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1.发明申请公开(公告)号：US20120168154A1
公开(公告)日：2012-07-05
申请号：US13332205
申请日：2011-12-20
IPC分类号： E21B43/00
CPC分类号： E21B43/34 , B01D53/1468 , B01D53/229 , B01D2252/204 , B01D2256/24 , B01D2257/304 , B01D2257/504 , C10L3/103 , C10L3/104 , C10L2290/545 , C10L2290/548 , Y02C10/06 , Y02C10/10
摘要： A method and system for processing produced fluids from a subterranean reservoir is disclosed. The system comprises: (a) a separator for separating produced fluids from a subterranean reservoir into associated gases, water and crude oil, (b) a membrane which receives at least a portion of the associated gases containing the hydrogen sulfide and separates the gas into a permeate stream enriched in hydrogen sulfide and carbon dioxide and a retentate stream depleted in hydrogen sulfide and carbon dioxide; (c) an amine unit for removing carbon dioxide and hydrogen sulfide from the retentate stream; and (d) a sour gas injection unit for injecting at the permeate stream in an underground formation.
摘要翻译： 公开了一种从地下储层处理产生的流体的方法和系统。 该系统包括：（a）用于将产生的流体从地下储层分离成相关气体，水和原油的分离器，（b）接收至少一部分含有硫化氢的相关气体并将气体分离成 富含硫化氢和二氧化碳的渗透物流和贫化硫化氢和二氧化碳的滞留物流; （c）用于从滞留物流中除去二氧化碳和硫化氢的胺单元; 以及（d）用于在渗透流中注入地下地层的酸性气体注入单元。
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2.发明授权公开(公告)号：US08869890B2
公开(公告)日：2014-10-28
申请号：US13332205
申请日：2011-12-20
CPC分类号： E21B43/34 , B01D53/1468 , B01D53/229 , B01D2252/204 , B01D2256/24 , B01D2257/304 , B01D2257/504 , C10L3/103 , C10L3/104 , C10L2290/545 , C10L2290/548 , Y02C10/06 , Y02C10/10
摘要： A method and system for processing produced fluids from a subterranean reservoir is disclosed. The system comprises: (a) a separator for separating produced fluids from a subterranean reservoir into associated gases, water and crude oil, (b) a membrane which receives at least a portion of the associated gases containing the hydrogen sulfide and separates the gas into a permeate stream enriched in hydrogen sulfide and carbon dioxide and a retentate stream depleted in hydrogen sulfide and carbon dioxide; (c) an amine unit for removing carbon dioxide and hydrogen sulfide from the retentate stream; and (d) a sour gas injection unit for injecting at the permeate stream in an underground formation.
摘要翻译： 公开了一种从地下储层处理产生的流体的方法和系统。 该系统包括：（a）用于将产生的流体从地下储层分离成相关气体，水和原油的分离器，（b）接收至少一部分含有硫化氢的相关气体并将气体分离成 富含硫化氢和二氧化碳的渗透物流和贫化硫化氢和二氧化碳的滞留物流; （c）用于从滞留物流中除去二氧化碳和硫化氢的胺单元; 以及（d）用于在渗透流中注入地下地层的酸性气体注入单元。
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3.发明申请Oxygenated hydrocarbon compositions and method for recovering the compositions 审中-公开氧化烃组合物和回收组合物的方法公开(公告)号：US20050222474A1
公开(公告)日：2005-10-06
申请号：US11137629
申请日：2005-05-25
申请人： Minquan Cheng , Michael Nicoletti
发明人： Minquan Cheng , Michael Nicoletti
摘要： Disclosed is a method of recovering oxygenates from an olefin production process and oxygenate compositions that can be recovered from an olefin production process. The recovered oxygenate compositions comprise a mixture of alcohols, ethers, ketones, and/or aldehydes.
摘要翻译： 公开了一种从烯烃生产过程中回收含氧化合物和从烯烃生产过程中回收的含氧化合物组合物的方法。 回收的含氧化合物组合物包含醇，醚，酮和/或醛的混合物。
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4.发明授权Process of removing contaminants from an olefin stream using extractive distillation 有权使用萃取蒸馏从烯烃流中除去污染物的方法公开(公告)号：US06559248B2
公开(公告)日：2003-05-06
申请号：US09943695
申请日：2001-08-31
申请人： Dan E. Hendriksen , Minquan Cheng , Keith H. Kuechler , David R. Lumgair , Michael P. Nicoletti , Richard Shutt
发明人： Dan E. Hendriksen , Minquan Cheng , Keith H. Kuechler , David R. Lumgair , Michael P. Nicoletti , Richard Shutt
IPC分类号： C08F1006
摘要： Disclosed is a method of purifying olefin containing oxygenate contaminants. The method incorporates the use of extractive distillation. Under the appropriate conditions, olefins containing very low levels of oxygenate contaminants can be recovered.
