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-3
2561
1 PM AIR COMPRESSOR @KBY 1 YR PLAN Punyaphat S.
ACTUAL Jiratchaya W.
2 PM BOIL OFF & TRANSFER REFRIG. 1 YR PLAN Punyaphat S.
COMPRESSOR @KBY ACTUAL Jiratchaya W.
3 PM AIR HEATER @KBY 1 YR PLAN Nuttakit P.
ACTUAL Chirawat S.
4 PM CRANE @KBY 6 M PLAN Rachatham A.
ACTUAL Wirat N.
5 PM ENGINE GENERATOR @KBY 1 YR PLAN Thanat K.
ACTUAL Nuttakit P.
6 PM RUBBER FENDER @KBY 1 YR PLAN Jiratchaya W.
ACTUAL Montree T.
7 PM LOADING ARM @KBY 6 M PLAN Chirawat S.
ACTUAL Montree T.
8 PM JETTY @KBY 1 YR PLAN Niti P. GL
ACTUAL Kittipong S. GS
9 PM PV VENT @KBY 1 YR PLAN Thanaphon S.
ACTUAL Montree T.
10 PM PUMP @KBY 1 YR PLAN Punyaphat S.
ACTUAL Thanat K.
11 PM SAFETY VALVE @KBY 1 YR PLAN Nuttakit P.
ACTUAL Montree T.
1A, 1B
1A, 1B
1A, 1B
,
3 A, B
OCT NOV
11 12REMARK
JAN FEB MAR APR MAY DECJUNNo. MACHINE AND EQUIPMENT FREQ MONTH
1 9
AUGJUL SEP
: 3
:...1 ..2561...
2561
3 4 5 7 8 10
(PREVENTIVE MAINTENANCE YEAR PLANNER 2018)
PLANT :
MACHINE : MECHANICAL & CIVIL
62
Rev.1 (20/07/58) 1/2 F- . .-0030 (1/1)
OCT NOV
11 12REMARK
JAN FEB MAR APR MAY DECJUNNo. MACHINE AND EQUIPMENT FREQ MONTH
1 9
AUGJUL SEP
: 3
:...1 ..2561...
2561
3 4 5 7 8 10
(PREVENTIVE MAINTENANCE YEAR PLANNER 2018)
PLANT :
MACHINE : MECHANICAL & CIVIL
62
12 PM SAFETY VALVE @KBY 1 YR PLAN Nuttakit P.
ACTUAL Montree T.
13 PM SAFETY VALVE @KBY 1 YR PLAN Nuttakit P.
ACTUAL Montree T.
14 PM QUICK RELEASE HOOK @KBY 6 M PLAN Jiratchaya W.
ACTUAL Montree T.
15 PM . . 1 YR PLAN Niti P. GL
ACTUAL Chirawat S.
16 PM JETTY BRIDGE @KBY 1 YR PLAN Kittipong S. GS
ACTUAL Niti P. GL
( )( )( )
……………………………………………………………………………………
1A, 1B
…………………………………………
1A, 1B
1A, 1B
…...../….….../...….. …...../….….../...….. …...../…..…../...…..
. .
Rev.1 (20/07/58) 2/2 F- . .-0030 (1/1)
1 PM Lightning Arrester System 1 YR PLAN
ELK Project ACTUAL
2 PM MASS FLOW Meter LPG 4 MON PLAN
ELK Project ACTUAL
3 PM Ground System 1 YR PLAN ,
ELK Project ACTUAL
4 PM DCS 6 MON PLAN
ELK Project ACTUAL
5 PM ATG System 3 MON PLAN
ELK Project ACTUAL
6 PM GAS Analyser (GC Online) 3 MON PLAN
ACTUAL
7 PM Compact Prover 1 YR PLAN
ACTUAL
8 PM UPS 1 YR PLAN
ELK Project ACTUAL
9 PM Battery & Charger 1 YR PLAN
ACTUAL
10 PM PLC Process 1 YR PLAN
ELK Project ACTUAL
11 PM Generator 1 YR PLAN
ACTUAL
10 11 12
MAY
3 4 5 8
DECSEP OCT NOV
9No. MACHINE AND EQUIPMENT FREQ MONTH
1 2
JAN FEB AUGJUN JUL
: 2
:...1 ..2561...
2561
REMARKMAR APR
(PREVENTIVE MAINTENANCE YEAR PLANNER 2018)
PLANT :
MACHINE : ELECTRICAL & INSTRUMENT
6 7
Rev.2 (20/02/61) 1/3 F- . .-0030 (1/1)
10 11 12
MAY
3 4 5 8
DECSEP OCT NOV
9No. MACHINE AND EQUIPMENT FREQ MONTH
1 2
JAN FEB AUGJUN JUL
: 2
:...1 ..2561...
2561
REMARKMAR APR
(PREVENTIVE MAINTENANCE YEAR PLANNER 2018)
PLANT :
MACHINE : ELECTRICAL & INSTRUMENT
6 7
12 PM HVAC Sub 3 & Jetty 1 YR PLAN
ACTUAL
13 PM Gas Detector System 1 YR PLAN
ACTUAL
14 PM ESD 1 YR PLAN
ELK Project ACTUAL
15 PM SCADA 1 YR PLAN
ACTUAL
16 PM Transformer 1 YR PLAN
ELK Project ACTUAL
17 PM Cathodic Protection 1 YR PLAN
ELK Project ACTUAL
18 PM SIS 1 YR PLAN
ACTUAL
19 1 YR PLAN
ELK Project ACTUAL
20 PM Flow Computer 1 YR PLAN
ELK Project ACTUAL
21 PM FIRE ALARM SYSTEM 1 YR PLAN
ELK Project ACTUAL
22 PM Switch Gear + Capacitor 1 YR PLAN
ELK Project ACTUAL
Rev.2 (20/02/61) 2/3 F- . .-0030 (1/1)
10 11 12
MAY
3 4 5 8
DECSEP OCT NOV
9No. MACHINE AND EQUIPMENT FREQ MONTH
1 2
JAN FEB AUGJUN JUL
: 2
:...1 ..2561...
2561
REMARKMAR APR
(PREVENTIVE MAINTENANCE YEAR PLANNER 2018)
PLANT :
MACHINE : ELECTRICAL & INSTRUMENT
6 7
23 PM Navigation Aid System 1 YR PLAN
ACTUAL
24 1 YR PLAN
ACTUAL
25 PM MOV 2 YR PLAN . .2562
ACTUAL
26 PM Motor 2 YR PLAN . .2562
ACTUAL
27 PM Mass Flow Meter PIG TRAP 2 YR PLAN . .2563
ACTUAL
28 PM 1 1 YR PLAN
ACTUAL
PLAN
ACTUAL
PLAN
ACTUAL
( ) ( )
. .
…...../….….../...….. …...../…..…../...…..
Rev.2 (20/02/61) 3/3 F- . .-0030 (1/1)
1 PM AIR COMPRESSOR @SRC 1 YR PLAN Punyaphat S.
ACTUAL Jiratchaya W.
2 PM PV VENT & FLAME ARRESTOR @SRC 1 YR PLAN Thanaphon S.
ACTUAL Wirat N.
3 PM CRANE @SRC 3 M PLAN Rachatham A.
ACTUAL Wirat N.
4 PM ENGINE GENERATOR @SRC 1 YR PLAN Thanat K.
ACTUAL Nuttakit P.
5 PM RUBBER FENDER @SRC 1 YR PLAN Jiratchaya W.
ACTUAL Montree T.
6 PM LOADING ARM @SRC 6 M PLAN Chirawat S.
ACTUAL Montree T.
7 PM JETTY&SEABERTH @SRC 1 YR PLAN Niti P. GL
ACTUAL Kittipong S. GS
8 PM PUMP @SRC 1 YR PLAN Punyaphat S.
ACTUAL Wirat N.
9 PM SAFETY VALVE @SRC 1 YR PLAN Nuttakit P.
ACTUAL Montree T.
10 PM QUICK RELEASE HOOK @SRC 6 M PLAN Jiratchaya W.
ACTUAL Montree T.
11 PM @SRC 1 YR PLAN Montree T.
ACTUAL Niti P. GL
MAR APR MAY JUN JUL AUG
11 12REMARK
SEP OCT NOV DEC
5 6 7 8 9 10No. MACHINE AND EQUIPMENT FREQ MONTH
1 2
JAN FEB
3
2561
: 3(PREVENTIVE MAINTENANCE YEAR PLANNER 2018)
PLANT : :...1 ..2561...MACHINE : MECHANICAL & CIVIL
4
Rev.1 (20/07/58) 3/2 F- . .-0030 (1/1)
MAR APR MAY JUN JUL AUG
11 12REMARK
SEP OCT NOV DEC
5 6 7 8 9 10No. MACHINE AND EQUIPMENT FREQ MONTH
1 2
JAN FEB
3
2561
: 3(PREVENTIVE MAINTENANCE YEAR PLANNER 2018)
PLANT : :...1 ..2561...MACHINE : MECHANICAL & CIVIL
4
12 PM . . 1 YR PLAN Niti P. GL
ACTUAL Montree T.
13 PM JETTY BRIDGE @SRC 1 YR PLAN Kittipong S. GS
ACTUAL Niti P. GL
14 PM 1 YR PLAN Thanaphon S.
ACTUAL Nuttakit P.
