e$ent Ratio H! 4 100H portland output ?5Hlin)er to ce$ent ratio H! 4 -ortland -o%%olna e$ent =5H

lin)er to e$ent Ratio H! 4 -ortland lag ce$ent 55H

Tonne o& Ra# @aterial per Tonne o& lin)er 1.50

=>H

tep > tep ? tep 10 tep 11 tep 12

H I F A L

onstant , * I * L * C

1.5 =>.00 0.:: 0.51 :>:1


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es

(o


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Color code3ser entry7 ource &uel description

De&ault values



Direct e1issions 4ro1 4ossil 4uel co1bustion

tep 1 tep 2 tep 8

< C

E*a$ple7 iln oal 188000 tonnes 22.50

ossil uel ty3e

iln 1 tonnes

iln 2 tonnes

-recalcinator1 litre

-recalcinator2 litre

D+ et litre

anteen litre

Any other source tonnes

tonnes

Notes#

+ The direct e1issions associated with stationary co1bustion should be re3orted

as direct e1issions 4ro1 stationary sources+

%+ ll 4ossil 4uels used in :iln, 3recalcinator, D/ sets etc to be entered as se3arate

bio1ass 4uels to be re3orted se3arately

Direct e1issions 4ro1 co1bustion o4 bio1ass based 4uels

0co3e# Direct C>%e1issions 4ro1 4uel co1bustion 4ro1 di44er

3ser entry7 6uel use e$ission &actorvalues

TotalGuantity o4

4uel burned

7nit used to1easure

Guantity o44uel use

?erage netcalori4ic ?alue

0ourcedescri3tion

"+


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tep 1 tep 2 tep 8

< C

E*a$ple7 iln /a$boo dust :5000 tonnes 15.25

ossil uel ty3e

iln 1 tonnes

iln 2

-recalcinator1

-recalcinator2

Any other source

TotalGuantity o4

4uel burned

7nit used to1easure

Guantitiy o4

4uel use

?erage netcalori4ic ?alue

0ourcedescri3tion


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tep : tep 5 tep < tep = tep > tep ?

D E / H I

A O

+Ltonne 2??2500 +L >?.5< 1.00

+Ltonne 0 +L

+Ltonne 0 +L

+Llitre 0 +L

+Llitre 0 +L

+Llitre 0 +L

+Llitre 0 +L

+Ltonnes 0 +L

+Ltonnes 0 +L

tep 11

in 0co3e

entries in the abo?e calculation table

nt stationary sources

7nit o4 netcalori4ic ?alue

uantity o44uel used

in energy

7nit o4Guantityo4 4uelusedin energy

C>%Co1bustion

E1ission actor

7nit o4 C>%

e1ission 4actor

>*idi@edcarbon4raction

)g 2+L

)g 2+L

)g 2+L

)g 2+L

)g 2+L

)g 2+L

)g 2+L

)g 2+L

)g 2+L

0u1 C>%e1issions ton

ng table+ The C>%e1issions 4ro1 use o4 such


36/80

tep : tep 5 tep < tep = tep > tep ?

D E / H I

A O

+Ctonnes %

e1ission 4actor

>*idi@edcarbon4raction

)g 2+L

)g 2+L

0u1 C>%e1issions ton


37/80

tep 10

F A

E O + O I L 1P000

2'021'


38/80

tep 10

F A

E O + O I L 1P000


39/80


I13ortant notes 4or using this wor:sheet#

o$panies can esti$ate direct $obile e$issions by either o& the &ollo#ing $eth

@ethod 17 This $ethod is based on the actual &uel cosu$ption in vehicles.

@ethod 27 This $ethod is based on distance run by the vehicle.

