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公开(公告)号：US06416659B1
公开(公告)日：2002-07-09
申请号：US09640835
申请日：2000-08-17
IPC分类号： C10G4502
CPC分类号： C10G45/02 , C10G2300/4087
摘要： A process for the hydrodesulfurization of a diesel boiling range petroleum fraction wherein the hydrodesulfurization is carried out concurrently with a fractional distillation in a distillation column reactor containing a catalyst bed. The diesel is fed above the catalyst bed and hydrogen is fed below the bed. The bottoms from the distillation column reactor is then separated by fractional distillation to remove a bottoms containing most of the unconverted sulfur.
摘要翻译： 一种柴油沸程石油馏分的加氢脱硫方法，其中加氢脱硫在含有催化剂床的蒸馏塔反应器中与分馏同时进行。 柴油进料到催化剂床上方，氢气被送入床底。 然后通过分馏分离来自蒸馏塔反应器的塔底物以除去含有大部分未转化的硫的塔底物。
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公开(公告)号：US07553995B2
公开(公告)日：2009-06-30
申请号：US11853351
申请日：2007-09-11
申请人： Christopher C. Boyer , Mitchell E. Loescher , Willibrord A. Groten , Mario J. Maraschino , Kerry L. Rock
发明人： Christopher C. Boyer , Mitchell E. Loescher , Willibrord A. Groten , Mario J. Maraschino , Kerry L. Rock
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.
摘要翻译： 一种生产叔醚的方法，包括：将含有异烯烃和丙腈的烃流进料到含有至少一个醚化反应区的蒸馏塔反应器系统中; 将C2至C6一元醇或其混合物加入蒸馏塔反应器中; 同时在蒸馏塔反应器系统中：使一部分异烯烃与一部分醇反应形成叔乙醚; 并将叔醚与未反应的异烯烃分离; 从蒸馏塔反应器系统中取出叔醚和丙腈作为底部物质; 从蒸馏塔反应器系统中取出未反应的异烯烃作为塔顶馏出物; 并操作蒸馏塔反应器系统，使得醚化反应区基本上不含丙腈。
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公开(公告)号：US20090069608A1
公开(公告)日：2009-03-12
申请号：US11853351
申请日：2007-09-11
申请人： Christopher C. Boyer , Mitchell E. Loescher , Willibrord A. Groten , Mario J. Maraschino , Kerry L. Rock
发明人： Christopher C. Boyer , Mitchell E. Loescher , Willibrord A. Groten , Mario J. Maraschino , Kerry L. Rock
IPC分类号： C07C41/08
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.
摘要翻译： 一种生产叔醚的方法，包括：将含有异烯烃和丙腈的烃流进料到含有至少一个醚化反应区的蒸馏塔反应器系统中; 将C2至C6一元醇或其混合物加入蒸馏塔反应器中; 同时在蒸馏塔反应器系统中：使一部分异烯烃与一部分醇反应形成叔乙醚; 并将叔醚与未反应的异烯烃分离; 从蒸馏塔反应器系统中取出叔醚和丙腈作为底部物质; 从蒸馏塔反应器系统中取出未反应的异烯烃作为塔顶馏出物; 并操作蒸馏塔反应器系统，使得醚化反应区基本上不含丙腈。
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公开(公告)号：US07030277B2
公开(公告)日：2006-04-18
申请号：US10839401
申请日：2004-05-05
IPC分类号： C07C319/00 , C07C41/05 , C07C41/06 , B01D3/34
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.
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公开(公告)号：US06946068B2
公开(公告)日：2005-09-20
申请号：US09877277
申请日：2001-06-08
申请人： Willibrord A. Groten
发明人： Willibrord A. Groten
IPC分类号： B01J23/44 , B01J23/755 , B01J23/882 , C10G7/00 , C10G45/02 , C10G45/08 , C10G45/10 , C10G45/32 , C10G45/40 , C10G45/04 , B01D3/34
CPC分类号： C10G45/08 , B01J23/44 , B01J23/755 , B01J23/882 , C10G7/00 , C10G45/02 , C10G45/10 , C10G45/32 , C10G45/40 , C10G2300/4087
摘要： A process for concurrently fractionating and hydrotreating of a full range naphtha stream. The full boiling range naphtha stream, for example which is derived from fluid catalytic cracking, is first subjected to simultaneous hydrogenation of the thiophene contained therein and thioetherification and fractionation to remove the mercaptans the light fraction and then to simultaneous hydrodesulfurization and splitting of the bottoms into an intermediate boiling range naphtha and a heavy boiling range naphtha. The three boiling range naphthas are treated separately according to the amount of sulfur in each cut and the end use of each fraction.
