Regulation of Fuels and Fuel Additives: Renewable Fuel Standard ...
Regulation of Fuels and Fuel Additives: Renewable Fuel Standard ...
Regulation of Fuels and Fuel Additives: Renewable Fuel Standard ...
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We calculated fixed <strong>and</strong> variable operating costs using percentages <strong>of</strong> direct labor <strong>and</strong><br />
total installed capital costs. Following this methodology, we estimate that producing a gallon<br />
<strong>of</strong> ethanol using corn stover as a cellulosic feedstock would cost $1.65 in 2012 (2004<br />
dollars).<br />
c. Ethanol’s Blending Cost<br />
Ethanol has a high octane value <strong>of</strong> 115 (R+M)/2 which contributes to its value as<br />
a gasoline blendstock. As the volume <strong>of</strong> ethanol blended into gasoline increases from<br />
2004 to 2012, refiners will account for the octane provided by ethanol when they plan<br />
their gasoline production. This additional octane would allow them to back <strong>of</strong>f <strong>of</strong> their<br />
octane production from their other gasoline producing units resulting in a cost savings to<br />
the refinery. For this cost analysis, the cost savings is expressed as a cost credit to<br />
ethanol added to the production cost for producing ethanol.<br />
We obtained gasoline blending costs on a PADD basis for octane from a<br />
consultant who conducted a cost analysis for a renewable fuels program using an LP<br />
refinery cost model. LP refinery models value the cost <strong>of</strong> octane based on the octane<br />
producing capacity for the refinery’s existing units, by added capital <strong>and</strong> operating costs<br />
for new octane producing capacity, <strong>and</strong> based on purchased gasoline blendstocks. The<br />
value <strong>of</strong> octane is expressed as a per-gallon cost per octane value, <strong>and</strong> ranges from 0.38<br />
cents per octane-gallon in PADD 2 where lots <strong>of</strong> ethanol is expected to be used, to 1.43<br />
cents per octane-gallon in California. Octane is more costly in California because the<br />
Phase 3 RFG st<strong>and</strong>ards restriction aromatics content which also reduces the use <strong>of</strong> a<br />
gasoline blendstock named reformate - a relatively cheap source <strong>of</strong> octane. Also,<br />
California’s Phase 3 RFG distillation restrictions tend to limit the volume <strong>of</strong> eight carbon<br />
alkylate, another lower cost <strong>and</strong> moderately high octane blendstock.<br />
Another blending factor for ethanol is its energy content. Ethanol contains a<br />
lower heat content per gallon than gasoline. Since refiners blend up their gasoline based<br />
on volume, they do not consider the energy content <strong>of</strong> its gasoline, only its price. Instead,<br />
the consumer pay’s for a gasoline’s energy density based on the distance that the<br />
consumer can achieve on a gallon <strong>of</strong> gasoline. Since we try to capture all the costs <strong>of</strong><br />
using ethanol, we consider this effect. Ethanol contains 76,000 British Thermal Units<br />
(BTU) per gallon which is significantly lower than gasoline, which contains an average<br />
<strong>of</strong> 115,000 BTUs per gallon. This lower energy density is accounted for below in the<br />
discussion <strong>of</strong> the gasoline costs.<br />
2. Biodiesel Production Costs<br />
We based our cost to produce biodiesel fuel on a range estimated from the use <strong>of</strong><br />
USDA’s <strong>and</strong> NREL’s biodiesel computer models. Both <strong>of</strong> these models represent the<br />
continuous transesterification process for converting vegetable soy oil to esters, along<br />
with the ester finishing processes <strong>and</strong> glycerol recovery. The models estimate biodiesel<br />
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