14 PM WATER TREATMENT UNIT 1 YR PLAN Kittipong S. GS
ACTUAL Kittipong S. GS
. .
…...../….….../...….. …...../….….../...….. …...../…..…../...…..
………………………………………… ………………………………………… …………………………………………
( ) ( ) ( )
Rev.1 (20/07/58) 4/2 F- . .-0030 (1/1)
1 PM Mass Flow Jetty 4 MON PLAN .
ACTUAL
2 PM Lightning Arrester System 1 YR PLAN
ACTUAL
3 PM ATG System 3 MON PLAN
ACTUAL
4 PM Ground System 1 YR PLAN ,
ACTUAL
5 PM Fire Alarm System 1 YR PLAN
ACTUAL
6 PM ESD 1 YR PLAN
ACTUAL
7 PM PLC 1 YR PLAN
ACTUAL
8 PM Battery & Charger 1 YR PLAN
ACTUAL
9 PM Meter Truck Loading 6 MON PLAN
ACTUAL
10 PM Portable Gas Detector 1 YR PLAN
ACTUAL
11 PM Generator 1 YR PLAN
ACTUAL
10 11 12
MAY
3 4 5 8
DECSEP OCT NOV
9No. MACHINE AND EQUIPMENT FREQ MONTH
1 2
JAN FEB AUGJUN JUL
: 2
:...1 ..2561...
2561
REMARKMAR APR
(PREVENTIVE MAINTENANCE YEAR PLANNER 2018)
PLANT :
MACHINE : ELECTRICAL & INSTRUMENT
6 7
Rev.2 (20/02/61) 1/2 F- . .-0030 (1/1)
10 11 12
MAY
3 4 5 8
DECSEP OCT NOV
9No. MACHINE AND EQUIPMENT FREQ MONTH
1 2
JAN FEB AUGJUN JUL
: 2
:...1 ..2561...
2561
REMARKMAR APR
(PREVENTIVE MAINTENANCE YEAR PLANNER 2018)
PLANT :
MACHINE : ELECTRICAL & INSTRUMENT
6 7
12 PM UPS 1 YR PLAN
ACTUAL
13 PM Cathodic Protection 1 YR PLAN
ACTUAL
14 PM Heat Tracing System 1 YR PLAN
ACTUAL
15 1 YR PLAN
ACTUAL
16 1 YR PLAN
ACTUAL
17 PM Compact Prover 1 YR PLAN
ACTUAL
PLAN
ACTUAL
PLAN
ACTUAL
( ) ( )
. .
…...../….….../...….. …...../…..…../...…..
Rev.2 (20/02/61) 2/2 F- . .-0030 (1/1)
-4
-5
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2. ( . . /
. .)
3.
( . . / . .)
4. ( . .)
5. ( . .)
6. t ( .
. / . .)
. .
. .
-6
Environment Greenhouse Gas Accounting and Reporting
) | 1
Greenhouse Gas Accounting and Reporting
1.
(GHG)
(Global warming) (Climate Change)
GHG
GHG ( ) Carbon dioxide (CO2), Methane (CH4), Nitrous
oxide (N2O), Hydrofluorocarbons (HFCs), Perfluorocarbons (PFCs) Sulphur hexafluoride (SF6)
(Fossil Fuel) GHG
GHG
(PTT
Greenhouse Gas Accounting and Reporting Standard) GHG
GHG Scopes
1) Scope 1: Direct GHG Emissions GHG
Fire Pump
GHG
2) Scope 2: Indirect GHG Emissions GHG
3) Scope 3: Other indirect GHG Emissions GHG
Scope 2
GHG (CO2-equivalent)
GHG Scope 1, 2 Global Warming
Potential (GWP) GHG
Environment Greenhouse Gas Accounting and Reporting
) | 2
GWP GHG
2.
PTT Greenhouse Gas Accounting and Reporting
Standard (PTT GHG Calculation Template)
3.
1. GHG
2. GHG GHG
4.
(PTT Group GHG Inventory)
(PTT Group GHG Inventory Verification)
DJSI
5.
(PTT GHG Calculation Template)
6.
PTT Greenhouse Gas Accounting and Reporting Standard
-7
-8
1
.
2553
Version 1,1
. VERSION 1.1
2
. Version 1.1 ( 30 2553)
- .
. VERSION 1.1
3
.
Document ID : PTT GHG Standard Effective : version…1.1.... Date…30 June 2010…….
Document Title : PTT Greenhouse Gas Accounting and Reporting Standard
Reviewed by : …………signature………………………. Date: …………………
Ms. Sarintip Vaewhongs
Vice President
Environmental Research & Management Department
And: …………signature………………………. Date: …………………
Mr. Pipit Hongjinda
Vice President
Security, Safety, Health and Environment Department
Approved by:…………..signature………………………. Date: …………………
Mr. Nuttachat Charuchinda
Senior Executive Vice President
Corporate Strategy & Development
Reviewed by : ...(Position)…………………………
Approved by : .....(Position) ………………………
Version Page List of Modified Item Effective Date
. VERSION 1.1
4
.
.
9 :
1
2 .
3 Organizational Boundary
4 Operational Boundary
5
6
7
8 ( )
9 ( )
1:
2:
2.1: (Corporate)
:
3: (Organizational Boundary)
(Equity
Share Approach)
.
4:
5:
. VERSION 1.1
5
6:
7:
8: .
9: .
2.2 .
:
4:
5:
6:
7:
8: .
1.2
. VERSION 1.1
6
1 . 8
1.1 8
1.2 10
1.3 .
. 20
2. . 21
2.1 . 21
2.2 6 24
3. (ORGANIZATIONAL BOUNDARY) 33
3.1 (EQUITY SHARE APPROACH) 33
3.2 . 34
3.3 EQUITY SHARE APPROACH .
34
4. (OPERATIONAL BOUNDARY) 37
4.1 . 37
4.2 . 38
4.3 SCOPE 1 38
4.4 SCOPE 2 38
4.5 SCOPE 3 39
4.6 40
5. 44
5.1 44
5.2 SCOPE 1 47
5.3 SCOPE 2 83
. VERSION 1.1
7
5.4 SCOPE 3 89
5.5 93
6. 97
6.1 97
6.2 98
6.3 100
6.4 100
6.5 . 100
7. 106
7.1 108
7.2 108
7.3 109
7.4 110
7.5 110
8. ( ) 112
8.1 112
9. 115
9.1 ( ) 115
9.2 116
A .
B
C .
D .
E .
. VERSION 1.1
8
1 .
1.1
61
.
.
.
.
( )
.
. VERSION 1.1
9
.
.
.
ISO 14064-1:2006
Specification with guidance at the organization level for quantification and reporting of
greenhouse gas emissions and removals” ( “ISO 14064-1”)
International Organization for Standardization (ISO) “The Greenhouse Gas Protocol: a
Corporate Accounting and Reporting Standard, revised edition” ( “The
GHG Protocol”) World Business Council for Sustainable Development World
Resources Institute (WBCSD/WRI, 2004)1
“Compendium of Greenhouse Gas Emission Methodologies for the Oil
and Gas Industry” ( “API Compendium”) URS Corporation
( 2004) American Petroleum Institute (API)
“2006 IPCC Guidelines for National Greenhouse Gas Inventories” (
“2006 IPCC Guidelines”) developed by the Intergovernmental
Panel on Climate Change (IPCC).
.
1 GHG Protocol WBCSD/WRI
ISO, Climate Registry, EPA,
63 Fortune 500 [NASA Environmental and
Energy Conference, A Greenhouse Gas Accounting Protocol for the Public Sector, 24th September 2008, p.7]
. VERSION 1.1
10
1.1.1
.
.
1.2
1.2.1 – Greenhouse gas (GHG)
(“greenhouse gas” “GHG”)
6
(CO2), (CH4), (N2O), (HFCs),
(PFCs) (SF6)
1.2.2 – Greenhouse gas source
(physical unit) (process)
( )
( )
1.2.3 – Greenhouse gas sink
(physical unit) (process)
. VERSION 1.1
11
1.2.4 – Greenhouse gas reservoir
“Carbon stock”
GHG capture and
storage
1.2.5 – Greenhouse gas emission
( )
1.2.6 – Greenhouse gas removal
( )
1.2.7 – Greenhouse
gas emission or removal factor
(Default
emission factor)
(Stationary combustion) 5.7222
. VERSION 1.1
12
(mmscf) 5.3
5
1.2.8 – Direct greenhouse gas emission
(1.2.2)
. .
1.2.9 – Energy indirect
greenhouse gas emission
. .
1.2.10 – Other indirect greenhouse gas
emission
.
( 1.2.9)
.
4.5
1.2.11 – Greenhouse gas activity data
1.2.12 – Greenhouse gas assertion
(responsible party)
. VERSION 1.1
13
(validator) (verifier)
1.2.13 – Greenhouse gas information system
1.2.14 – Greenhouse gas inventory
.
1.2.15 – Greenhouse gas project
1.2.16 – Greenhouse gas programme
A:
B: PTT Greenhouse Gas ( GHG)
Programme
.
. VERSION 1.1
14
1.2.17 – Greenhouse gas report
(Greenhouse gas assertion)
1.2.18 – Global warming potential (GWP)
GWP
GWP Intergovernmental Panel on Climate Change (IPCC)
2.1.