摘要翻译： 一种用于同时分馏和加氢处理全程石脑油流的方法。 首先对来自流化催化裂化的全沸点石脑油流进行同时氢化其中所含的噻吩和硫醚化和分馏以除去轻馏分的硫醇，然后同时加氢脱硫和将塔底分解成 中间沸点石脑油和重沸点石脑油。 根据每个切割中的硫量和每个馏分的最终使用，分别处理三个沸点范围的石脑油。
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公开(公告)号：US06930206B1
公开(公告)日：2005-08-16
申请号：US10167196
申请日：2002-06-11
IPC分类号： B01D3/00 , C07C2/06 , C07C2/66 , C07C5/03 , C07C5/10 , C07C5/23 , C07C5/25 , C07C5/27 , C07C41/06 , C07C41/42 , C07C319/18 , C07C319/00 , B01D3/34 , C07C41/05
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.
摘要翻译： 一种使第一组分与其自身或第二组分反应以产生第三组分的方法，其中将包含第一组分或所述第一组分的第一组分或第二组分加入到具有催化蒸馏结构的至少一种 的分隔壁柱的单独的竖直部分，其中同时：（1）单独的第一组分或与第二组分的第一组分在蒸馏反应区中与催化蒸馏结构接触，从而使第一组分的至少一部分与其自身的催化反应 或与第二组分形成产物和（2）包含第一组分和产物或第一组分，第二组分和产物的第一混合物; 并从蒸馏塔反应器中取出产物; 同时在塔内同时进行催化反应和分馏，将第二混合物分馏，其含有第一组分和产物或第一和第二组分（如果存在第二组分），并且产物在平行和分离的蒸馏非反应区 以分馏产物并从所述蒸馏非反应区抽出产物。 例如，叔戊基甲基醚可以通过使用蒸馏塔反应器的甲醇与C 6 C 5流中的异戊烯反应制备，其中蒸馏塔反应器包括分隔壁塔的一侧。 一方面，将产物叔戊基甲基醚与未反应的甲醇和C 5 S分离，另一侧将剩余的异戊烯与甲醇反应并分离叔戊基甲基醚 和来自甲醇/ C 5 H 3共沸物的C 5 S 5。
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公开(公告)号：US06620965B1
公开(公告)日：2003-09-16
申请号：US10093708
申请日：2002-03-08
IPC分类号： C07C67055
CPC分类号： C07C67/055 , C07C69/01 , C07C69/15
摘要： A process for producing vinyl acetate comprising reacting ethylene, acetic acid and oxygen together in at least partially liquid phase in the presence of a catalyst comprising a noble metal component.
摘要翻译： 一种生产乙酸乙烯酯的方法，包括在包含贵金属组分的催化剂的存在下，使至少部分液相中的乙烯，乙酸和氧一起反应。
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公开(公告)号：US20100063334A1
公开(公告)日：2010-03-11
申请号：US12206039
申请日：2008-09-08
申请人： Montri Vichailak , Purvis K. Ho , Martinus J. Almering , Arvids Judzis, JR. , Willibrord A. Groten , Lawrence A. Smith, JR. , Yongqiang Xu
发明人： Montri Vichailak , Purvis K. Ho , Martinus J. Almering , Arvids Judzis, JR. , Willibrord A. Groten , Lawrence A. Smith, JR. , Yongqiang Xu
IPC分类号： C07C7/163
CPC分类号： C10G45/44 , C10G35/04 , C10G65/04 , Y02P20/127 , Y02P20/132
摘要： A process for reducing the concentration of benzene in a hydrocarbon stream, the process including: fractionating a reformate to form a benzene concentrate fraction comprising benzene and other C6 hydrocarbons, and a heavies fraction comprising C7+ hydrocarbons; and hydrogenating the benzene concentrate fraction to form a hydrocarbon fraction having a reduced benzene concentration.
摘要翻译： 一种用于降低烃流中苯浓度的方法，该方法包括：将重整产物分馏以形成含有苯和其它C 6烃的苯浓缩物馏分，以及包含C7 +烃的重馏分; 并将苯浓缩物馏分氢化以形成苯浓度降低的烃馏分。
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公开(公告)号：US07319176B2
公开(公告)日：2008-01-15
申请号：US11010907
申请日：2004-12-13
申请人： J. Yong Ryu , John R. Adams , Willibrord A. Groten
发明人： J. Yong Ryu , John R. Adams , Willibrord A. Groten
IPC分类号： C07C7/163
CPC分类号： C07C7/167 , C07C5/09 , C07C2523/755 , C07C2523/80 , C07C2523/89
摘要： A process for removing acetylenic compounds using unsulfided metallic nickel or unsulfided metallic nickel modified with metallic Mo, Re, Bi or mixtures in which the catalyst is used alone or is used in combination with other acetylenic selective catalysts. The unsulfided metallic nickel catalyst or modified catalyst must be the first catalyst to contact the hydrocarbon stream.
摘要翻译： 使用用金属Mo，Re，Bi改性的未硫化金属镍或未硫化金属镍除去炔属化合物的方法或其中催化剂单独使用或与其它炔属选择性催化剂组合使用的混合物。 未硫化的金属镍催化剂或改性催化剂必须是与烃流接触的第一催化剂。
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公开(公告)号：US07014833B2
公开(公告)日：2006-03-21
申请号：US10839399
申请日：2004-05-05
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.
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