PDF File - GEC
PDF File - GEC
PDF File - GEC
You also want an ePaper? Increase the reach of your titles
YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.
4.4 Baseline emissions<br />
BE y , baseline emissions in year y (tCO 2 e), is estimated as follows:<br />
BE y<br />
= (MD Project,y<br />
– MD BL,y<br />
) • GWP CH4 + EF LFG,y<br />
• CEF elec,BL,y + ET LFG,y • CEF ther,BL,y<br />
(1) (2) (3) (4) (5) (6) (7)<br />
(1) MD project,y The amount of methane that would have been destroyed/combusted during the<br />
year (tCH 4 ) in project scenario<br />
Figure A-1 shows how MD project,y is to be determined ex post by metering the actual quantity of<br />
methane captured and destroyed once the project activity is operational.<br />
CH4<br />
Landfill<br />
LFGtotal,y<br />
(a) MDtotal,y<br />
LFGther,y<br />
LFGPL,y<br />
LFGelec,y<br />
LFGflare,y<br />
The lower of<br />
(a) or (b)<br />
should be<br />
chosen as<br />
MDproject,y<br />
Boiler Pipe Power Plant Flare<br />
MDther,y<br />
+ MDPL,y + MDelec,y + MDflared,y =<br />
(b) The sum<br />
: monitored : calculated<br />
Here, MD total,y , MD flared,y , MD elec,y , MD PL,y and MD ther,y are calculated based on monitored flow of landfill gas at<br />
different points, i.e. LFG total,y , LFG flare,y , LFG elec,y , LFG PL,y and LFG ther,y , using the following formula:<br />
MD total,y = LFG total,y • W CH4,y • D CH4<br />
MD elec,y = LFG elec,y • w CH4,y • D CH4<br />
MD ther,y = LFG ther,y • w CH4,y • D CH4<br />
MD PL,y = LFG PL,y • w CH4,y • D CH4<br />
MD flared,y = (LFG flare,y • w CH4,y • D CH4 ) – (PE flare,y /GWP CH4 )<br />
w CH4,y : Average methane fraction of the landfill gas as measured during the year (in m 3 CH 4 / m 3 LFG)<br />
D CH4 : Methane density (tCH 4 /m 3 CH 4 )<br />
PE flare,y : Project emissions from flaring of residual gas stream in year y (tCO 2 e). Determined by following<br />
the procedure described in the “Tool to determine project emissions from flaring gases containing<br />
Methane” [EB28, Annex 13].<br />
Figure A-1 Flow diagram of MD project,y calculation<br />
MD project,y should be chosen as the lower value of MD total,y or the sum of MD flared,y , MD elec,y , MD PL,y and<br />
MD ther,y . When the sum of MD flared,y , MD elec,y , MD PL,y and MD ther,y is lower, then the working hours of the<br />
energy plant(s) and the boiler(s) should be monitored and no emission reduction could be claimed<br />
for methane destruction in the energy plant or the boiler when they are not working.<br />
(2) MD BL,y The amount of methane that would have been destroyed/combusted during the year<br />
in the absence of the project (tCH 4 ) due to regulatory and/or contractual requirement<br />
(a) In the case where the MD BL,y is given/defined in the regulation and/or contract as a quantity<br />
that quantity will be used.<br />
104