1.2.19 – Carbon dioxide equivalent
GWP
1.2.20 – Base year
. . . 2553
1.2.21 – Facility
(Facility)
. VERSION 1.1
15
1.2.22 – Company
(Facility)
1.2.23 – Organization (Corporate)
(Organization Corporate) .
(Company)
1.2.24 . – PTT Group
.
20
. .
. 20
1.2.25 – Responsible party
(validator) (verifier)
. (PTT Corporate Climate Change Committee (CCC))
(validator)
(verifier)
. VERSION 1.1
16
1.2.26 – Intended user
.
. (PTT Corporate Climate Change Committee (CCC))
1.2.27 – Client
(validation)
(verification)
“ ”
. (PTT Corporate Climate Change Committee (CCC))
1.2.28 – Directed action
(Greenhouse Gas Project)
ISO 14064-2
(Greenhouse Gas Project)
(organizational boundaries)
. VERSION 1.1
17
1.2.29 – Level of assurance
1.2.30 – Materiality
(
)
1.2.31 – Material discrepancy
1.2.32 – Monitoring
(continuous) (periodic)
. VERSION 1.1
18
1.2.33 – Validation
(greenhouse gas
assertion)
1.2.34 – Validation criteria and verification
criteria
1.2.35 – Validation statement and
verification statement
1.2.36 – Validator
. VERSION 1.1
19
1.2.37 – Verification
(greenhouse gas
assertion)
1.2.38 – Verifier
1.2.39 – Uncertainty
1.2.40 – Standard Procedure (SP)
(
)
Standard Procedure SP
Procedure Manual (PM)
. VERSION 1.1
20
1.2.41 – Work Instruction (WI)
1.2.42 – Supporting Document (SD)
.
1.3 .
.
.
PTT GHG Program
.
. (PTT GHG Accounting
and Reporting Program)
. ISO 14064-1
GHG Protocol
3 (scope) .
.
(Centralized approach)
(Organizational Boundary)
(Equity Share Approach)
. VERSION 1.1
21
2. .
2.1 .
2.1.1 6
(GHGs)
1
(CO2)
(CH4) (O3)
6 (CO2) (CH4)
(N2O) (HFCs)
(PFC) (SF6)
(GWP) 6 2.1
1 : ISO 14064-1:2006.
. VERSION 1.1
22
2.1 6 (100 yr-GWP, 2nd
Assessment Report of IPCC 1995)
GWP Carbon Dioxide (CO2) 1 ;
Methane (CH4) 21 ;
; ;
Nitrous Oxide (N2O) 310 Adipic acid Nitric acid; ;
Hydrofluorocarbons (HFCs) 140 – 11,700
Perfluorocarbons (PFCs) 6,500 – 9,200 ;
Sulphur Hexafluoride (SF6) 23,900 ;
:
1) GWP
1
1 21
(tonnes of CO2 equivalent tCO2e)
2) Intergovernmental Panel on Climate Change (IPCC 2001) GWP
23 296 GWP 21 300
( 2012) GWP
3) HFCs PFCs GWP
2.1.2 .
3
.
. VERSION 1.1
23
2.1.3
.
GHG Protocol
WBCSD .
5 1:
– Relevance
.
.
– Completeness
– Consistency
1 ISO 14064-1:2006 Specification with guidance at the organization level for quantification and reporting of greenhouse gas
emissions and removals A Corporate Accounting and Reporting Standard (WBCSD/WRI, 2004).
. VERSION 1.1
24
– Accuracy
– Transparency
2.2 6
2.2.1 (Organizational Boundary)
.
Equity Share Approach
:
Equity Share Approach
. VERSION 1.1
25
2.1
2.1
2.2.2 (Operational Boundary)
(Operational Boundary)
2 :
(Direct GHG emissions) –
(Indirect GHG emissions) –
Company X
Company A Company B Company C Company D
100% Share 75% Share 50% Share 25% Share
100% control 100% control 50% control 0% control
Equity Share Approach
GHGX = 100%*GHGA + 75%*GHGB + 50%*GHGC + 25%*GHGD
. VERSION 1.1
26
3
(Direct GHG emissions)
(Energy indirect GHG emissions)
(Other indirect GHG emissions)
– Direct GHG
Emissions and Removals
(organizational boundary)
:
(direct GHG removals)
. VERSION 1.1
27
–
Energy Indirect GHG Emissions
(Organizational Boundary)
– Other Indirect GHG
Emissions
WBCSD 1
2.2.3
5 :
1 A Corporate Accounting and Reporting Standard (WBCSD/WRI, 2004).
. VERSION 1.1
28
(GHG emission or removal factors)
1.
WBCSD1, API2 Intergovernmental Panel on Climate Change (IPCC)3
WBCSD :
1 A Corporate Accounting and Reporting Standard (WBCSD/WRI, 2004).
2 Compendium of Greenhouse Gas Emissions Methodology for the Oil and Gas Industry (API 2004).
3 2006 IPCC Guidelines for National Greenhouse Gas Inventories.
. VERSION 1.1
29
(Stationary Combustion)
(Mobile Combustion)
(Process Emissions)
catalytic cracking
(Fugitive Emissions)
2.
:
–
(emission factors or removal
factors)
Mass Balance
–
. VERSION 1.1
30
3.
4.
(GHG emission or removal factors)
(emission factor removal
factor)
emission factor removal factor
5.
2 3 4
. VERSION 1.1
31
2.2.4
4
1.
2.
3.
4.
2.2.5
. VERSION 1.1
32
2.2.6
(GHG programme)
ISO
14064 ISO14064
(verification
statement)
. VERSION 1.1
33
3. (ORGANIZATIONAL BOUNDARY)
3.1 (EQUITY SHARE APPROACH)
.
(Equity Share Approach) :
.
.
.
Control Approach
.
(Equity Share Approach)
Equity Share Approach
.
.
Control Approach Equity Share Approach
.
Equity Share Approach .
( )
.
.
.
. VERSION 1.1
34
3.2 .
. .
.
( )
.
3.3 EQUITY SHARE APPROACH .
Equity Share Approch
. . .
( . . 45%)
0.45 . .
“ ”
. .
.
. . . .
. .
.
20
.
.
. VERSION 1.1
35
5,000
.
. VERSION 1.1
36
Box 3.1 .
:
1) “ ” “ ”
2) “ ” “ ”
“ ”
. . ( )
“ ”
“Equity Share Approach”
.
. A 25% A
1,000
. 1,000 x 25% = 250
. VERSION 1.1
37
4. (OPERATIONAL BOUNDARY)
4.1 .
.
.
ISO 14064-1 GHG Protocol 4.1
4.1
ISO 14064-1 The GHG Protocol
(Direct GHG emissions & Removal)
Scope 1:
(Direct GHG emissions)
(Energy indirect GHG emissions)
( )
Scope 2:
(Electricity
indirect GHG emissions
( )
Scope 3:
: ISO 14064-1 GHG Protocol
ISO 14064-1 GHG Protocol
GHG Protocol
Scope 1, Scope 2, Scope 3
. VERSION 1.1
38
4.2 .
. 3
Scope 1, Scope 2, Scope 3 4.1
. . 2552
. 5.1 5
.
4.3 SCOPE 1
Scope 1 .
( ) ISO
14064-1
WBCSD GHG Protocol
.
Scope 1 .
.
4.4 SCOPE 2
Scope 2
( )
.
.
.
. VERSION 1.1
39
Scope 2
(National Grid) Grid Emission Factor
-
4.5 SCOPE 3
Scope 3
.
Scope 3
:
stationary fuel combustion;
mobile fuel combustion;
mobile fuel
combustion;
.
. Scope 3
Stationary Fuel Combustion
.
stationary fuel combustion (
mobile fuel combustion)
. .
. VERSION 1.1
40
Mobile fuel combustion
.
.
4.5.1
Mobile Fuel
Combustion
( ) .
.
.
.
. .
Scope 1
. Scope
3
4.6
.
Scope 4.1
. VERSION 1.1
41
4.1 Scope
. 4.1
4.2
.
4
Section 4.5
Scope 1
Scope 2 Scope 3
. VERSION 1.1
42
4.2
:
: carbon,
?
: ,
,
: ,
. VERSION 1.1
43
Box 4.1 .
Scope 1
Scope 1
. .
Scope 2
Scope 2
.
.
.
.
Scope 3
Scope 3
.
.
. VERSION 1.1
44
5.
4.3.1 ISO 14064-1 .
:
1) ;
2) ;
3) ;
4)
(GHG emission or removal factors); ,
5)
.
5.1
.
3 scope B F
1:
2:
4:
(GHG emission or removal factors) 5:
3:
. VERSION 1.1
45
(Data Quality
Management Manual)
5.1
Scope 1 Scope 2 Scope 3
(Stationary fuel combustion)
(Mobile fuel combustion)
(Flare)
CO2 (CO2 separation)
Coke (Coke combustion)
(Ethylene production)
Hydrogen
plant
(Leakage from refrigeration unit)
(Leakage
from facilities)
(
)
( Purchased
energy (electricity
and steam))
(Employee
air travel)
(
) (Product
consumption by end-users:
Mobile Fuel Combustion)
(
) (Product consumption
by end-users: Stationary Fuel
Combustion
. (Mobile fuel combustion
from Raw material and Product
transportation)
. VERSION 1.1
46
5.1
5 (standard
gas conditions) 14.7 psia 60
379.3 standard cubic feet (scf)/lb-mole 23,685 cm3/gmole (API, 2004).
