专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

EP2197825B1 METHOD OF PRODUCING TERTIARY AMYL ETHYL ETHER 有权
标题翻译：用于生产TERT戊基乙基醚
公开(公告)号：EP2197825B1
公开(公告)日：2015-11-04
申请号：EP08798613.9
申请日：2008-08-25
申请人： Catalytic Distillation Technologies
发明人： BOYER, Christopher, C. , LOESCHER, Mitchell, E. , ROCK, Kerry, L. , GROTEN, Willibrord, A. , MARASCHINO, Mario, J.
IPC分类号： C07C43/03 , C07C41/06 , C07C41/42
CPC分类号： C07C41/06 , Y02P20/127 , C07C43/046

2. 发明公开

EP0991613A1 OLEFIN SKELETAL ISOMERIZATION PROCESS 失效
标题翻译： OLEFIN骨架异构化过程
公开(公告)号：EP0991613A1
公开(公告)日：2000-04-12
申请号：EP98923872.0
申请日：1998-06-02
申请人： Catalytic Distillation Technologies
发明人： RYU, J., Yong , GROTEN, Willibrord, A.
IPC分类号： C07C1/00 , C07C2/66 , C07C4/14 , C07C5/22
CPC分类号： C07C11/02 , Y02P20/127
摘要： An isomerization process for C4 to C15 olefins carried out by the reaction of C4 to C15 olefins, having a first skeletal distribution, with aromatic compounds under alkylation conditions to produce an alkylated aromatic product, dealkylation of the alkylated aromatic product under dealkylation conditions to produce a dealkylated product comprising said aromatic compounds and olefins corresponding to the olefins in the alkylation and having a second skeletal distribution different than said first skeletal distribution. Acidic catalysts such as molecular sieves are used in both alkylation and dealkylation. The reactions may be carried out in either straight pass fixed beds or in catalytic distillation reactors.
摘要翻译： C4-C15烯烃的异构化方法，其通过在烷基化条件下使C4至C15烯烃（具有第一骨架分布）与芳族化合物反应以产生烷基化芳族产物，在烷基化芳族产物在脱烷基化条件下脱烷基化以产生包含所述芳族化合物和烯烃的脱烷基化产物，所述烯烃对应于烷基化中的烯烃并具有不同于所述第一骨架分布的第二骨架分布。酸性催化剂如分子筛用于烷基化和脱烷基化。反应可以在直通固定床或催化蒸馏反应器中进行。

3. 发明授权

EP1019346B1 PROCESS FOR PRODUCTION OF METHANOL 失效
标题翻译：用于生产甲醇
公开(公告)号：EP1019346B1
公开(公告)日：2003-05-07
申请号：EP98910139.9
申请日：1998-01-07
申请人： Catalytic Distillation Technologies
发明人： NEMPHOS, Speros, P. , GROTEN, Willibrord, A. , ADAMS, John, R.
IPC分类号： C07C27/10 , C07C29/00 , C07C27/00 , C07C29/151
CPC分类号： C07C29/1512 , C07C31/04

4. 发明公开

EP1563038A1 PROCESS FOR THE TREATMENT OF LIGHT NAPHTHA HYDROCARBON STREAMS 审中-公开
标题翻译：治疗方法LEICHTNAPHTA烃流
公开(公告)号：EP1563038A1
公开(公告)日：2005-08-17
申请号：EP03754639.7
申请日：2003-09-16
申请人： Catalytic Distillation Technologies
发明人： PODREBARAC, Gary, G. , GROTEN, Willibrord, A. , SOM, Manoj , ALMERING, Martinus, J.
IPC分类号： C10G45/00 , C10G65/02
CPC分类号： C10G45/02 , C10G2400/02
摘要： A light cracked naphtha is treated to convert mercaptans to sulfides and saturate dienes and then subjected to destructive hydrodesulfurization (HDS) to convert the organic sulfur compounds to hydrogen sulfide. The recombinant mercaptans formed by reaction of hydrogen sulfide and olefins at the outlet of the HDS are generally heavier than the light cracked naphtha is fractionated in admixture with a heavy cracked naphtha. A low sulfur content light cracked naphtha is produced as an overheads and the major portion of the mercaptans leave with heavy cracked naphtha as bottoms. It also advantageous to pass the heavy cracked naphtha through the HDS in admixture with the light cracked naphtha, since the recombinant mercaptans formed with the heavy cracked naphtha olefins (which displace some of the lower mercaptans which would form the light cracked naphtha olefins) will be even higher boiling and easier to separate by fractionation.

