公开(公告)号：US20170327445A1

公开(公告)日：2017-11-16

申请号：US15526124

申请日：2015-11-13

申请人： Abengoa Bioenergia Nuevas Tecnologias, S.A.

发明人： Juan Luis SANZ YAGUE ,  Francisco Antonio LADRÓN DE GUEVARA VIDAL ,  Laura SÁNCHEZ HOLGADO ,  Yolanda PEÑA GÓMEZ ,  Carmen Maria REYES VALLE ,  Ana Rosa SÁNCHEZ SÁNCHEZ

IPC分类号： C07C29/34 ,  B01J23/89 ,  B01J37/18 ,  B01J37/08 ,  B01J37/06 ,  B01J37/03 ,  B01J37/02 ,  B01D3/00 ,  B01J23/72 ,  B01J23/648 ,  B01J23/62 ,  B01J23/44 ,  B01J23/08 ,  B01J21/10 ,  B01J8/02 ,  B01D3/14 ,  C07C29/80

CPC分类号： C07C29/34 ,  B01D3/009 ,  B01D3/143 ,  B01J8/0278 ,  B01J21/10 ,  B01J23/08 ,  B01J23/44 ,  B01J23/62 ,  B01J23/6482 ,  B01J23/72 ,  B01J23/898 ,  B01J37/0213 ,  B01J37/0236 ,  B01J37/036 ,  B01J37/06 ,  B01J37/08 ,  B01J37/18 ,  B01J2208/021 ,  C07C29/80 ,  Y02P20/125 ,  Y02P20/127 ,  Y02P20/132 ,  C07C31/125

摘要： The present disclosure generally relates to processes for preparation of n-butanol, n-octanol and n-decanol from a reaction mixture comprising ethanoi and n-hexanol by Guerbet condensation. In some aspects, the present disclosure relates to improvements in n-octanol and n-decanol yield and selectivity by the selection of process reaction conditions such as, but not limited to, mole ratio of n-hexanol to ethanol. The present disclosure further generally relates to integrated processes for preparation of n-butanol in a n-butanol reactor from a reaction mixture comprising ethanol and hydrogen to produce a n-butanol product stream by Geurbet condensation comprising n-butanol and n-hexanol and for preparation of n-octanol in a n-octanol reactor from a reaction mixture comprising ethanol, n-hexanol and hydrogen to produce a n-octanol product stream by Geurbet condensation comprising n-butanol, n-hexanol and n-octanol. A predominant proportion of the n-hexanol contained in the n-butanol and n-octanol product streams is isolated and recycled to the n-octanol reaction mixture. In some aspects, the present disclosure relates to improvements in n-octanol and n-butanol yield and selectivity by the selection of process reaction conditions such as, but not limited to, mole ratio of n-hexanol to ethanol and recovery and recycle of n-hexanol.