CO2
Ethylene
Hydrogen
Scope 1
Mid-stream
Scope 3
Scope 2
Scope 1
Direct Indirect
Up-stream
Coke
Down-stream
Direct
Direct Indirect . .
. VERSION 1.1
47
(million standard cubic feet: mmscf) - (gmole)
1 gmole 0.8364 scf 1 mol 0.8364 scf1
1 mol 23,684 cm3 106
cm3 1 m3
5.2 SCOPE 1
5.2.1 (Stationary Fuel Combustion)
.
(emission factor)
5.2
5.2
(1) 1 14.7 psia 60
CO2 = Amount of Fuel x EFCO2
CH4 = Amount of Fuel x EFCH4
N2O = Amount of Fuel x EFN2O
: Mmbtu, Nm3, mmscf, tonne, kg, liter,
Default
Default
Default
Feedstock Specific
(CO2): %mol C content
Default ( ):
API IPCC
. VERSION 1.1
48
5.1
CO2 = ( )
x (tCO2/ )
5.2
CH4 = ( )
x (tCH4/ )
5.3
N2O emissions = ( )
x (tN2O/ )
(CO2 emission factor)
CO2 emission factor 5.4
5.3
5.4 CO2 emission factor
CO2 emission factor = (number of C atom x % mol/100) (mol C/mol gas)
x gas molar volume conversion (1 mol/0.8364 scf)
x molar ratio (1 mol CO2/1 mol C)
x oxidation fraction (100%)
x molecular weight of CO2 (44g CO2/mol CO2)
x (106 scf/mmscf) x (1 tonne/106 g)
= CO2 emission factor (tCO2/mmscf)
. VERSION 1.1
49
(number of
C atom x % mol)
5.2
Mol%
C1 1 60
C2 2 8
C3 3 5
C4 4 3
C5+ 5 1
CO2 1 23
CO 1 1
(number of C atom x % mol)/100
= (1 x 60%+ 2 x 8% + 3 x 5% + 4 x 3% + 5 x 1% + 1 x 23% + 1 x 1%)/100
= 1.32 mol C/mol gas
(flare)
5.3 Emission factors
tCO2/ tCH4/ tN2O/
Mmbtu* 5.8992E-02 5.2577E-06 1.0515E-07
Nm3** 1.9119E-03 1.7040E-07 3.4080E-09
mmscf*** 5.7222E+01 5.1000E-03 1.0200E-04
Refinery fuel gas/off gas Mmbtu* 6.3000E-02 2.5200E-07 0.0000E+00
tonne*** 1.0596E+00 1.0470E-04 1.4658E-05
tonne*** 2.5333E+00 2.6370E-04 3.6918E-05
Anthracite tonne*** 3.0856E+00 3.1400E-04 4.3960E-05
Acetylene kg*** 3.3846E-03 9.5645E-08 2.8693E-08
. VERSION 1.1
50
tCO2/ tCH4/ tN2O/
Heavy Fuel Oil liter*** 3.0769E-03 7.9540E-08 2.3862E-08
LPG kg*** 3.1090E-03 9.8593E-08 2.9578E-08
:
2.2 IPCC (2006) emission factor TJ
* TJ Mmbtu.
** Nm3 ( 101.325 kPa 0 )
*** . (2550) 42
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry, API
(2004).
emission factors
2006 IPCC Guidelines for National Greenhouse Gas Inventories, IPCC (2006).
Electric Power in Thailand, Department of Alternative Energy Development and Efficiency,
Ministry of Energy, DEDE (2007).
5.2.2 (Mobile Fuel Combustion)
(
) .
emission factor
3 5.3
. VERSION 1.1
51
5.3
5.5
CO2 = ( )
x (tCO2/ )
5.6
CH4 = ( )
x (tCH4/ )
5.7
N2O = ( )
x (tN2O/ )
5.4 emission factors
CO2 = Amount of Fuel x EFCO2
CH4 = Amount of Fuel x EFCH4
N2O = Amount of Fuel x EFN2O Default
Default
Default
:
. VERSION 1.1
52
5.4 emission factors
tCO2/ tCH4/ tN2O/
LPG kg* 3.1090E-03 9.8593E-08 2.9578E-08
liter* 2.1816E-03 6.2960E-07 1.8888E-08
E10 liter* 1.9634E-03 6.2960E-07 1.8888E-08
liter* 2.6975E-03 1.8210E-07 2.1852E-08
B5 liter* 2.5626E-03 1.8210E-07 2.1852E-08
NGV kg* 2.5972E-03 2.3148E-07 4.6295E-09
Jet Fuel liter* 2.4689E-03 8.0000E-08 2.5000E-07
AvGas liter* 2.1289E-03 2.1900E-06 2.3000E-07
:
3.2.1 3.2.2 IPCC (2006) emission factor
TJ
* . (2550) 42
5.5
5.6
5.5
/100 . ( ) 7.3
( ) 9.0
( ) 7.8
( ) 10.7
( ) 9.4
( ) 13.1
LPG LPG (liter/100 km) 11.2
NGV NGV (kg/100 km) 8.4
1 9.0
9.8
. VERSION 1.1
53
/100 . 15.7
33.6
35.1
* 337.75
** Marine Fuel Oil 28,634.9
:
4-10 API (2004)
* (2006-9).
** Dead Weight Tonnage (DWT) 200,000 short tons = 2.31 t-fuel/106 ton-mile Ocean Policy Research
Foundation (1997); Fuel oil density = 909.48 kg/m3 Compendium of Greenhouse Gas Emissions Methodology for the
Oil and Gas Industry (API, 2004) ( 3-5).
5.6
< 1.4 L
1.4 – 2.1 L
> 2.1 L
1
6
6
LPG Car LPG
NGV Car NGV
:
: 4-11 API (2004)
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry, API
(2004)
emission factors
. VERSION 1.1
54
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry, API
(2004)
2006 IPCC Guidelines for National Greenhouse Gas Inventories, IPCC (2006).
Electric Power in Thailand, Department of Alternative Energy Development and Efficiency,
Ministry of Energy, DEDE (2007).
State railway of Thailand (2006-9).
Ocean Policy Research Foundation (1997).
5.2.3 (Flare)
(Flaring)
(emission factor)
5.4
emission factor
. VERSION 1.1
55
5.4 (Flare)
5.8
CO2 = (mmscf)
x CO2 (tCO2/mmscf of flared gas)
5.9 CO2 emission factors
CO2 emission factor = (number of C atom x % mol/100) (mol C/mol gas)
x gas molar volume conversion (1 mol/0.8364 scf)
x combustion fraction (mol CO2/mol C)
x molecular weight of CO2 (44g CO2/mol CO2)
x (106 scf/mmscf) x (1 tonne/106 g)
= CO2 emission factor (tCO2/mmscf)
Hydrocarbons from Petroleum
CO2 = Volume of Gas Flared x EFCO2
CH4 = Volume of Gas Flared x EFCH4
N2O = Volume of Gas Flared x EFN2O
Default
Site Specific
Default
Site Specific
Default
Volume of Gas Flared (mmscf)
: Measure %mol C content Measure %mol CH4 Content
:
(API, 2004)
. VERSION 1.1
56
Combustion fraction
API (2004) 99.5%
98% (API 2004, 4-27)
(number of C atom x % mol) 5.2
5.10
CH4 = (mmscf)
x CH4 (tCH4/mmscf of flared gas)
5.11 CH4 emission factors
CH4 emission factor = CH4 mole fraction (% mol/100)
x % residual CH4 (%/100)
x gas molar volume conversion (1 mol/0.8364 scf)
x molecular weight of CH4 (16g CH4/mol CH4)
x (106 scf/mmscf) x (1 tonne/106 g)
= CH4 emission factor (tCH4/mmscf)
% residual CH4
0.5% 2.0%
(API 2004, 4-29).
5.12
N2O = (mmscf)
x N2O (tN2O/mmscf of flared gas)
(emission factors)
5.7
. VERSION 1.1
57
5.7 CO2 CH4 N2O
CO2 CH4 N2O
5.1E-02 3.1E-04 5.9E-07 t/mmscf
1.8 1.1E-02 2.1E-05 t/106 m3
Sweet gas
5.9E-02 3.7E-04 7.1E-07 t/mmscf
2.1 1.3E-02 2.5E-05 t/106 m3
Sour gas
0.13 8.2E-04 1.5E-06 t/mmscf
4.6 2.9E-02 5.4E-05 t/106 m3
conventional oil
10.7 2.19E-02 * 1.0E-04 t/1000 bbl
67.0 1.38E-01 ** 6.4E-04 t/1000 m3
heavy oil
7.8 2.00E-02 *** 7.3E-05 t/1000 bbl
49.0 1.25E-01 **** 4.6E-04 t/1000 m3
crude bitumen
3.5 1.4E-02 3.8E-05 t/1000 bbl
22.0 8.8E-02 2.4E-04 t/1000 m3
No data 3.62E-06 No data t/1000 bbl
No data 2.28E-05 No data t/1000 m3
:
: API (2004) 4-7.
* 7.9E-04 4.3E-02 (max + min)/2.
