Abstract: This invention features methods and apparatus for producing syngas from any carbon-containing feed material. In some embodiments, a substoichiometric amount of oxygen is used to enhance the formation of syngas. In various embodiments, both oxygen and steam are added during the conversion of the feed material into syngas. The syngas can be converted to alcohols, such as ethanol, or to other products.

Abstract: The present invention provides methods to increase yields and selectivities to particular alcohols, such as ethanol, during alcohol synthesis from syngas. In some embodiments, a starting catalyst can be activated by contacting with a gas stream under certain preferred activation temperatures, pressures, and compositions.

Abstract: The present invention discloses and teaches new methods of converting syngas into ethanol and/or other higher alcohols. Preferred embodiments recycle methanol, partially convert it to syngas, and then convert this additional syngas also to C2+ alcohols. Generally, the invention provides reactors comprising catalysts capable of converting syngas to alcohols with low selectivities to carbon dioxide and methane, and further provides process strategies to separate and recycle unreacted syngas as well as methanol produced by the catalyst. The invention is capable of turning modest per-pass reaction selectivities to a particular alcohol, such as ethanol, into economically significant net selectivities and yields.

Abstract: This invention features methods and apparatus for producing syngas from any carbon-containing feed material. In some embodiments, a substoichiometric amount of oxygen is used to enhance the formation of syngas. In various embodiments, both oxygen and steam are added during the conversion of the feed material into syngas. The syngas can be converted to alcohols, such as ethanol, or to other products.

Abstract: Methods and apparatus for producing alcohols from syngas are disclosed herein. In some variations, syngas is catalytically converted to methanol in a first reaction zone, and residual syngas from the first reaction zone is then catalytically converted to ethanol in a second reaction zone. Also, in some variations, syngas is catalytically converted to methanol in high yield in a first reaction zone, and the methanol is then converted (optionally, with additional syngas) to ethanol in a second reaction zone.

Abstract: Removal of carbon monoxide, hydrocarbons, and nitrogen oxides from the exhaust gas from lean-burn, diesel and other engines which produce exhaust gases containing excess oxygen is provided by at least two catalysts in sequence, each capable of reducing nitrogen oxides within a particular range of engine operating temperatures. Oxidation of the remaining reducing gases is also accomplished.