发明名称 Separation process with modified enhanced hot separator system
摘要 A separation process with a modified enhanced hot separator system is described. The process eliminates undesirable entrainment while allowing for enhanced stripping of the net liquid only. The modified enhanced hot separator system combines a hot separator with a hot stripping column.
申请公布号 US9416321(B2) 申请公布日期 2016.08.16
申请号 US201213475075 申请日期 2012.05.18
申请人 UOP LLC 发明人 Eizenga Donald A.;Van Wees Mark;Steacy Paul C
分类号 C10G3/00;B01D19/00;C10G45/58;C10G69/06 主分类号 C10G3/00
代理机构 代理人
主权项 1. A process for producing biofuel from renewable feedstocks, the process comprising: deoxygenating the renewable feedstocks in a deoxygenation reaction zone, separating the deoxygenation reaction zone effluent in a first vapor-liquid separator into a vapor stream and a liquid stream wherein the first vapor-liquid separator is operated at a temperature from about 40 C to about 350 C; dividing the liquid stream into a recycle portion and a product portion; stripping the product portion of the liquid stream in a stripping column with a stripping gas into an overhead vapor stream and a bottoms stream wherein a level of contaminants in the bottoms stream of the stripping column after the first vapor-liquid separator is less than 1/100 of a level of contaminants in a bottoms stream of a stripping column without a vapor-liquid separator, and wherein the stripping column is operated at a temperature of from about 50 C to about 350 C; isomerizing the bottoms stream of the stripping column in an isomerization reaction zone; recycling the recycle portion of the liquid stream to the deoxygenation reaction zone; fractionating at least a portion of an effluent of the isomerization reaction zone to form at least one biofuel product stream.
地址 Des Plaines IL US