公开(公告)号：JP2008303213A

公开(公告)日：2008-12-18

申请号：JP2008124626

申请日：2008-05-12

Applicant: Basf Se ,  ビーエーエスエフ ソシエタス・ヨーロピアBasf Se

Inventor： GOEBBEL HANS-GEORG ,  KAIBEL GERD ,  MILLER CHRISTIAN ,  DOBLER WALTER ,  DIRNSTEINER THOMAS ,  HAHN THILO ,  BREUER KLAUS ,  AQUILA WERNER

IPC: B01J23/44 ,  C07C45/62 ,  B01J8/22 ,  B01J8/34 ,  C07B61/00 ,  C07C49/04

CPC classification number: C07C45/62 ,  C07C49/04

Abstract: PROBLEM TO BE SOLVED: To provide a method for preparing tetrahydrogeranylacetone by selectively hydrogenating pseudoionone, geranylacetone and/or dihydrogeranylacetone.
SOLUTION: A method for preparing tetrahydrogeranylacetone is disclosed, wherein pseudoionone, geranylacetone and/or dihydrogeranylacetone are (is) contained in a liquid phase, in which particles of a catalyst which is preferentially hydrogenating carbon-carbon double bonds over carbon-oxygen double bonds are suspended, is conducted through a device which inhibits the transport of the catalyst particles in the presence of a hydrogen-containing gas.
COPYRIGHT: (C)2009,JPO&INPIT

Abstract translation: 要解决的问题：提供通过选择性氢化假雄酮，香叶基丙酮和/或二氢鲱鱼基丙酮来制备四氢笨香基丙酮的方法。 解决方案：公开了一种制备四氢胆烷基丙酮的方法，其中在液相中包含假戊烯酮，香叶基丙酮和/或二氢呱呱酮丙酮，其中优先在碳 - 氧上氢化碳 - 碳双键的催化剂颗粒 双键悬浮，通过在含氢气体存在下抑制催化剂颗粒的输送的装置进行。 版权所有（C）2009，JPO＆INPIT

公开(公告)号：ES2295646T3

公开(公告)日：2008-04-16

申请号：ES03763838

申请日：2003-07-14

Applicant: BASF SE

Inventor： GOBBEL HANS-GEORG ,  KAIBEL GERD ,  MILLER CHRISTIAN ,  DOBLER WALTER ,  DIRNSTEINER THOMAS ,  HAHN THILO

IPC: B01J23/44 ,  C07C45/62 ,  B01J8/22 ,  B01J8/34 ,  C07B61/00 ,  C07C49/04

Abstract: Procedimiento para la elaboración de tetrahidrogeranilacetona, en el que se conduce una fase líquida, que comprenda al menos un 90% en peso de pseudojonona y en la que hay partículas de un catalizador suspendidas, que es capaz de la hidrogenación preferencial de los dobles enlaces carbono-carbono antes de los dobles enlaces carbono-oxígeno y cuyo componente activo contiene paladio, en presencia de un gas conteniendo hidrógeno a través de un dispositivo, que inhibe el transporte de las partículas de catalizador.

公开(公告)号：DE50214066D1

公开(公告)日：2010-01-21

申请号：DE50214066

申请日：2002-12-20

Applicant: BASF SE

Inventor： KAIBEL GERD DR ,  MILLER CHRISTIAN DR ,  KLASS KATRIN DR ,  KINDLER ALOIS DR ,  AQUILA WERNER DR ,  DOBLER WALTER DR ,  BREUER KLAUS DR ,  POMMER ACHIM ,  DIRNSTEINER THOMAS

IPC: B01D3/14 ,  B01D3/26

Abstract: Distillation column has a dividing wall which divides it into inflow and extraction sections, and upper and lower column zones. The mixture for distillation comprises a vapor feed which enters between the upper and lower inflow sections, between which the side extraction point removes vapor. The inflow and the extraction zones are offset relative too the dividing wall. The vapor feed rate is equal in all zones of the column. The distillation column has a dividing wall (TW) which divides it into an inflow section (2,4), an extraction section (3,5), and common upper (1) and lower (6) column zones. The mixture for distillation is at least partially a vapor feed (F) which enters between the upper and lower inflow sections, and the side extraction point (B) removes vapor between the upper and lower extraction zones. The cross sectional surfaces of the inflow and the extraction zones are set by an offset in the dividing wall. The F-factor is equal in all the zones of the column, defined as the product of the gas flow speed in m/seconds multiplied with the square root of the gas density in kg/m3.