发明名称 From carbon monoxide and hydrogen anaerobic fermentation processing using a pre-reactor/deep tank reactor system
摘要 Processes are disclosed for the low energy, anaerobic bioconversion of hydrogen and carbon monoxide in a gaseous substrate stream to oxygenated organic compounds such as ethanol by contact with microorganisms in a fermentation system with high conversion efficiency of both hydrogen and carbon monoxide. The processes of this invention use a pre-reactor and a deep, tank reactor in gaseous substrate flow sequence to obtain high conversion of gas substrate without undue risk of carbon monoxide inhibition.
申请公布号 US8980597(B2) 申请公布日期 2015.03.17
申请号 US201113243347 申请日期 2011.09.23
申请人 Coskata, Inc. 发明人 Hickey Robert;Donnellan Steven L.
分类号 C12P7/06;C12P1/04;C12P7/04;C12P7/24;C12P7/40 主分类号 C12P7/06
代理机构 代理人
主权项 1. A continuous process for the anaerobic bioconversion of a gas substrate comprising carbon monoxide, carbon dioxide and hydrogen in an aqueous menstruum containing microorganisms suitable for converting said substrate to oxygenated organic compound, said process comprising: a. continuously supplying a gas feed comprising said gas substrate to a pre-reactor assembly comprising at least one pre-reactor and contacting the gas feed with an aqueous menstruum therein, said contacting being under conditions sufficient to convert in the pre-reactor assembly between 10 and 40 percent of carbon monoxide in the gas feed to said oxygenated organic compound and provide a pretreated gas comprising unreacted carbon monoxide in a mole fraction less than that in the gas feed, unreacted hydrogen, and carbon dioxide in a mole fraction greater than that in the gas feed; b. continuously supplying at least a portion of the pretreated gas to a deep, tank reactor as microbubbles having a diameter of less than 500 microns for contact with an aqueous menstruum therein, said contacting being under conditions sufficient to provide a total, overall molar conversion of carbon monoxide and hydrogen contained in said gas feed in steps a and b to said oxygenated organic compound of at least 80 percent; and c. recovering oxygenated organic compound from the aqueous menstruum from the deep, tank reactor.
地址 Warrenville IL US