摘要翻译： 公开了一种纯化含有含氧化合物污染物的烯烃的方法。 该方法包括萃取蒸馏的使用。 在合适的条件下，可以回收含有非常低水平的含氧化合物污染物的烯烃。
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5.发明申请Acetylene Enhanced Conversion of Syngas to Fischer-Tropsch Hydrocarbon Products 失效乙炔增强合成气转化为费 - 托烃产品公开(公告)号：US20120172459A1
公开(公告)日：2012-07-05
申请号：US13421601
申请日：2012-03-15
IPC分类号： C07C27/00
CPC分类号： C10G2/32 , C10G2300/304
摘要： A method is disclosed for converting syngas to Fischer-Tropsch (F-T) hydrocarbon products. A synthesis gas including carbon monoxide and hydrogen gas is provided to a F-T reactor. Also, acetylene is supplied to the F-T reactor. The ratio of the volume of acetylene to the volume of synthesis gas is at least 0.01. The synthesis gas and acetylene are reacted under suitable reaction conditions and in the presence of a catalyst to produce F-T hydrocarbon products. The F-T hydrocarbon products are then recovered from the reactor. The synthesis gas and acetylene may be provided in a combined feed stream or introduced separately into the reactor. The acetylene enhanced syngas conversion in a F-T reactor results in the synthesis of F-T products which have a tighter distribution of intermediate length carbon products than do F-T products synthesized according to conventional methods.
摘要翻译： 公开了将合成气转化为费 - 托（F-T）烃产物的方法。 将包含一氧化碳和氢气的合成气体提供给F-T反应器。 此外，向F-T反应器供应乙炔。 乙炔体积与合成气体积之比至少为0.01。 合成气和乙炔在合适的反应条件下和催化剂存在下反应生成F-T烃产物。 然后从反应器中回收F-T烃产物。 合成气和乙炔可以以组合的进料流提供或分开引入反应器。 在F-T反应器中乙炔增强的合成气转化导致F-T产物的合成，其具有与根据常规方法合成的F-T产物相比中等长度碳产物分布更严格的F-T产物。
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公开(公告)号：US20050215698A1
公开(公告)日：2005-09-29
申请号：US10810739
申请日：2004-03-26
申请人： Venkatkrishna Raghavendran , Daniel Woodman , Erich Teutsch , Ralph Buoniconti , Scott Davis , Paul Bristow , Minquan Cheng , Daniel Sowle , Benny David
发明人： Venkatkrishna Raghavendran , Daniel Woodman , Erich Teutsch , Ralph Buoniconti , Scott Davis , Paul Bristow , Minquan Cheng , Daniel Sowle , Benny David
CPC分类号： B32B27/06 , B32B5/28 , B32B27/08 , B32B2260/021 , B32B2260/046 , B32B2307/3065 , B32B2419/00 , B32B2605/00 , D21H13/20 , D21H13/40 , Y10T428/31507 , Y10T428/31551 , Y10T428/31562 , Y10T428/31721 , Y10T428/31833
摘要： A composite sheet material that includes at least one porous core layer including a thermoplastic material and from about 20 weight percent to about 80 weight percent fibers based on a total weight of the porous core layer, and at least one skin covering a surface of the core layer. The skin includes at least one of a thermoplastic film, a fiber based scrim, a non-woven fabric, and a woven fabric.
摘要翻译： 一种复合片材材料，其包括至少一个包含热塑性材料的多孔芯层和基于所述多孔芯层的总重量的约20重量％至约80重量％的纤维，以及至少一个覆盖所述芯的表面的皮肤 层。 皮肤包括热塑性薄膜，纤维系稀松布，无纺布和机织织物中的至少一种。
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公开(公告)号：US08258195B2
公开(公告)日：2012-09-04
申请号：US13421601
申请日：2012-03-15
IPC分类号： C07C27/00
CPC分类号： C10G2/32 , C10G2300/304
摘要： A method is disclosed for converting syngas to Fischer-Tropsch (F-T) hydrocarbon products. A synthesis gas including carbon monoxide and hydrogen gas is provided to a F-T reactor. Also, acetylene is supplied to the F-T reactor. The ratio of the volume of acetylene to the volume of synthesis gas is at least 0.01. The synthesis gas and acetylene are reacted under suitable reaction conditions and in the presence of a catalyst to produce F-T hydrocarbon products. The F-T hydrocarbon products are then recovered from the reactor. The synthesis gas and acetylene may be provided in a combined feed stream or introduced separately into the reactor. The acetylene enhanced syngas conversion in a F-T reactor results in the synthesis of F-T products which have a tighter distribution of intermediate length carbon products than do F-T products synthesized according to conventional methods.
