초록 ▼

The present invention relates to a process and apparatus for processing agricultural waste to make alcohol and/or biodiesel. The agricultural wastes are subjected to anaerobic digestion which produces a biogas stream containing methane, which is subsequently reformed to a syngas containing carbon mo

The present invention relates to a process and apparatus for processing agricultural waste to make alcohol and/or biodiesel. The agricultural wastes are subjected to anaerobic digestion which produces a biogas stream containing methane, which is subsequently reformed to a syngas containing carbon monoxide and hydrogen. The syngas is converted to an alcohol which may be stored, sold, used, or fed directly to a reactor for production of biodiesel. The solids effluent from the anaerobic digester can be further utilized as slow release, organic certified fertilizer. Additionally, the wastewater from the process is acceptable for immediate reuse in agricultural operations.

대표청구항 ▼

What is claimed is: 1. A method for treating agricultural wastes comprising: anaerobic digesting a mixture of at least agricultural waste and up to 99% by weight water to yield solids and a biogas including methane and carbon dioxide; reforming the biogas including methane and carbon dioxide to a s

What is claimed is: 1. A method for treating agricultural wastes comprising: anaerobic digesting a mixture of at least agricultural waste and up to 99% by weight water to yield solids and a biogas including methane and carbon dioxide; reforming the biogas including methane and carbon dioxide to a syngas including carbon monoxide and hydrogen in a steam reformation process; and converting the syngas containing carbon monoxide and hydrogen to methanol in an alcohol conversion process. 2. The method according to claim 1, wherein the anaerobic digesting comprises digesting concentrated agricultural waste having a solids content of greater than about 4-8% that is heated prior to digestion. 3. The method according to claim 1, wherein prior to anaerobic digestion, the agricultural waste is concentrated up to about 30% solids, the concentrated agricultural waste then is contacted with water to produce an agricultural waste stream having a solids content from about 4% to about 8%. 4. The method according to claim 1, wherein the anaerobic digesting has a retention time of less than about 30 days. 5. The method according to claim 1, wherein the agricultural waste is comprised primarily of animal manures. 6. The method according to claim 1, wherein the biogas produced by anaerobic digestion is purified to form a cleaned biogas stream prior to reforming. 7. The method according to claim 6, wherein the biogas is purified by passing the gas through a solvent vessel to remove entrained H2S. 8. The method according to claim 7, wherein the biogas is purified by: separating entrained moisture from the biogas by passing the gas through an inlet separator; compressing the separated gas in a feed gas compressor to form a compressed gas stream; and removing hydrogen sulfide in a hydrogen sulfide absorber wherein the compressed gas stream is contacted with methyldiethanolamine to produce a cleaned biogas stream. 9. The method according to claim 1, wherein reforming the biogas comprises: heating the biogas; reforming the biogas by mixing the heated biogas with steam in the presence of a catalyst to form a hot syngas stream; and cooling the hot syngas stream to form a syngas stream. 10. The method according to claim 9, wherein the syngas stream comprises about 69 mol % hydrogen, about 13 mol % carbon dioxide, and about 17 mol % carbon monoxide. 11. The method according to claim 1, wherein converting the syngas to methanol comprises; compressing the syngas to form a hot, compressed syngas stream; converting the hot, compressed syngas into methanol in a methanol converter to form a hot methanol stream; cooling the hot methanol stream to form a condensed methanol stream; and separating condensed methanol from gas in a methanol separator. 12. The method according to claim 11, wherein additional carbon dioxide is not added to convert the syngas into methanol. 13. The method according to claim 11, wherein the methanol converter is a catalytic reactor containing a catalyst selected from ZnO--Cr3O3 and CuO--ZnO--Al2O3. 14. The method according to claim 1, wherein at least a portion of the solids remaining after anaerobic digestion are removed and treated to form fertilizer.