5. 发明公开

EP1019346A1 PROCESS FOR PRODUCTION OF METHANOL 失效
标题翻译：用于生产甲醇
公开(公告)号：EP1019346A1
公开(公告)日：2000-07-19
申请号：EP98910139.9
申请日：1998-01-07
申请人： Catalytic Distillation Technologies
发明人： NEMPHOS, Speros, P. , GROTEN, Willibrord, A. , ADAMS, John, R.
IPC分类号： C07C27/10 , C07C29/00 , C07C27/00
CPC分类号： C07C29/1512 , C07C31/04
摘要： A process for the production of methanol is disclosed wherein the gaseous reactants of CO, H2 and optimally CO2 are reacted in a distillation column reactor in the presence of an inert C7-C12 component, which is boiling at the reaction temperature within the catalyst bed. The inert component is taken overhead along with the methanol and separated therefrom for reflux of the inert component back to the reactor.

6. 发明授权

EP1537062B1 SELECTIVE HYDROGENATION OF ACETYLENES 有权
标题翻译：乙炔选择性加氢
公开(公告)号：EP1537062B1
公开(公告)日：2016-01-13
申请号：EP03737041.8
申请日：2003-06-12
申请人： Catalytic Distillation Technologies
发明人： RYU, J., Yong , ADAMS, John, R. , GROTEN, Willibrord, A.
IPC分类号： C07C5/03 , C07C5/05 , C07C5/09 , C07C7/167
CPC分类号： C07C7/167 , C07C5/09 , C07C2523/755 , C07C2523/80 , C07C2523/89

7. 发明公开

EP2197825A2 METHOD OF PRODUCING TERTIARY AMYL ETHYL ETHER 有权
标题翻译：用于生产TERT戊基乙基醚
公开(公告)号：EP2197825A2
公开(公告)日：2010-06-23
申请号：EP08798613.9
申请日：2008-08-25
申请人： Catalytic Distillation Technologies
发明人： BOYER, Christopher, C. , LOESCHER, Mitchell, E. , ROCK, Kerry, L. , GROTEN, Willibrord, A. , MARASCHINO, Mario, J.
IPC分类号： C07C41/05 , C07C43/03
CPC分类号： C07C41/06 , Y02P20/127 , C07C43/046
摘要： A process for the production of tertiary ethers, including: feeding a hydrocarbon stream comprising isoolefins and propionitrile to a distillation column reactor system containing at least one etherification reaction zone; feeding a C2 to C6 monoalcohol or mixture thereof to the distillation column reactor; concurrently in the distillation column reactor system: reacting a portion of the isoolefins with a portion of the alcohols to form a tertiary ether; and separating the tertiary ether from unreacted isoolefins; withdrawing the tertiary ether and propionitrile from the distillation column reactor system as a bottoms; withdrawing the unreacted isoolefins from the distillation column reactor system as an overheads; and operating the distillation column reactor system such that the etherification reaction zone is substantially free of propionitrile.

8. 发明公开

EP1513791A2 PROCESS AND APPARATUS FOR CATALYTIC DISTILLATIONS 有权
标题翻译：方法和装置催化蒸馏
公开(公告)号：EP1513791A2
公开(公告)日：2005-03-16
申请号：EP03733858.9
申请日：2003-04-16
申请人： Catalytic Distillation Technologies
发明人： GROTEN, Willibrord, A. , MARASCHINO, Mario, J.
IPC分类号： C07C41/00 , C07C2/02 , C07C2/56 , B01D3/34 , B01D3/00
CPC分类号： B01D3/141 , B01D3/009 , C07C2/06 , C07C2/66 , C07C5/03 , C07C5/10 , C07C5/23 , C07C5/2506 , C07C5/27 , C07C41/06 , C07C41/42 , C07C319/18 , Y02P20/127 , C07C43/046
摘要： A process for reacting a first component with itself or a second component to produce a third component in which a first material comprising a first component or said first component and a second component is fed to divided wall column having a catalytic distillation structure in at least one of the separate vertical sections of the divided wall column where concurrently: (1) a first component alone or with a second component is contacted with a catalytic distillation structure in a distillation reaction zone thereby catalytically reacting at least a portion of the first component with itself or with the second component to form a product and (2) a first mixture comprising the first component and the product or the first component, the second component and the product; and withdrawing the product from the distillation column reactor; while within the column concurrently with the catalytic reaction and fractionation a second mixture is fractionated, which contains the first component and the product or first and second components (if a second component is present) and the product in a parallel and separate distillation non reaction zone to fractionate the product and withdrawing the product from said distillation non reaction zone. For example, tertiary amyl methyl ether may be prepared by reacting methanol with isoamylene in a C5 stream utilizing a distillation column reactor wherein the distillation column reactor comprises one side of a divided wall column. On one side the product, tertiary amyl methyl ether, is separated from the unreacted methanol and C5's and on the other side the remaining isoamylenes are reacted with methanol and a separation of the tertiary amyl methyl ether and C5's from the methanol/C5 azeotrope is effected.

