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 />
compression to prepare this gas for use as fuel in the generator engine drivers in the<br />
project scenario. 22 Similarly, the minor combustion and fugitive emissions associated<br />
with oil-gas separation in the baseline scenario are unchanged by implementation of the<br />
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 the<br />
form of crude oil.<br />
• Electric power generating capacity in the baseline scenario using the existing engines is<br />
950 kW. The thermal efficiency of these engines burning only crude oil is 28%. Most of<br />
the produced electrical energy is used to drive electric pumps for shipment of the<br />
remaining produced crude oil to an off-site destination.<br />
What the project will change:<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 />
• 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 associated<br />
gas and crude oil fuel. The thermal efficiency of the replacement engines is 33% on<br />
associated gas fuel and 30% on crude oil.<br />
EXHIBIT 7.3:<br />
<strong>Flare</strong> Gas Recovery for On-Site Power Generation<br />
<strong>Project</strong> Information (based on hypothetical, measured data):<br />
• 2.62×10 6 m 3 /year (92.56×10 6 scf/yr) of processed associated gas is sent to the flare in<br />
the baseline scenario.<br />
• The carbon content of the processed associated gas is 0.65 kg carbon/m 3 (0.0404 lb<br />
C/scf).<br />
• In the baseline scenario, crude oil fuel consumption for operation of the internal<br />
combustion engine drivers used to generate electricity for on-site combustion is 13,963<br />
barrels per year.<br />
• Average carbon content of the produced crude after gas and water separation is 85%<br />
by weight, and the higher heating value of this crude oil is 570 MMBtu/barrel.<br />
22 As noted previously, if gas dehydration and compression equipment were not present in the baseline scenario,<br />
their addition in the project scenario would create new emissions.<br />
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