Color code

3ser entry7 ource &uel description

De&ault values



6hich 1ethod do you 3lan to useB

ctual 4uel consu13tion based 1ethodology

Distance based 1ethodology

.ethod # E1ission calculated based on actual 4uel consu13

tep 1 tep 2

%e1issions 4ro1 4uel co1bustion 4ro1

sources+

3ser entry7 6uel use e$ission &actorvalues

uantity o4 4uelburned

7nit used to1easure Guantitiy

o4 4uel use

0ourcedescri3tion


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Notes#

+ The 4uel used in ?arious ?ehicles should be entered se3arately as inde3endent e

.ethod %# E1ission calculated based on distance tra?el

tep 1 tep 2 %e1ission 4actor using the e1ission 4actors 3ro?ided in the 6or:sheet

C>%e1ission 4actor

)g 2)$

0u1 C>%e1issions tonnesJ#

+ 7se only custu1ised C>%e1ission 4actor since :g C>

%:1 is ?aried wit

%+ or 1ore details on distance based e1ission see Calculating C>%e1iss


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ntries+

tep 8C

Total e1issions

1etric tonnes

A * / 1000

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

0.0

KDe4ault E1ission actorsK+

the ?ehicle ty3e, ?ehicle age, loading, road condition etc++

ions 4ro1 1obile co1bustion tool


43/80


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6or:sheet 4or calculating #

Color code#

3ser entry7ource &uel description


tep 1 tep 2

0000000 >0%e1issions due to electricity 3urchased

3ser entry7 6uel use e$ission&actor values

Electricity

9urchased (:6h)

C>%e1ission 4actor

(gra1sC>

% :6h)

0u1 C>%e1issions tonnesJ #


50/80


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Color code#

3ser entry7ource &uel description

3ser entry7 6uel use e$ission &actor values

De&aultstandard values


tep 1 tep 2 tep 8

< C

A O / 1000

0 >0< 0

0co3e"# Indirect C>%e1issions due to clin:er i13orted by the 3lant

Clin:er i13orted(tonnes)

De4ault direct

E1issions actor4or clin:er

(:g C>%tonnes

clin:er 3roduced)

Carbon Dio*ideE1issions(tonnes)


52/80


Colour code



De&aultstandard values



tep 1a tep 1b tep 1c

< C D

A O / 1000

E*a$pleM 20000 0.80 %e1issions 4ro1 the ce1ent 3lant

0te3 # Direct 0>%e1ission 4ro1 the 3rocess (1easured ?alue 4ro1 :iln sta

Ce1ent9roduction

(tonnes)

0ul3hur Dio*ide E1issionactor 4or ce1ent

(:g 0>%tonne ce1ent

3roduced)

0ul3hur Dio*ideE1ission (:g 0>

%)

0ul3hurDio*ide

E1ission(t 0>

%)

0ul3hur dio*ide e1ission 4actor 4or ce1ent 3rocess ?aries 4ro1 3lant to 3lant as the sul3hdata is a?ailable, co13lete 0te3 otherwise, lea?e it blan:+

0te3 %# Direct 0>%e1issions 4ro1 stationary 4uel co1bustion (4ro1 non-:iln

uantity o4 4uelburned (tonnes)

0ul3hurcontent

(wt)

0ourcedescri3tion


53/80


54/80

tep 2c tep 2d

D E

/ O E 1000

11.00 1'100

0.00 0

0.00 0

0.00 0

0.00 00.00 0

:)

ur content o4 raw 1aterials ?aries+I4 3lant-s3eci4ic 1easured

sources)

Ty3ical density(gc1") at C

0>%e1ission

4actor(:g 0>

%

tonne)

0>%

e1issions(tonnes)


55/80

0.00 0

0.00 0

0.00 0

0.00 0

!

tep 8b tep 8c tep 8d

D E /

/ O 6 10001.>0 0.>< 0.08 0.%e1issions

Indirect e$issions &ro$ i$ported clin)er tonnes 2!

Direct e$issions &ro$ bio$ass burning tonnes 2!

Total direct 2e$issions tonnes!


57/80

4

4

Annual12801>??