** 5.0E-03 2.7E-01 (max + min)/2.
*** 7.9E-03 3.2E-02 (max + min)/2.
**** 5.0E-02 2.0E-01 (max + min)/2.
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry, API
(2004).
emission factors
. VERSION 1.1
58
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry, API
(2004).
5.2.4 (CO2 Separation)
(Flare)
5.5
5.5
CO2 (tonne) = (tonne)
+ (tonne)
(Hydrocarbons input + CO2 input + CH4 input) = (Hydrocarbons output + CO2 output + CH4 output)
+ (CO2 permeate gas + CH4 permeate gas)
:
CO2
Hydrocarbons
CO2
CH4
Hydrocarbons
CO2
CH4
(Permeate gas)
CO2 CH4
(Input gas)
(Output gas)
. VERSION 1.1
59
Hydrocarbons input = Hydrocarbons output
CO2 permeate gas = CO2 input – CO2 output
CH4 permeate gas = CH4 input – CH4 output
mass
balance
(Permeate
gas) CO2 (Flare)
(Permeate gas)
3
5.6 5.7 5.8.
1: Mass Balance
5.6 1: Mass Balance
CO2
Separation
Hydrocarbons
CO2
CH4
Hydrocarbons
CO2
CH4
Input Gas Stream Output Gas Stream
Permeate Gas
Collected CO2 CH4
CO2
CO2 CH4
CH4
%mol CO2 concentration %mol CH4 concentration
%mol CO2 concentration %mol CH4 concentration
. VERSION 1.1
60
5.13 CO2
CO2 Mass Balance
CO2 = CO2 input gas – CO2 output gas + CO2 from flaring
:
CO2 input gas = volume of input gas (mmscf)
x CO2 concentration of input gas (% mol/100)
x molecular weight of CO2 (44 g of CO2 per mol)
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
CO2 output gas = volume of output gas (mmscf)
x CO2 concentration of output gas (% mol/100)
x molecular weight of CO2 (44 g of CO2 per mol)
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
CO2 from flaring = CH4 permeate gas (tCH4)
x combustion fraction (%)
x (44/16) (gmolCO2/gmolCH4)
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
5.14 CH4
CO2 Mass Balance
CH4 emissions = CH4 permeate gas x (1 – combustion fraction (%))
:
CH4 permeate gas = (CH4 input gas – CH4 output gas)
. VERSION 1.1
61
CH4 input gas = volume of input gas (mmscf)
x CH4 concentration of input gas (% mol/100)
x molecular weight of CH4 (16g of CH4 per mol)
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
CH4 output gas = volume of output gas (mmscf)
x CH4 concentration of output gas (% mol/100)
x molecular weight of CH4 (16g of CH4 per mol)
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
2: Mass Balance
5.7 2: Mass Balance
Permeate Gas
Collected CO2 CH4
CO2 CH4
CO2 CH4
:
:
CO2
Separation
Hydrocarbons
CO2
CH4
Hydrocarbons
CO2
CH4
Input Gas Stream Output Gas Stream
%mol CO2 concentration %mol CH4 concentration
%mol CO2 concentration %mol CH4 concentration
. VERSION 1.1
62
5.15 CO2
CO2 Mass Balance
CO2 = CO2 input gas – CO2 output gas – Sale of CO2
:
CO2 input gas = volume of input gas (mmscf)
x CO2 concentration of input gas (% mol/100)
x molecular weight of CO2 (44 g of CO2 per mol)
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
CO2 output gas = volume of output gas (mmscf)
x CO2 concentration of output gas (% mol/100)
x molecular weight of CO2 (44 g of CO2 per mol)
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
Sale of CO2 = CO2 (tonne)
5.16 CH4
CO2 Mass Balance
CH4 = CH4 permeate gas x (CO2 emissions)
(CO2 emissions + Sale of CO2)
:
CH4 permeate gas = (CH4 input gas – CH4 output gas)
CH4 input gas = volume of input gas (mmscf)
x CH4 concentration of input gas (% mol/100)
x molecular weight of CH4 (16g of CH4 per mol)
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
. VERSION 1.1
63
CH4 output gas = volume of output gas (mmscf)
x CH4 concentration of output gas (% mol/100)
x molecular weight of CH4 (16g of CH4 per mol)
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
Sale of CO2 0, CH4 emissions CH4
permeate gas.
3: Vent Flow Rate
5.8 3: Vent Flow Rate
5.17 CO2
CO2 Vent Flow Rate
CO2 = volume of vented gas (mmscf)
x CO2 concentration of vented gas (% mol/100)
x molecular weight of CO2 (44 g of CO2 per mol)
Vented Gas
CO2 CH4
%mol CO2 concentration %mol CH4 concentration
CO2
Separation
Hydrocarbons
CO2
CH4
Hydrocarbons
CO2
CH4
Input Gas Stream Output Gas Stream
. VERSION 1.1
64
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
CH4 = volume of vented gas (mmscf)
x CH4 concentration of vented gas (% mol/100)
x molecular weight of CH4 (16 g of CO2 per mol)
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
5.8
5.8
CO2
1: Flaring & Mass Balance Approach
(Volume of input gas) mmscf
CO2 concentration input gas % mol
CH4 concentration input gas % mol
(Volume of output gas) mmscf
CO2 concentration output gas % mol
CH4 concentration output gas % mol
%
2: Flaring & Mass Balance Approach
(Volume of input gas) mmscf
CO2 concentration input gas % mol
CH4 concentration input gas % mol
(Volume of output gas) mmscf
CO2 concentration output gas % mol
CH4 concentration output gas % mol
CO2 tonne
3: Flaring & . Vent Flow Approach
. VERSION 1.1
65
mmscf
CO2 concentration vented gas % mol
CH4 concentration vented gas % mol
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry , API
(2004).
. VERSION 1.1
66
5.2.5 (Coke Combustion)
(Catalyst)
(Coke)
2
Blower
5.9 5.10
5.9 1: Coke Burn Rate
Catalytic Cracking Process
Carbon Coke (tonne C / tonne Coke) CO2
By-Product
Coke
X C + X O2 X CO2
. VERSION 1.1
67
5.18 CO2
Coke Burn Rate
CO2 = Coke (tonne)
x fraction of carbon in the coke burnt (t C/t coke)
x mass ratio of CO2/C (44/12)
(fraction of carbon in the coke
burnt) 1.0 (API 2004, 5-13).
5.10 2: Air Rates CO/CO2
5.19 CO2
Air Rates CO/CO2
CO2 = [Air Rate or Blower Capacity (mmscf)
Catalytic Cracking Process
%mol CO2
%mol CO
O2
Blower
(Air Rate)
. VERSION 1.1
68
+ Supplement Oxygen Rate (mmscf)]
x [CO2 Concentration (%mol/100)
+ CO Concentration (%mol/100)]
x molecular weight of CO2 (44 g of CO2 per mol)
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry , API
(2004).
emission factors
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry, API
(2004).
. VERSION 1.1
69
5.2.6 (Ethylene production)
5.11
5.11
5.20 CH4
CH4 = Ethylene (tonne)
x emission factor (0.001 tCH4/t ethylene produced)
0.001 tCH4/tonne
ethylene 5-20 API (2004)
Ethylene Ethylene
CH4 = Ethylene Produced x EFCH4 Default
. VERSION 1.1
70
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry, API
(2004).
emission factors
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry, API
(2004).
. VERSION 1.1
71
5.2.7 Hydrogen Plant
Hydrogen plant
C:H Hydrogen plant
refinery fuel gas
5.12
:
CxH(2x+2) + 2xH2O (3x + 1)H2 + xCO2
1
. VERSION 1.1
72
5.12 Hydrogen Plant
5.21 CO2 Hydrogen Plant
CO2 = volume of gas feed (mmscf)
x CO2 emission factor (tCO2/mmscf)
5.22 (Emission Factor)
Hydrogen Plant
CO2 emission factor = (number of C atom x % mol/100) (mol C/mol gas)
x molar ratio (1 mol CO2/1 mol C)
x molecular weight of CO2 (44 g of CO2 per mol)
Hydrogen Plant
Hydrocarbon Feedstock
H2
Default ( )
CO2 = Volume of Gas Feed x EFCO2
CH4
Naphtha
Refinery
Feedstock
Natural
. VERSION 1.1
73
x gas molar volume conversion (1 mol/0.8364 scf)
x (106 scf/mmscf) x (1 tonne/106 g)
(emission factor) 56.9359 tCO2/mmscf
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry, API
(2004).
emission factors
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry, API
(2004).
5.2.8 (Leakage from refrigeration units)
(Refrigerants)
HFC
(hydrofluorocarbon)
5.13
. VERSION 1.1
74
5.13
.
