Part III: Flare Reduction Project Family - IPIECA
Part III: Flare Reduction Project Family - IPIECA
Part III: Flare Reduction Project Family - IPIECA
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Section 7. <strong>Flare</strong> <strong>Reduction</strong> <strong>Project</strong> <strong>Family</strong><br />
EXHIBIT 7.3:<br />
<strong>Flare</strong> Gas Recovery for On-Site Power Generation, continued<br />
• The combustion and fugitive emissions associated with dehydration and compression<br />
of the associated gas for flaring in the baseline scenario are the same as dehydration<br />
and compression to prepare this gas for use as fuel in the generator engine drivers in<br />
the project scenario. Similarly, the minor combustion and fugitive emissions<br />
associated with oil-gas separation in the baseline scenario are unchanged by<br />
implementation of the project.<br />
• All of the gas flared in the baseline scenario is used as fuel in the project scenario.<br />
However the quantity of gas is sufficient to meet only 90% of the required annual fuel<br />
stream to the replacement engines, with the remaining 10% of the fuel still supplied in<br />
the form of crude oil.<br />
• Electric power generating capacity is 950 kW in the baseline scenario using the<br />
existing engines. The thermal efficiency of these engines burning only crude oil is<br />
28%. Most of the produced electrical energy is used to drive electric pumps for<br />
shipment of the remaining produced crude oil to an off-site destination.<br />
• Electric power generating capacity in the project scenario uses new, more efficient<br />
engines rated at 1350 kW, and these engines are configured to operate on both<br />
associated gas and crude oil fuel. Thermal efficiency of the replacement engines is<br />
33% on associated gas fuel and 30% on crude oil.<br />
• The quantity of crude oil used for power generation in the project scenario is 2,362<br />
barrels per year. This scenario thus enables 11,601 additional barrels of crude to be<br />
shipped to markets compared with the baseline scenario. The increase in fugitive<br />
emissions associated with this increment of crude oil shipping is negligibly small.<br />
Baseline Emissions<br />
Baseline emissions = CMB 1 + VENT 1 + FUG 1 + IND 1<br />
where,<br />
CMB 1 = Combustion emissions from the flared stream prior to the project and from<br />
the combustion of crude oil to operate the pump engines.<br />
VENT 1 = Vented gas from maintenance or upset conditions associated with gas<br />
separation, dehydration, and compression. The vented emissions also occur<br />
unchanged in the project activity and therefore cancel out in the calculation<br />
of project emission reductions.<br />
FUG 1 = Fugitive emissions from process units associated with gas separation,<br />
dehydration, and compression. These fugitive emissions also occur in the<br />
project activity and therefore cancel out in the calculation of baseline<br />
emission reductions.<br />
IND 1 = Indirect emissions would result from usage of electricity obtained from<br />
outside sources. No such purchased power is used for either the baseline or<br />
project scenarios.<br />
October 2009 51