4

0

0

0

0

0

0

0

0

ility+


58/80

6or:sheet

Note# The 4acility le?el data in this sheet related to C>% e1ission should be ta:en 4ro

Colour code




o$pany na$e

rganisational boundaries choosen

Reporting period

tart report ti$e

End report ti$e

tep 1 tep 2 tep 8 tep : tep 5a tep 5b tep 5c

acility

< C D E /

0 or 100H Tonnes

/i?ing a su11ary o4 total C>%e1ission 4ro1 the co13any+

Control()

EGuity0hare ()

9roduction o4ce1ent

0co3e# Direct C>%e1issi

Directprocessrelated

e$issionstonnes

2!

Direct

e$issions&ro$

stationaryco$bustion tonnes

2!

Direct

e$issions&ro$

$obilesourcestonnes

2!


59/80

tep ? 0 0 0 0Total &orco$pany


60/80

the res3ecti?e 4acility le?el su11ary in?entory wor:sheets+

tep 5d tep < tep = tep >

H I F A L

0 0

0 0

0 0

0 0

0 00 0

ons0co3e %#

Indirect C>%

e1issions

0co3e "#Indirect C>

%

e1issions

0co3e 4or

control

0co3e4or eGuity

Totaldirect

e$issionstonnes

2!

Indirecte$ission

&ro$purchasedelectricity

tonnes 2!

Indirecte$ission

&ro$i$portedclin)er

tonnes 2!

Absolute

2

per stage

Absolute

2

per stage


61/80

0 0

0 0

0 0

0 0

0 0

0 0

0 0

0 0 0 0 0


62/80

Re4erence wor:sheet #

De4ault e1ission 4actors

tate

Raasthan 580.=2

@-hattisgarh 52:.2?

+uarat 581.=0

@aharashtra 581.1>

Andhra -radesh 588.02

arnata)a 58:.5>

Ta$il (adu 58


63/80

Aviation gasoline


64/80

ource7 1. 3E-A report (o. E-A4

6uel

+asoline I7 2=?2! :.00

6urnace oil @V2! I7 15?841?>2! :.00

6urnace oil ,V1! I7 15?841?>2! :.50

Ci;ue&ied petroleu$ gas C-+! I7 :5= 0.02

ource7 Respective /I standards and Technical $e$ento 4Ther$a*

Table'# 0tate wise sul3hur content and 0>%e1ission 4actor o4 co

content#t H!

Table8# 0ul3hur content and 0>%e1ission 4actor o4 3etroleu1 4u

content#t H!


65/80

:58.5>

::>.85

:5:.8=

:58.?5

:55.::

:5.1:

:51

::0.50

:58.?

::0.50

::2.21

1022 :8.5 ::.0= 0.>1::.5?00

e1ission 4actor 4or CAD

2e$ission &actor &or D

)g 2tonne D lost!

e

2e$ission &actor)g

2 +L!

0ection + Heating ?alues are 4ro1 9I, %!!+ 5alues in other colu1ns is deri?ed

Ty3icaldensity

(Deri?ed)

Ag C>%litre gra1c1

"

(9I, %!!)


66/80

0.08:8

0.08=1 2.=:5> ::.1:

0.08=1 2.=:5> :8.?211 0.>:

0.08=? 2.>050 0.00

0.08?= 8.0> 8?.?585 0.??

0.0:05 8.180= :0.=5>< 0.??

0.02:? 1.5=8= :5.?==? 0.5:

0.08>2 2.=??8

0.02>. 0.0000 0.5>

0.02:0 :=.88=8 0.51

28.58 O

eating values are &ro$ A-I' 2001. Values in other colu$ns is derived arith$atically e*cept as co$$ent

>00

?80

=50

11?0

8 0.01 0.2

10=.2: 0.05 1

?>.2> (A (A

1=0.15 (A (A

2.>11: )g2)g

2.>5=< )g 2)g

0.08? +L standard cubic$eter

E$ission &actorgra$ o&

2"h!

2e$ission &actor g

2+L!