HFC R-134a, R-
404a, R-407c
5.23 HFC
HFC = (kg)
: HFC
2006 IPCC Guidelines for National Greenhouse Gas Inventories, IPCC (2006).
5.2.9 (Leakage from facilities)
fugitive emissions
2
(emission factor)
HFC Leaked
HFC Refill
. VERSION 1.1
75
Mass Balance 5.14
5.15
1 (activity data)
(emission factor) 5.14
5.14 1: Emission Factor Approach
. VERSION 1.1
76
:
CH4 CH4 = Production Volume x EFCH4 Default
Site
:
CH4
CH4 = Number of Stations x EFCH4 Default
:
CH4
CO2 = Length of Pipeline x EFCO2
CH4 = Length of Pipeline x EFCH4
Default
Site
Default
Site
Site
CO
CO
CO2 ( CH4)
CO2 ( CH4)
:
CH4 = Feedstock Volume x EFCH4 Default
Site
CH4
CO
CO2 ( CH4)
CO
. VERSION 1.1
77
5.9
(emission factors)
(Onshore Gas Production)
2.595E-02 tCH4/mmscf
9.164E-01 tCH4/106 m3
(Offshore Gas Production)
1.038E-02 tCH4/mmscf
3.665E-01 tCH4/106 m3
Onshore Oil Production
2.342E-01 tCH4/1000 bbl
1.473E+00 tCH4/1000 m3
Offshore Oil Production
9.371E-02 tCH4/1000 bbl
5.894E-01 tCH4/1000 m3
2.918E-02 tCH4/mmscf
1.030E+00 tCH4/106 m3
6.754E+02 tCH4/ –
( )
CH4 3.594E+00 tCH4/ –
2.233E+00 tCH4/ . –
CO2 oxidation 3.443E-03 tCO2/ –
2.139E-03 tCO2/ . –
CO2 2.117E-01 tCO2/ –
1.315E-01 tCO2/ . –
( )
CH4 1.611E+00 tCH4/ –
1.001E+00 tCH4/ . –
CO2 oxidation 5.611E-01 tCO2/ –
3.486E-01 tCO2/ . –
CO2 1.069E-01 tCO2/ –
6.640E-02 tCO2/ . –
8.43E-02 tonnes THC*/1000 bbl feedstock
5.30E-01 tonnes THC*/1000 m3 feedstock
: * THC = Total Hydrocarbon
. VERSION 1.1
78
: 6-1, API (2004)
5.10
CH4 CO2
78.8 %mol CH4 3.78 %mol CO2*
87 %mol CH4 2.0 %mol CO2
93.4 %mol CH4 2.0 %mol CO2
:
: 6-1, API (2004)
* Dalrymple, D.A., F.D. Skinner, and N.P. Misrule (1991).
5.9 5.10
5.24
( 5.25)
5.26
-
- associated gas
. VERSION 1.1
79
5.24 CH4
(Facility-level Average Emission
Factors)
CH4 = ( )
x [ CH4 (% mol/100)
÷ CH4 (% mol/100)]
x CH4 emission factor (tCH4/ )
5.25 CO2
(Facility-level Average Emission Factors)
CO2 = (km)
x [ CO2 (% mol/100)
÷ CO2 (% mol/100)]
x CO2 emission factor (tCO2/km-year)
5.26
CH4
CO2 = [ CH4 (tonne)
÷ CH4 (% mol/100)]
x [molecular weight of CO2 (44g of CO2 per mol)
÷ molecular weight of CH4 (16g of CH4 per mol)]
x [ CO2 (% mol/100)
THC Total Hydrocarbon
5.27
. VERSION 1.1
80
5.27 CH4
CH4 = (unit)
x CH4 (% mol/100)
x THC emission factor (tonnes THC/unit)
x [molecular weight of CH4 (16g of CH4 per mol)
÷ molecular weight of gas stream (g/mol)]
5.15 2: Mass Balance Approach
5.28 CO2
CO2 = CO2 (A) – CO2 (B) – CO2 (C)
CH4 leaked = CH4 (A) - CH4 (B) – CH4 (C)
CH4
CO2
CO2 leaked = CO2 (A) - CO2 (B) – CO2 (C)
Process/
Transmission A B
Vents CH4 CO2 C
. VERSION 1.1
81
:
CO2 (A) = (tonne)
x CO2 (% mol/100)
x [molecular weight of CO2 (44g of CO2 per mol)
÷ molecular weight of gas stream (g/mol)]
CO2 (B) = (tonne)
x CO2 (% mol/100)
x [molecular weight of CO2 (44g of CO2 per mol)
÷ molecular weight of gas stream (g/mol)]
CO2 (C) = CO2 (tonne)
5.29 CH4
CH4 = CH4 (A) – CH4 (B) – CH4 (C)
:
CH4 (A) = (tonne)
x CH4 (% mol/100)
x [molecular weight of CH4 (16g of CH4 per mol)
÷ molecular weight of gas stream (g/mol)]
CH4 (B) = (tonne)
x CH4 (% mol/100)
x [molecular weight of CH4 (16g of CH4 per mol)
÷ molecular weight of gas stream (g/mol)]
CH4 (C) = CH4 (tonne)
. VERSION 1.1
82
Compendium of Greenhouse Gas Emissions Methodology for the Oil and Gas Industry (API,
2004).
emission factors
Compendium of Greenhouse Gas Emissions Methodology for the Oil and Gas Industry (API,
2004).
Dalrymple, D.A., F.D. Skinner, and N.P. Meserole. Investigation of U.S. Natural Gas Reserve
Demographics and Gas Treatment Processes, Topical Report, GRI-91/0019. Gas Research
Institute, January 23, 1991.
. VERSION 1.1
83
5.3 SCOPE 2
5.3.1 ( ) (Purchased
Energy)
( ) .
Scope 2
(emission factor)
3
Scope 2 3
4
5.16
.
.
Scope 2
.
. VERSION 1.1
84
5.16 ( )
(Purchased Energy)
1:
Average tCO2 per
MWh
2:
3:
4:
Default 0.197 tCO2 per MWh
Indirect Emissions
Indirect Emissions
= MWh x EF Source
Default
= MWh x EF Grid
Default
= MWh x EF Source
Default
= MWh x EF Unknown
Default = 0.197 tCO2
Indirect Emissions
Average tCO2 per
MWh
Indirect Emissions
Average tCO2 per
MWh
. VERSION 1.1
85
1:
5.30 CO2 (
)
CO2 = (MWh)
x emission factor (tCO2/MWh)
emission factors II
III 5.12 II Cogeneration III
(Cogeneration)
2:
5.31 CO2 (
)
CO2 = (MWh)
x grid emission factor (tCO2/MWh)
(grid
emission factor) emission factor
grid emission factor
( . 2553) 5.11
5.11 Electricity Grid Emission Factors
tCO2/MWh
2007* 0.5057
2008** 0.5025
2009*** 0.4860
. VERSION 1.1
86
tCO2/MWh
2010**** 0.4669
2011**** 0.4559
2012**** 0.4528
2013**** 0.4298
2014**** 0.4328
2015**** 0.4081
2016**** 0.3796
2017**** 0.3646
2018**** 0.3528
2019**** 0.3556
: * Grid emission factor 2007 Hinchiranan (2007)
** Hinchiranan (2007) PDP 2004 default emission factors
fuels from IPCC (2006)
*** Hinchiranan (2007) PDP 2007 rev.2 default emission factors
fuels from IPCC (2006)
**** Hinchiranan (2007) PDP 2010 default emission factors
fuels from IPCC (2006)
3:
MWh
emission factor
5.32 CO2 (
)
CO2 = (MWh)
x emission factor (tCO2/MWh)
emission factor
IV 5.12
. VERSION 1.1
87
5.12 Emission factors CO2 CH4 N2O
(tCO2/MWh)
I II III IV
EFelectrity
(Non-Cogen)
EFelectrity
(Cogen)
EFSteam
(Cogen)
0.5882 0.4504 0.2252
0.7845 N/A N/A
0.9434 0.6632 0.3316
1.0246 N/A N/A
Import Coal 0.9076 N/A N/A
0.0000 N/A N/A
0.0000 N/A N/A
:
22 . (2550) default emission factors IPCC (2006), 2.2.
4:
0.05772 tCO2/Mmbtu (API 2004, 4-51) 0.1969 tCO2/MWh.
5.33 CO2 (
)
CO2 = (MWh)
x emission factor (0.1969 tCO2/MWh)
Compendium of Greenhouse Gas Emissions Methodologies for the Oil and Gas Industry , API
(2004)
emission factors
. VERSION 1.1
88
1:
Electric Power In Thailand, Department of Alternative Energy Development and Efficiency,
Ministry of Energy, DEDE (2007).
2006 IPCC Guidelines for National Greenhouse Gas Inventories, IPCC (2006).
2:
2006 IPCC Guidelines for National Greenhouse Gas Inventories, IPCC (2006).
Dr. Sukamon Hinchiranan, The estimation of emission factor for an electricity system in
Thailand 2007, Bureau of Energy Research, Department of Alternative Energy Development
and Efficiency, Ministry of Energy, Hinchiranan (2007).
Power Development Plan, PDP 2004.
Power Development Plan, PDP 2007 rev. 2.
Power Development Plan, PDP 2010.
3:
Electric Power In Thailand, Department of Alternative Energy Development and Efficiency,
Ministry of Energy, DEDE (2007).
2006 IPCC Guidelines for National Greenhouse Gas Inventories, IPCC (2006).
4:
Compendium of Greenhouse Gas Emissions Methodology for the Oil and Gas Industry, API
(2004).
