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 |
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代理人 |
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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 |