9. 发明授权

EP0991613B1 OLEFIN SKELETAL ISOMERIZATION PROCESS 失效
标题翻译：方法烯烃骨骼
公开(公告)号：EP0991613B1
公开(公告)日：2004-03-24
申请号：EP98923872.0
申请日：1998-06-02
申请人： Catalytic Distillation Technologies
发明人： RYU, J., Yong , GROTEN, Willibrord, A.
IPC分类号： C07C11/02 , C07C2/66 , C07C4/14 , C07C5/22
CPC分类号： C07C11/02 , Y02P20/127
摘要： An isomerization process for C4 to C15 olefins carried out by the reaction of C4 to C15 olefins, having a first skeletal distribution, with aromatic compounds under alkylation conditions to produce an alkylated aromatic product, dealkylation of the alkylated aromatic product under dealkylation conditions to produce a dealkylated product comprising said aromatic compounds and olefins corresponding to the olefins in the alkylation and having a second skeletal distribution different than said first skeletal distribution. Acidic catalysts such as molecular sieves are used in both alkylation and dealkylation. The reactions may be carried out in either straight pass fixed beds or in catalytic distillation reactors.

10. 发明授权

EP1513791B1 PROCESS AND APPARATUS FOR CATALYTIC DISTILLATIONS 有权
标题翻译：方法和装置催化蒸馏
公开(公告)号：EP1513791B1
公开(公告)日：2011-06-15
申请号：EP03733858.9
申请日：2003-04-16
申请人： Catalytic Distillation Technologies
发明人： GROTEN, Willibrord, A. , MARASCHINO, Mario, J.
IPC分类号： C07C41/00 , C07C2/02 , C07C2/56 , B01D3/34 , B01D3/00
CPC分类号： B01D3/141 , B01D3/009 , C07C2/06 , C07C2/66 , C07C5/03 , C07C5/10 , C07C5/23 , C07C5/2506 , C07C5/27 , C07C41/06 , C07C41/42 , C07C319/18 , Y02P20/127 , C07C43/046
摘要： A process for reacting a first component with itself or a second component to produce a third component in which a first material comprising a first component or said first component and a second component is fed to divided wall column having a catalytic distillation structure in at least one of the separate vertical sections of the divided wall column where concurrently: (1) a first component alone or with a second component is contacted with a catalytic distillation structure in a distillation reaction zone thereby catalytically reacting at least a portion of the first component with itself or with the second component to form a product and (2) a first mixture comprising the first component and the product or the first component, the second component and the product; and withdrawing the product from the distillation column reactor; while within the column concurrently with the catalytic reaction and fractionation a second mixture is fractionated, which contains the first component and the product or first and second components (if a second component is present) and the product in a parallel and separate distillation non reaction zone to fractionate the product and withdrawing the product from said distillation non reaction zone. For example, tertiary amyl methyl ether may be prepared by reacting methanol with isoamylene in a C5 stream utilizing a distillation column reactor wherein the distillation column reactor comprises one side of a divided wall column. On one side the product, tertiary amyl methyl ether, is separated from the unreacted methanol and C5's and on the other side the remaining isoamylenes are reacted with methanol and a separation of the tertiary amyl methyl ether and C5's from the methanol/C5 azeotrope is effected.

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式