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8.发明申请ACETYLENE ENHANCED CONVERSION OF SYNGAS TO FISCHER-TROPSCH HYDROCARBON PRODUCTS 失效乙烯增强转化为FISCHER-TROPSCH碳氢化合物产品公开(公告)号：US20090170965A1
公开(公告)日：2009-07-02
申请号：US12342978
申请日：2008-12-23
IPC分类号： C07C27/04
CPC分类号： C10G2/32 , C10G2300/304
摘要： A method is disclosed for converting syngas to Fischer-Tropsch (F-T) hydrocarbon products. A synthesis gas including carbon monoxide and hydrogen gas is provided to a F-T reactor. Also, acetylene is supplied to the F-T reactor. The ratio of the volume of acetylene to the volume of synthesis gas is at least 0.01. The synthesis gas and acetylene are reacted under suitable reaction conditions and in the presence of a catalyst to produce F-T hydrocarbon products. The F-T hydrocarbon products are then recovered from the reactor. The synthesis gas and acetylene may be provided in a combined feed stream or introduced separately into the reactor. The acetylene enhanced syngas conversion in a F-T reactor results in the synthesis of F-T products which have a tighter distribution of intermediate length carbon products than do F-T products synthesized according to conventional methods.
摘要翻译： 公开了将合成气转化为费 - 托（F-T）烃产物的方法。 将包含一氧化碳和氢气的合成气体提供给F-T反应器。 此外，向F-T反应器供应乙炔。 乙炔体积与合成气体积之比至少为0.01。 合成气和乙炔在合适的反应条件下和催化剂存在下反应生成F-T烃产物。 然后从反应器中回收F-T烃产物。 合成气和乙炔可以以组合的进料流提供或分开引入反应器。 在F-T反应器中乙炔增强的合成气转化导致F-T产物的合成，其具有与根据常规方法合成的F-T产物相比中等长度碳产物分布更严格的F-T产物。
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公开(公告)号：US20060111601A1
公开(公告)日：2006-05-25
申请号：US10511241
申请日：2002-09-30
申请人： Minquan Cheng , Jeffrey Phillips , Michael Nicoletti , David Lumgard Jr. , John Shutt , Jeffrey Kabin , Wilfried Borgmann , Josef Kunkel , Helmut Fritz , Roland Walzi , Gerhard Lauermann , Klaus Muller
发明人： Minquan Cheng , Jeffrey Phillips , Michael Nicoletti , David Lumgard Jr. , John Shutt , Jeffrey Kabin , Wilfried Borgmann , Josef Kunkel , Helmut Fritz , Roland Walzi , Gerhard Lauermann , Klaus Muller
摘要： This invention is directed to a method of removing dimethyl ether from an olefin stream. The method includes distilling the olefin stream so that the dimethyl ether is separated out of the olefin stream with propane. The olefin stream can then be further distilled to provide a polymer grade ethylene stream and a polymer grade propylene stream, with each stream containing not greater than about 10 wppm dimethyl ether.
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10.发明授权Acetylene enhanced conversion of syngas to Fischer-Tropsch hydrocarbon products 失效乙炔增强合成气转化为费 - 托烃产品公开(公告)号：US08163808B2
公开(公告)日：2012-04-24
申请号：US12342978
申请日：2008-12-23
IPC分类号： C07C27/00
CPC分类号： C10G2/32 , C10G2300/304
摘要： A method is disclosed for converting syngas to Fischer-Tropsch (F-T) hydrocarbon products. A synthesis gas including carbon monoxide and hydrogen gas is provided to a F-T reactor. Also, acetylene is supplied to the F-T reactor. The ratio of the volume of acetylene to the volume of synthesis gas is at least 0.01. The synthesis gas and acetylene are reacted under suitable reaction conditions and in the presence of a catalyst to produce F-T hydrocarbon products. The F-T hydrocarbon products are then recovered from the reactor. The synthesis gas and acetylene may be provided in a combined feed stream or introduced separately into the reactor. The acetylene enhanced syngas conversion in a F-T reactor results in the synthesis of F-T products which have a tighter distribution of intermediate length carbon products than do F-T products synthesized according to conventional methods.
摘要翻译： 公开了将合成气转化为费 - 托（F-T）烃产物的方法。 将包含一氧化碳和氢气的合成气体提供给F-T反应器。 此外，将乙炔供给到F-T反应器。 乙炔体积与合成气体积之比至少为0.01。 合成气和乙炔在合适的反应条件下和催化剂存在下反应生成F-T烃产物。 然后从反应器中回收F-T烃产物。 合成气和乙炔可以以组合的进料流提供或分开引入反应器。 在F-T反应器中乙炔增强的合成气转化导致F-T产物的合成，其具有与根据常规方法合成的F-T产物相比中等长度碳产物分布更严格的F-T产物。
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