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Produced By:
Worst
Case Scenario:
Quick
note:
Long time viewers may notice that our diesel numbers and thus numbers
based on our diesel numbers have changed.
This is the result of our mistakenly entering the "low" value
of BTU for petroleum based diesel. This
means that we jumped a gap of approx 9,000 BTU when comparing that value to
the "high" value BTU of methanol.
To clarify, one BTU is the energy necessary to raise 1 lb water 1
degree Fahrenheit. "high"
value refers to this water in liquid state, "low" value refers to
the water in vapor state. Our apologies for this rookie-level mistake.
1 mol CO = 28.01g
1 mol CH3OH
= 32.042g
28.01g CO / 32.042g CH3OH
= .874165 CO in CH3OH
137 bil gal gasoline x 1.16
delta efficiency/BTU ratio = 158.9 bil gal CH3OH
/ year
1 gal CH3OH
x 4.78 kg CH3OH
/ gal CH3OH
= 4.78 kg/gal CH3OH
158,900,000,000 gal x 4.78 kg / gal = 759,540,000,000
kg CH3OH
.874165 kg CO / kg CH3OH
x 759,540,000,000 kg CH3OH
= 663.96 bil kg CO
59.05 bil gal diesel x 2.20 delta efficiency/BTU ratio = 129.91
bil gal CH3OH
/ year
129,910,000,000 gal x 4.78 kg / gal = 620.97 bil
kg CH3OH
.874165 kg CO / kg CH3OH
x 620,969,800,000 kg CH3OH
= 542.83 bil kg CO
663.98
bil kg CO + 542.83 bil kg CO
= 1.207 Trillion kg CO
total
http://web.archive.org/web/20060615133520/http://www.fpl.fs.fed.us/documnts/fplgtr/fplgtr12.pdf
Reference
to Gasification Study Above (733.74 tons):
63,500
lb carbon yields 96.5% or 61,271.3 lb carbon (CO, CO2, CH4)
323,705,079,358 kg carbon required per year
.965
= 335,479,707,699 kg carbon
335,479,707,699
kg carbon minimum required
.504 avg carbon in biomass =
733.74 mil (English) tons
Though not factored into calculations above, the
remaining 3.5 % of carbon found in the heavy oil (hydrocarbons) left
behind from the gasification process may be further utilized by super-critical
water reformation. The following link offers an excellent explanation of
this process and is also found on our biomass page: http://web.archive.org/web/20060615133520/http://media.fsec.ucf.edu/
Carbon
Monoxide can be obtained from a variety of sources, however, it may still
be considered the limiting reagent of thme 2H2 + CO =
CH3OH
reaction:
http://www.epa.gov/air/urbanair/co/what1.html
. Please feel free to
examine http://www.caloric.com/cms/upload/pdf/calcor.pdf
and imagine how this same process could be used with gasification of Biomass
and Coal
Also, many of our industrial sites that produce CO today are mandated
to convert this emission into CO2 . Sometimes this can be
accomplished with the reaction: (CO + H2O => CO2
+ H2). At
the very minimum, we this country is in no shortage of CO2 to
the extent that we need to devote our CO supply to make more CO2 (sarcasm).
One can imagine the prospects at hand to capture enough CO for making
sufficient quantities of methanol (CH3OH).
Engine efficiency study performed by the EPA demonstrating 43%
efficiency: http://www.epa.gov/otaq/presentations/sae-2002-01-2743.pdf.