. VERSION 1.1
89
5.4 SCOPE 3
5.4.1 (Employee Air Travel)
5.17
3
. VERSION 1.1
90
5.18 :
5.34 CO2
CO2 = (km) x
x emission factors (kgCO2/passenger-km)
Short Haul (< 1,000 km)
Medium Haul (1,000 – 5,000 km)
Long Haul (> 5,000 km)
Economy Class
Premium Economy Class
Business Class
First Class CO2 = (Travel distance x EFCO2)
Default
. VERSION 1.1
91
5.13 CO2
Economy kg CO2e/passenger-km 0.360 0.200 0.230
Premium Economy kg CO2e/passenger-km 0.468 0.260 0.299
Business kg CO2e/passenger-km 0.756 0.420 0.483
First kg CO2e/passenger-km - 0.640 0.736
:
: 1,000
: 1,001-3,700
: 3,700
: GHG Emissions Resulting from Aircraft Travel, Carbon Planet, Dr. Davide Ross, 2009, Emission Factor 1
Comparison Factor 2
GHG Emissions Resulting from Aircraft Travel, Carbon Planet, Dr. Davide Ross, 2009.
emission factors
GHG Emissions Resulting from Aircraft Travel, Carbon Planet, Dr. Davide Ross, 2009.
5.4.2 (Product consumption by end-users)
. .
:
(LPG)
( )
. VERSION 1.1
92
(stationary fuel combustion) (mobile fuel
combustion) 5.2.1 5.2.2
.
.
.
(Stationary fuel combustion)
5.2.1
(Mobile fuel combustion)
5.2.2
5.4.3 . (Raw
Material & Product distribution (mobile fuel combustion))
.
. .
.
Scope 1 –
.
5.2.2
. VERSION 1.1
93
5.5
5.14 Emission Factor
/
5.2 SCOPE 1
5.2.1
5.1
5.2
5.3
- API (2004) - 5.3
5.4 - API (2004) -
5.3 - - IPCC (2006)
- DEDE (2007)
5.2.2 5.5
5.6
5.7
- API (2004) - 5.4
5.4 - - IPCC (2006)
- DEDE (2007)
5.5 - - API (2004),
- State Railway of Thailand
- Ocean Policy Research Foundation
(1997)
5.6 - - API (2004)
5.2.3 5.8 - API (2004) - 5.7
5.9 - API (2004) - API (2004)
5.10 - API (2004) - 5.7
5.11 - API (2004) - API (2004)
5.12 - API (2004) - 5.7
5.7 - - API (2004)
5.2.4 (CO2
. VERSION 1.1
94
/
5.13
5.14
5.15
5.16
5.17
- API (2004) -
5.2.5 5.18
5.19
- API (2004) -
5.2.6 (Ethylene production
5.20
- API (2004) - API (2004)
5.2.7 Hydrogen Plant Hydrogen Plant
5.21 - API (2004) - API (2004)
5.22 - API (2004) -
5.2.8 (Leakage from refrigeration units
5.23 - IPCC (2006) -
5.2.9 (Leakage from facilities
5.9 - - API (2004)
5.10
- - API (2004)
- Dalrymple, D.A., F.D. Skinner, and
N.P. Meserole (1991).
5.24
5.25
5.26
5.27
- API (2004) - 5.9
- 5.10
5.28
5.29
- API (2004) -
5.3 SCOPE 2
5.3.1 ( )
. VERSION 1.1
95
/
5.30 - API (2004) - 5.12
5.31 - 5.11
5.11
- - Hinchiranan (2007).
- PDP 2004
- PDP 2007 rev.2
- PDP 2010
5.32 - API (2004) - 5.12
5.12 - - DEDE (2007)
- IPCC (2006)
5.33 - API (2004) - API (2004)
5.4 SCOPE 3
5.4.1
5.34 - Carbon Planet (2009) - 5.13
5.13 - - Carbon Planet (2009)
5.4.2
5.4.3 . (Raw Material
& Product distribution (mobile fuel combustion)
5.15
API (2004) Compendium of Greenhouse Gas Emissions Methodology for the
Oil and Gas Industry
Carbon Planet (2009) GHG Emissions Resulting from Aircraft Travel, Carbon Planet, Dr.
Davide Ross, 2009
Dalrymple, D.A., F.D. Skinner, and
N.P. Meserole (1991)
Dalrymple, D.A., F.D. Skinner, and N.P. Meserole. Investigation of
U.S. Natural Gas Reserve Demographics and Gas Treatment
Processes, Topical Report, GRI-91/0019. Gas Research Institute,
January 23, 1991.
DEDE (2007) Electric Power In Thailand, Department of Alternative Energy
. VERSION 1.1
96
Development and Efficiency, Ministry of Energy
Hinchiranan (2007). Dr.Sukamon Hinchiranan, The estimation of emission factor for an
electricity system in Thailand 2007
IPCC (2006) 2006 IPCC Guidelines for National Greenhouse Gas Inventories
Ocean Policy Research
Foundation (1997)
http://www.sof.or.jp/en/activities/pdf/06_04.pdf
PDP 2004 Thailand Power Development Plan 2004
PDP 2007 rev.2 Thailand Power Development Plan 2007 rev.2
PDP 2010 Thailand Power Development Plan 2010
State Railway of Thailand (2009) Annual Report of Mechanic Department for Quantity and Cost of
Fuel used in Various types of Diesel Locomotive from 2006-2009.
. VERSION 1.1
97
6.
:
6.1
.
. 3
(facility) (company/business unit)
(corporate)
(centralized approach)
6.1.1 (Centralized Approach)
( )
/
6.1
. VERSION 1.1
98
6.1
2
6.2
(GHG information management manual)
Corporate
Company/BU
Centralised
Level Tasks Direction
PTT (central)
Centralized
Validate & Consolidate data by Company/BU
(QSHE)
GHG Calculation, Consolidation & Report
Facility Level
Activity Data Collect, and verify activity data &
input data
. VERSION 1.1
99
4 1)
2) 3) QA/QC 4) 1
:
6.2.1
6.2.2
6.2
6.2.3 QA/QC
1 “WI” QA/QC
“SP”
. VERSION 1.1
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6.2.4
3
6.3
7
6.4
8 9
(Corporate)
6.5 .
. 3 :
– Standard Procedure (SP), Procedure Manual
(PM);
– Work Instruction (WI);
– Supporting Document (SD)
. VERSION 1.1
101
6 :
SP WI SD
6.5.1 (Standard Procedure: SP)
SP :
. (PTT GHG Calculation Tool)
log sheet 6.1
. VERSION 1.1
102
6.1
. 1
QNG
Mmscf
,
LOG SHEET Fuel Gas(NG) Consumption Data Worksheet
Orifice Flow Meter
2
, , 1
Intranet
:
. VERSION 1.1
103
6.2
/
1 Product and Sale
Summary (Daily
and Monthly
Report)
10
2 Production History 10
3 Diesel-Month-Year 10
4 Diesel
Consumption-
Monthly Report
........ 10
5 Light Fleet Fuel
Consumption
....... 10
6
7
8
9
10
ISO
ISO
QA/QC ( )
3
:
. VERSION 1.1
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6.3
1
2
3 Log sheet
4
5
6
7
8
9
10
6.5.2 (Work Instruction: WI)
WI :
6.4
. VERSION 1.1
105
6.4
...
...
. (PTT GHG Calculation Tool)
6.5.3 (Supporting Document: SD)
SD :
WI
. VERSION 1.1
106
7.
.
(internal verification)
(external verification)
(level of assurance)
5
7.1
. VERSION 1.1
107
7.1
/
-
/
. VERSION 1.1
108
7.1
(level of assurance)
.
.
7.2
:
;
(responsible party);
;
3 :
;
. VERSION 1.1
109
.
Check-list
3 :
1 –
2 –
3 –
A
.
7.3
:
;
;
;
;
;
( )
. VERSION 1.1
110
7.4
(acceptable without
material discrepancy)
(level of assurance)
7.5
.
“Climate Change Committee”
.
:
;
. VERSION 1.1
111
(level of assurance) ;
B
. VERSION 1.1
112
8. ( )
. 2
(facility) (company) (corporate)
(intended users) 2
.
.
1 & 2 3
2
C
D
8.1
:
:
;
:
;
;
. VERSION 1.1
113
tonnes of CO2e;
( ) tonnes of CO2e;
( );
tonnes of CO2e;
tonnes of
CO2e;
tonnes of CO2e ( );
( );
(base year) ;
( );
;
( );
(emission factor) ;
( );
ISO 14064 ( );
(level of assurance) ( );
;
(offsets)
tonnes of CO2e ( );
. VERSION 1.1
114
( )
(carbon intensity)
. VERSION 1.1
115
9. ( )
.
5
.
.
ISO 14064 .
ISO 14064
9.1 ( )
.
:
. ;
( );
( );
tonnes of CO2e;
( ) tonnes of CO2e;
( );
tonnes of CO2e;
(base year) ;
( );
. VERSION 1.1
116
;
( );
(emission factor) ;
( );
ISO 14064 ( );
(level of assurance) ( );
. ;
(directed actions)
( ) tonnes
of CO2e;
(offsets)
tonnes of CO2e ( );
;
tonnes of
CO2e;
( );
( );
9.2
1
. VERSION 1.1
117
.
9.2.1
1
. 2552 (2009)
9.2.2
/
:
A.
. VERSION 1.1
118
1
Outsource Insource
+/- 10
A
( . ) 10
B. emission factor
A
+/- 10
B
10
C.
