发明名称 |
PRODUCTION OF ETHANOL AND RECYCLE WATER IN A CELLULOSIC FERMENTATION PROCESS |
摘要 |
Processes for producing ethanol from fermentation systems employing cellulosic feedstocks are provided, where water is processed for recycle. The water handling portion of the process employs multi-effect evaporators where the first effect evaporator is maintained at temperatures in excess of 105° C., and the evaporation train, beer column form a heat integrated system. |
申请公布号 |
US2015087040(A1) |
申请公布日期 |
2015.03.26 |
申请号 |
US201314037407 |
申请日期 |
2013.09.26 |
申请人 |
E I DU PONT DE NEMOURS AND COMPANY |
发明人 |
Parten William D.;Kasat Rahul B. |
分类号 |
C12P7/10 |
主分类号 |
C12P7/10 |
代理机构 |
|
代理人 |
|
主权项 |
1. A process for the production of ethanol and recycle water comprising:
a) providing a hydrolysate fermentation medium; b) fermenting the medium in a fermenter in the presence of a microorganism that produces ethanol to produce a beer comprising from about 6% to about 10% ethanol, water, solutes, and solids; c) providing a distillation and water handling system comprising the elements:
I) a beer column;II) a rectification column;III) a solids removal mechanism; andIV) an evaporation train comprising at least four evaporation effect equivalents; wherein each element in the system is connected to at least one other element in the system, and wherein the beer column, the rectification column, and the evaporation train form a heat integrated system; d) passing the beer into the beer column of (I) where a beer column ethanol-rich vapor stream is separated from a water stream containing solutes and solids; e) condensing the beer column ethanol-rich vapor stream forming a beer column ethanol-rich stream; f) passing the beer column ethanol-rich stream into the rectification column of (II) wherein a further ethanol-enriched rectification column vapor stream is separated from an ethanol depleted water stream; g) passing the water stream containing solutes and solids of (d) through the solids removal mechanism of (III) producing a water stream containing solutes with solids substantially removed; h) passing the water stream containing solutes with solids substantially removed of (g) through the evaporation train of (IV) producing an evaporate comprising water containing high-volatility solutes and a syrup comprising low-volatility solutes, wherein a first effect evaporator of the evaporator train of (IV) is run at a temperature that is greater than 105° C. for at least about 10 days without fouling of heat exchange surfaces; and i) treating the evaporate of (h) to substantially remove the high-volatility solutes producing recycle water; wherein ethanol-enriched vapor is produced and water is processed for recycle. |
地址 |
Wilmington DE US |