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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


PLANT :

MACHINE : MECHANICAL & CIVIL

62


ACTUAL Montree T.


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


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


1 2

JAN FEB AUGJUN JUL

: 2

:...1 ..2561...

2561

REMARKMAR APR


PLANT :


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


1 2

JAN FEB AUGJUN JUL

: 2

:...1 ..2561...

2561

REMARKMAR APR


PLANT :


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


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


. .

…...../….….../...….. …...../….….../...….. …...../…..…../...…..

………………………………………… ………………………………………… …………………………………………

( ) ( ) ( )

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


1 2

JAN FEB AUGJUN JUL

: 2

:...1 ..2561...

2561

REMARKMAR APR


PLANT :


6 7

Rev.2 (20/02/61) 1/2 F- . .-0030 (1/1)

10 11 12

MAY

3 4 5 8

DECSEP OCT NOV


1 2

JAN FEB AUGJUN JUL

: 2

:...1 ..2561...

2561

REMARKMAR APR


PLANT :


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)

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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

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

.


1.2.27 – Client

(validation)

(verification)

“ ”


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

:


. 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


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)


.

.

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)


(2004)

emission factors

. VERSION 1.1

54


(2004)


Electric Power in Thailand, Department of Alternative Energy Development and Efficiency,


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



x combustion fraction (mol CO2/mol C)

x molecular weight of CO2 (44g CO2/mol CO2)


= 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 molecular weight of CH4 (16g CH4/mol CH4)


= 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.


(2004).

emission factors

. VERSION 1.1

58


(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


. 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)



CO2 output gas = volume of output gas (mmscf)

x CO2 concentration of output gas (% mol/100)




CO2 from flaring = CH4 permeate gas (tCH4)

x combustion fraction (%)

x (44/16) (gmolCO2/gmolCH4)



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)



CH4 output gas = volume of output gas (mmscf)

x CH4 concentration of output gas (% mol/100)




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




. 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)




CO2 output gas = volume of output gas (mmscf)

x CO2 concentration of output gas (% mol/100)




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)




. VERSION 1.1

63

CH4 output gas = volume of output gas (mmscf)

x CH4 concentration of output gas (% mol/100)




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)


Vented Gas

CO2 CH4


CO2

Separation

Hydrocarbons

CO2

CH4

Hydrocarbons

CO2

CH4


. VERSION 1.1

64



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)



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)]





(2004).

emission factors


(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


(2004).

emission factors


(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


x molar ratio (1 mol CO2/1 mol C)


Hydrogen Plant

Hydrocarbon Feedstock

H2

Default ( )

CO2 = Volume of Gas Feed x EFCO2

CH4

Naphtha

Refinery

Feedstock

Natural

. VERSION 1.1

73



(emission factor) 56.9359 tCO2/mmscf


(2004).

emission factors


(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


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)


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


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)



CO2 (B) = (tonne)

x CO2 (% mol/100)



CO2 (C) = CO2 (tonne)

5.29 CH4

CH4 = CH4 (A) – CH4 (B) – CH4 (C)

:

CH4 (A) = (tonne)

x CH4 (% mol/100)



CH4 (B) = (tonne)

x CH4 (% mol/100)



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


**** Hinchiranan (2007) PDP 2010 default emission factors


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)


(2004)

emission factors

. VERSION 1.1

88

1:

Electric Power In Thailand, Department of Alternative Energy Development and Efficiency,



2:


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,



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

100

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

104

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


.

.

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)


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)






. VERSION 1.1

142



10) ………………………… Carbon footprint ……tCO2e & intensity ….. ..tCO2e/ (Unit)

11) ………………………… Carbon footprint ……tCO2e & intensity ….. ..tCO2e/ (Unit)






17) ………………………… 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

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