. VERSION 1.1
119
C B
+/- 10
A B C
/ /
A B C
+/- 10
120
- -
. VERSION 1.1
121
122
A
123
.
:
1 –
2 –
3 –
1. ( / /
)
1.1
-
-
-
1.2
-
-
-
1.3
-
-
-
-
. VERSION 1.1
124
2. ( )
2.1
- Site
- Facility
-
2.2
- Site Boundary
- Site Boundary
2.3
-
-
- (default data)
(estimates)
2.4
-
(Information flow diagram)
-
o
o
. VERSION 1.1
125
o
/ /
2.5
(QA/QC Procedures)
2.6
-
2.7
-
-
2.8
-
-
3.
3.1 (WI,
)
3.2
-
. VERSION 1.1
126
3.3
-
-
-
-
. VERSION 1.1
127
4. /
4.1 (GHG
Calculation Tool)
4.2
-
-
-
4.3 IT
-
-
5. ( /
)
5.1 PTT
GHG Program
-
-
5.2
-
-
128
B
129
: :
PTT GHG Standard version
1)
2)
1)
2)
3)
PTT GHG Standard
PTT GHG Standard
1) PTT GHG Standard
2) ………………………
3) ………………………
4) ………………………
. VERSION 1.1
130
(3)
(2) (1)
1.1
1.2
1.3
2.1
2.2
2.3
2.4
2.5
(QA/QC Procedures)
2.6
2.7
2.8
3.1 (WI,
)
3.2
3.3
4.1 (GHG
. VERSION 1.1
131
(3)
(2) (1)
Calculation Tool)
4.2
4.3 IT
5.1
PTT GHG Program
5.2
............. .............
(Observation) (Opportunity for Improvement: OFI)
( 2)
( 1)
(Observation) (Opportunity for Improvement: OFI)
Verification Reporting Form version 1 (July 2010)
. VERSION 1.1
132
C
. VERSION 1.1
133
.
: ……………………………………………………………………
:……………………… . : …..%
: …… : 25…..
1) Scope 1
a. ………………………………………………………..
b. ………………………………………………………..
c. ………………………………………………………..
d. ………………………………………………………..
e. ………………………………………………………..
f. ………………………………………………………..
g. ………………………………………………………..
h. ………………………………………………………..
i. ………………………………………………………..
2) Scope 2
a. ………………………………………………………..
3) Scope 3
a. ………………………………………………………..
b. ………………………………………………………..
c. ………………………………………………………..
d. ………………………………………………………..
(Facility)
1) …………………………………………………………………
2) …………………………………………………………………
3) …………………………………………………………………
4) …………………………………………………………………
5) …………………………………………………………………
6) …………………………………………………………………
7) …………………………………………………………………
8) …………………………………………………………………
9) …………………………………………………………………
. VERSION 1.1
134
10) …………………………………………………………………
11) …………………………………………………………………
12) …………………………………………………………………
13) …………………………………………………………………
14) …………………………………………………………………
15) …………………………………………………………………
16) …………………………………………………………………
17) …………………………………………………………………
18) …………………………………………………………………
19) …………………………………………………………………
20) …………………………………………………………………
Scope 1
Scope 1 …… tCO2e
2 ...( 1)... ...( 2)...
...(%1)... ...(%2)...
Scope 1
Scope 2
Scope 2 (
. ) …… tCO2e
Scope 3
Scope 3 (
. Scope 1 ) …… tCO2e
2 ...( 1)... ...( 2)...
...(%1)... ...(%2)...
Scope 3
(
. .
Scope 1 ) …… tCO2e.
. VERSION 1.1
135
Scope 1 ……
Scope 2 ……
Scope 3 ……
……
…… tCO2e
. VERSION 1.1
136
D
. VERSION 1.1
137
.
: ……………………………………………………………………
: ……………………… . : ….. %
: 25…..
1) Scope 1
a. ………………………………………………………..
b. ………………………………………………………..
c. ………………………………………………………..
d. ………………………………………………………..
e. ………………………………………………………..
f. ………………………………………………………..
g. ………………………………………………………..
h. ………………………………………………………..
i. ………………………………………………………..
2) Scope 2
a. ………………………………………………………..
3) Scope 3
a. ………………………………………………………..
b. ………………………………………………………..
c. ………………………………………………………..
d. ………………………………………………………..
1) Scope 1
a. ………………………………………………………..
(……………………………………………………………...)
b. ………………………………………………………..
. VERSION 1.1
138
(……………………………………………………………...)
c. ………………………………………………………..
(……………………………………………………………...)
d. ………………………………………………………..
(……………………………………………………………...)
e. ………………………………………………………..
(……………………………………………………………...)
f. ………………………………………………………..
(……………………………………………………………...)
g. ………………………………………………………..
(……………………………………………………………...)
h. ………………………………………………………..
(……………………………………………………………...)
i. ………………………………………………………..
(……………………………………………………………...)
2) Scope 2
a. ………………………………………………………..
(……………………………………………………………...)
3) Scope 3
a. ………………………………………………………..
(……………………………………………………………...)
b. ………………………………………………………..
(……………………………………………………………...)
c. ………………………………………………………..
(……………………………………………………………...)
d. ………………………………………………………..
(……………………………………………………………...)
. VERSION 1.1
139
(Facility):
1) …… ……………
: … , , , . .……………………
…………………………………………………………………………………………………………
………………………………………………………………
2) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
3) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
4) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
5) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
6) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
7) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
8) …… ……………
. VERSION 1.1
140
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
9) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
10) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
11) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
12) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
13) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
14) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
15) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
. VERSION 1.1
141
16) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
17) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
18) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
19) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
20) …… ……………
: … , , , ..……………………
…………………………………………………………………………………………………………
………………………………………………………………
Carbon footprint & intensity 1) ………………………… Carbon footprint ……tCO2e & intensity ..….. tCO2e/ (Unit)
2) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
3) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
4) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
5) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
6) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
7) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
. VERSION 1.1
142
8) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
9) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
10) ………………………… Carbon footprint ……tCO2e & intensity ….. ..tCO2e/ (Unit)
11) ………………………… Carbon footprint ……tCO2e & intensity ….. ..tCO2e/ (Unit)
12) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
13) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
14) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
15) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
16) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
17) ………………………… Carbon footprint ……tCO2e & intensity …… tCO2e/ (Unit)
18) ………………………… Carbon footprint ……tCO2e & intensity ….... tCO2e/ (Unit)
19) ………………………… Carbon footprint ……tCO2e & intensity …… tCO2e/ (Unit)
20) ………………………… Carbon footprint ……tCO2e & intensity .…... tCO2e/ (Unit)
Carbon footprint …………tCO2e
:
1)…………………………………………. ………………………………….
2)…………………………………………. ………………………………….
3)…………………………………………. ………………………………….
4)…………………………………………. ………………………………….
5)…………………………………………. ………………………………….
6)…………………………………………. ………………………………….
7)…………………………………………. ………………………………….
. VERSION 1.1
143
. VERSION 1.1
144
Scope 1
Scope 1 ………… tCO2e
…….%
:
1. ………tCO2e (……..%)
2. ………tCO2e (……..%)
3. CO2 ………tCO2e (……..%)
4. ………tCO2e (……..%)
5. Hydrogen plant ………tCO2e (……..%)
6. Coke ………tCO2e (……..%)
7. ………tCO2e (……..%)
8. ………tCO2e (……..%)
9. ………tCO2e (……..%)
Scope 2
Scope 2 (
. ) …… tCO2e …….%
:
1. ………tCO2e (……..%)
Scope 3
(
.
. Scope 1 ) …… tCO2e …….%
:
1. ………tCO2e (……..%)
. VERSION 1.1
145
2. ( )
………tCO2e (……..%)
3. ( )
………tCO2e (……..%)
4. .
………tCO2e (……..%)
……
…… tCO2e :
: …..………………………………………………………………….
: ………………………………………………………….
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………….. tCO2e
: …..………………………………………………………………….
: ………………………………………………………….
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………….. tCO2e
: …..………………………………………………………………….
: ………………………………………………………….
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
. VERSION 1.1
146
………….. tCO2e
: …..………………………………………………………………….
: ………………………………………………………….
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………….. tCO2e
: …..………………………………………………………………….
: ………………………………………………………….
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………….. tCO2e
: …..………………………………………………………………….
: ………………………………………………………….
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………….. tCO2e
: …..………………………………………………………………….
: ………………………………………………………….
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………………………………………………………………………………
………….. tCO2e
. VERSION 1.1
147
( ) ….………………..
…………… % 1:
1 ………………………………………………
2 ……………………………………...………
3 ………………………………………………
( ……) (.....) /
……….. tCO2e .……………………………...……………………
………………………………………………………………………...…………………
…………………………………………………………………………...………………
…………… tCO2e / (
) / ……………. %
__( )__
( /
)
( )1 1 – ; 2 – ; 3 –
. VERSION 1.1
148
E
. VERSION 1.1
149
.
1. .
.
1.1 .
. 1.2
.
QA/QC
1.3
2. .
2.1 Scope
2.2 . Scope
Scope
2.3 .
2.4 .
. VERSION 1.1
150
2.5 .
3. .
. .
3.1 .
. .
3.2 . .
4. .
4.1 .
Scope
(benchmark)
4.2
5. .
. VERSION 1.1
151
( )
. VERSION 1.1
152
-9
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