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Assessment of Conversion Technologies for Bioalcohol Fuel ...

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Alcohol Synthesis<br />

The direct synthesis <strong>of</strong> methanol is an established commercial technology, and the<br />

catalysts <strong>for</strong> this process can be purchased from many suppliers. Copper/Zinc based<br />

catalysts are typically used <strong>for</strong> this synthesis and achieve high productivity. The perpass<br />

CO conversion is low (7-20%) because <strong>of</strong> equilibrium limitations and the need to<br />

maintain mild conditions to prevent copper sintering, but selectivity is high (99.5%).<br />

Because <strong>of</strong> the low cost ($20-30 l -1 ) and long useful life (3 to 5 years) <strong>of</strong> these<br />

catalysts, the production <strong>of</strong> methanol from synthesis gas is a very cost-effective<br />

process and is the starting point <strong>for</strong> many other useful chemicals like <strong>for</strong>maldehyde,<br />

acetic acid, MTBE, plastic compounds, etc. Spath and Daton (2003) present a<br />

thorough overview <strong>of</strong> methanol catalysts and systems related to methanol production.<br />

The methanol catalysts have been used as a starting point <strong>for</strong> the manufacture <strong>of</strong><br />

ethanol and higher alcohols. Several processes <strong>for</strong> higher alcohol synthesis have<br />

focused on modifying the hydrogenation catalysts to produce larger amounts <strong>of</strong> higher<br />

alcohols including ethanol.<br />

Most <strong>of</strong> the recent ef<strong>for</strong>ts on the conversion <strong>of</strong> syngas to ethanol have focused on<br />

modifications <strong>of</strong> catalysts originally developed by Dow Chemical Company (U.S. Pat.<br />

No. 4,675,344; 4,749,724; 4,752,622; 4,752,623; and 4,762,858). They developed a<br />

supported catalyst based on molybdenum disulfide (MoS2) to produce mixed alcohols,<br />

primarily C1-C4 (methanol—butanol), in a packed column or fluidized bed. The best<br />

per-pass CO conversion is approximately 20%, with up to 85% selectivity to mixed<br />

alcohols. The alcohol mix is typically comprised <strong>of</strong> 40% ethanol, 55% methanol and<br />

about 5% C3-C5 alcohols.<br />

Alcohol Purification<br />

The resulting raw alcohol produced via catalytic synthesis requires purification to meet<br />

market standards <strong>for</strong> alcohol products. Both methanol and ethanol have quality<br />

standards <strong>for</strong> fuel grade and chemical grade products. Raw methanol can contain<br />

water, higher alcohols, hydrocarbons and other byproducts. Raw mixed alcohols<br />

contain a mixture <strong>of</strong> multiple linear alcohols and water (and possibly other trace<br />

products). In order to separate these constituents into fuel grade components, a<br />

combination <strong>of</strong> absorption and multi-step distillation can be used. The technology to<br />

purify alcohols is technically feasibly with various components that have been<br />

employed by methanol and ethanol production facilities around the world.<br />

Some have proposed that alcohol mixtures be accepted as fuel additives without<br />

further purification, but there are currently no accepted standards <strong>for</strong> these mixtures.<br />

Italy successfully used a mixed alcohol product (MAS-Metanolo piu Alcoli Superiori) in<br />

gasoline during the 1980’s produced by the Snamprogeti plant (Spath and Daton,<br />

2003). Ultimately, this type <strong>of</strong> approach would save some <strong>of</strong> the cost <strong>of</strong> purification<br />

steps in alcohol synthesis plants, but would require acceptance by vehicle<br />

manufacturers and air quality regulatory agencies.<br />

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