India Cement Tool-final
Transcript of 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
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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$ent 55H
Tonne o& Ra# @aterial per Tonne o& lin)er 1.50
=>H
tep > tep ? tep 10 tep 11 tep 12
H I F A L
onstant , * I * L * C
1.5 =>.00 0.:: 0.51 :>:1
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es
(o
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6or:sheet 4or calculating#
Color code3ser entry7 ource &uel description
De&ault values
3ser entry7 -hysical units
Auto calculated value7
Direct e1issions 4ro1 4ossil 4uel co1bustion
tep 1 tep 2 tep 8
< C
E*a$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$boo dust :5000 tonnes 15.25
ossil uel ty3e
iln 1 tonnes
iln 2
-recalcinator1
-recalcinator2
Any other source
TotalGuantity o4
4uel burned
7nit used to1easure
Guantitiy o4
4uel use
?erage netcalori4ic ?alue
0ourcedescri3tion
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tep : tep 5 tep < tep = tep > tep ?
D E / H I
A O
+Ltonne 2??2500 +L >?.5< 1.00
+Ltonne 0 +L
+Ltonne 0 +L
+Llitre 0 +L
+Llitre 0 +L
+Llitre 0 +L
+Llitre 0 +L
+Ltonnes 0 +L
+Ltonnes 0 +L
tep 11
in 0co3e
entries in the abo?e calculation table
nt stationary sources
7nit o4 netcalori4ic ?alue
uantity o44uel used
in energy
7nit o4Guantityo4 4uelusedin energy
C>%Co1bustion
E1ission actor
7nit o4 C>%
e1ission 4actor
>*idi@edcarbon4raction
)g 2+L
)g 2+L
)g 2+L
)g 2+L
)g 2+L
)g 2+L
)g 2+L
)g 2+L
)g 2+L
0u1 C>%e1issions ton
ng table+ The C>%e1issions 4ro1 use o4 such
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tep : tep 5 tep < tep = tep > tep ?
D E / H I
A O
+Ctonnes %
e1ission 4actor
>*idi@edcarbon4raction
)g 2+L
)g 2+L
0u1 C>%e1issions ton
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tep 10
F A
E O + O I L 1P000
2'021'
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tep 10
F A
E O + O I L 1P000
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6or:sheet 4or calculating#
I13ortant notes 4or using this wor:sheet#
o$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 $ethod is based on distance run by the vehicle.
Color code
3ser entry7 ource &uel description
De&ault values
3ser entry7 -hysical units
Auto calculated value7
6hich 1ethod do you 3lan to useB
ctual 4uel consu13tion based 1ethodology
Distance based 1ethodology
.ethod # E1ission calculated based on actual 4uel consu13
tep 1 tep 2
%e1issions 4ro1 4uel co1bustion 4ro1
sources+
3ser entry7 6uel use e$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
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6or:sheet 4or calculating #
Color code#
3ser entry7ource &uel description
Auto calculated value7
tep 1 tep 2
0000000 >0%e1issions due to electricity 3urchased
3ser entry7 6uel use e$ission&actor values
Electricity
9urchased (:6h)
C>%e1ission 4actor
(gra1sC>
% :6h)
0u1 C>%e1issions tonnesJ #
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6or:sheet 4or calculating #
Color code#
3ser entry7ource &uel description
3ser entry7 6uel use e$ission &actor values
De&aultstandard values
Auto calculated value7
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)
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6or:sheet 4or calculating #
Colour code
3ser entry7 ource &uel description
3ser entry7 6uel use e$ission &actor values
De&aultstandard values
3ser entry7 -hysical units
Auto calculated value7
tep 1a tep 1b tep 1c
< C D
A O / 1000
E*a$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
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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)
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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!
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4
4
Annual12801>??
4
0
0
0
0
0
0
0
0
ility+
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6or:sheet
Note# The 4acility le?el data in this sheet related to C>% e1ission should be ta:en 4ro
Colour code
3ser entry7 ource &uel description
3ser entry7 6uel use e$ission &actor values
Auto calculated value7
o$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$
$obilesourcestonnes
2!
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tep ? 0 0 0 0Total &orco$pany
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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
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0 0
0 0
0 0
0 0
0 0
0 0
0 0
0 0 0 0 0
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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$il (adu 58
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Aviation gasoline
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ource7 1. 3E-A report (o. E-A4
6uel
+asoline I7 2=?2! :.00
6urnace oil @V2! I7 15?841?>2! :.00
6urnace oil ,V1! I7 15?841?>2! :.50
Ci;ue&ied petroleu$ gas C-+! I7 :5= 0.02
ource7 Respective /I standards and Technical $e$ento 4Ther$a*
Table'# 0tate wise sul3hur content and 0>%e1ission 4actor o4 co
content#t H!
Table8# 0ul3hur content and 0>%e1ission 4actor o4 3etroleu1 4u
content#t H!
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:58.5>
::>.85
:5:.8=
:58.?5
:55.::
:5.1:
:51
::0.50
:58.?
::0.50
::2.21
1022 :8.5 ::.0= 0.>1::.5?00
e1ission 4actor 4or CAD
2e$ission &actor &or D
)g 2tonne D lost!
e
2e$ission &actor)g
2 +L!
0ection + Heating ?alues are 4ro1 9I, %!!+ 5alues in other colu1ns is deri?ed
Ty3icaldensity
(Deri?ed)
Ag C>%litre gra1c1
"
(9I, %!!)
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0.08:8
0.08=1 2.=:5> ::.1:
0.08=1 2.=:5> :8.?211 0.>:
0.08=? 2.>050 0.00
0.08?= 8.0> 8?.?585 0.??
0.0:05 8.180= :0.=5>< 0.??
0.02:? 1.5=8= :5.?==? 0.5:
0.08>2 2.=??8
0.02>. 0.0000 0.5>
0.02:0 :=.88=8 0.51
28.58 O
eating values are &ro$ 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.
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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
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ed.
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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 $eter
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Re4erence wor:sheet "#
Con?ersion actors
.ass
1 pound lb! :58.< gra$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 $ile statue! 1.
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0.:58< )ilogra$s )g! 0.000:58< $etric tons tonne!
?0=.2 )ilogra$s )g!
1P000 )ilogra$s )g! 1.1028 short tons tons!
0.1=>1 barrel bbl!
8.=>5 liters C!
15>.?? liters C!
0.2
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Listed below are the 1acros included in this wor:sheet 4or re4erence 3ur3oses+ 9lease do not 1odi4y this
ub ,idedirect$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
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election.EntireRo#.,idden N True
Activeheet.hapes+roup 22!.elect
election.hapeRange.rder $soend/ac)#ard
RangeI22!.elect
End ub
ub 3nhide$eth1$obile!
PP 3nhide$eth1$obile @acro
P @acro recorded :112005 by yste$ Ad$inistrator
P
P
Ro#s227:7=8!.elect
election.EntireRo#.,idden N True
Activeheet.hapes+roup 1?!.elect
election.hapeRange.rder $soend/ac)#ard
Range+:=!.electEnd ub
ub 3nhide$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
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sheet+
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