2E$ission&actor g

2tonne!

and 2respectively.


67/80

4he$ical haracterisation' Revised 2nd edition' 1??=

=?

10.240.>0.0 0.>?40.?5

>0.0 0.>?40.?5

?0.0 0.>?40.?5

0.:0

rivate Ci$ited.

l and lignite in India+

2e$ission &actor

g2tonne!

ls and natural gas in india+

2e$ission &actor g

2tonne!

Typical density gc$8! at150


68/80


69/80

ed.


70/80


71/80

Re4erence wor:sheet %#

or de4ault ?alues 4or energy content (HH5) and carbon conten

uel ty3e Higher heating ?alue Carbon, by weight

+asoline petrol 0.08< >5.50

erosene 0.08> >>.=0

Residual &uel oil (o.< 0.0:8 >>.80

C-+ 0.02.0.8.1.5.00

(atural gas 0.08?11 +Lcubic $eter


72/80


73/80

Re4erence wor:sheet "#

Con?ersion actors

.ass

1 pound lb! :58.< gra$s g!

1 )ilogra$ )g! 2.205 pounds lb!

1 short ton ton! 2P000 pounds lb!

1 $etric ton 2P205 pounds lb!

5olu1e

=.:>05 gallons gal!

2>.82 liters C!

1 gallon gal! 0.028> barrel bbl!

1 barrel bbl! :2 gallons gal!

1 litre C!

?= barrels bbl!

Energy

1 )ilo#att hour )"h! 8:12 /tu btu!

1 $egaoule @L! 0.001 gigaoules +L!

1 gigaoule +L! 0.?:=> $illion /tu $illion btu!

1 /tu btu! 1P055 oules L!

1 $illion /tu $illion btu! 1.055 gigaoules +L!

1 ther$ ther$! 100P000 btu

1 )cal :.1>< )L

>ther

)ilo 1P000

$ega 1P000P000

giga 1P000P000P000

tera 1P000P000P000P000

1 psi 0.0?5 bar

0.?>0= bar

1 at$osphere at$! 1.01825 bar

1 $ile statue! 1.


74/80


75/80

0.:58< )ilogra$s )g! 0.000:58< $etric tons tonne!

?0=.2 )ilogra$s )g!

1P000 )ilogra$s )g! 1.1028 short tons tons!

0.1=>1 barrel bbl!

8.=>5 liters C!

15>.?? liters C!

0.2


76/80


77/80

Listed below are the 1acros included in this wor:sheet 4or re4erence 3ur3oses+ 9lease do not 1odi4y this

ub ,idedirect$eth1!

PP ,idedirect$eth1 @acro

@acro recorded :112005

P

P

RangeA287I8?!.elect

Active"indo#.$allcroll Do#n7N8

election.EntireRo#.,idden N True

Activeheet.hapes+roup 2>!.elect

election.hapeRange.rder $soend/ac)#ard

RangeE22!.elect

End ubub 3nhide@eth1process!

P

P 3nhide@eth1process @acro

@acro recorded :112005

P

P

Ro#s227:0!.elect

End ub

ub 3nhide$eth2process!

P

P 3nhide$eth2process @acro@acro recorded :112005

P

P

Ro#s:17


78/80


Activeheet.hapes+roup 22!.elect


RangeI22!.elect

End ub

ub 3nhide$eth1$obile!

PP 3nhide$eth1$obile @acro

P @acro recorded :112005 by yste$ Ad$inistrator

P

P

Ro#s227:7=8!.elect


Activeheet.hapes+roup 1?!.elect


Range+:=!.electEnd ub

ub 3nhide$eth2$obile!

P

P 3nhide$eth2$obile @acro

P @acro recorded :112005 by yste$ Ad$inistrator

P

P

Ro#s:=7=:!.elect

election.EntireRo#.,idden N 6alse

Range+:=!.elect

Activeheet.hapes+roup 1


79/80

sheet+


80/80

india cement tool-final

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