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公开(公告)号：US20150330706A1
公开(公告)日：2015-11-19
申请号：US14651441
申请日：2013-12-13
CPC分类号： F25J3/0238 , B01D3/343 , C07C1/24 , C07C7/005 , C07C7/04 , C07C7/09 , C07C7/12 , F25J3/0209 , C07C11/04
摘要： A process for removing light components from an ethylene stream may include providing a dried ethylene stream containing ethylene, ethane, CO, CO2, H2, CH4, and C3+ hydrocarbons. The process may include sending the dried ethylene stream to a stripper to produce an overhead stream containing ethylene, CO, H2 and CH4, and a bottom stream containing ethylene, ethane, CO2, and C3+ hydrocarbons. The gaseous phase on top of the stripper may be condensed in a heat exchanger cooled by a refrigerant stream to get a first gaseous phase and a first liquid phase. The first gaseous phase may be condensed in a heat exchanger cooled by liquid ethane or liquid ethylene to get a second gaseous phase containing ethylene CO, H2 and CH4 and a second liquid phase. The first and second liquid phases may be the reflux of the stripper.
摘要翻译： 从乙烯流中除去轻组分的方法可包括提供包含乙烯，乙烷，CO，CO 2，H 2，CH 4和C 3+烃的干燥乙烯流。 该方法可以包括将干燥的乙烯流送至汽提塔，以产生含有乙烯，CO，H 2和CH 4的塔顶物流，以及含有乙烯，乙烷，CO 2和C 3+烃的塔底物流。 汽提器顶部的气相可以在由制冷剂流冷却的热交换器中冷凝，得到第一气相和第一液相。 第一气相可以在由液态乙烷或液体乙烯冷却的热交换器中冷凝，得到含有乙烯CO，H 2和CH 4的第二气相和第二液相。 第一和第二液相可以是汽提器的回流。
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12.发明申请PROCESS FOR RECOVERING HYDROCARBONS FROM POLYOLEFIN PLANTS AND APPARATUS SUITABLE FOR THIS PURPOSE 审中-公开从聚烯烃植物中回收烃类的方法和适用于本目的的装置公开(公告)号：US20150329445A1
公开(公告)日：2015-11-19
申请号：US14381783
申请日：2013-02-09
发明人： Michael Kleiber , Tobias Friederich
IPC分类号： C07C7/09 , F25J3/06 , C08F110/08 , C08F110/14 , C08F110/02 , C08F110/06
CPC分类号： C07C7/09 , B01D53/002 , B01D2256/24 , C08F10/00 , C08F110/02 , C08F110/06 , C08F110/08 , C08F110/14 , F25J3/061 , Y02P20/57 , C07C11/02 , C07C11/04 , C07C11/06 , C08F2/00
摘要： Disclosed herein is a method and apparatus for recovering hydrocarbons from polyolefin plants. A method of the present disclosure includes introducing a hydrocarbon-containing inert gas from a residual monomer separation unit of a polyolefin plant into a condensation and separation device, condensing hydrocarbons from a hydrogen-containing inert gas in the condensation and separation device, separating the condensed inert gas into a condensed hydrocarbon-containing product and purified inert gas in the device, and sending the condensed hydrocarbon-containing product to a downstream further separation device for removal of dissolved gasses therefrom. A device of the present disclosure includes a condensation and separation device for condensing hydrocarbons from an inert gas and separating condensed hydrocarbon-containing inert gas into a condensed hydrocarbon-containing product and a purified inert gas, and a further separation device connected downstream for purifying the condensed hydrocarbon-containing product originating from the condensation and separation device by separating off dissolved gases.
摘要翻译： 本文公开了一种用于从聚烯烃装置回收烃的方法和装置。 本公开的方法包括将来自聚烯烃设备的残余单体分离单元的含烃惰性气体引入冷凝和分离装置中，从冷凝和分离装置中的含氢惰性气体中冷凝烃，将冷凝 将惰性气体转化为含冷凝烃的产物和装置中的纯化惰性气体，并将冷凝的含烃产物送至下游的分离装置，以从其中除去溶解的气体。 本公开的装置包括用于将来自惰性气体的烃和将含冷凝烃的惰性气体分离成冷凝的含烃产物和纯化的惰性气体的冷凝和分离装置，以及连接在下游用于净化 通过分离溶解的气体，来自冷凝和分离装置的冷凝的含烃产物。
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公开(公告)号：US20150239805A1
公开(公告)日：2015-08-27
申请号：US14635041
申请日：2015-03-02
发明人： Vincent A. Welch , James R. Butler
CPC分类号： C07C7/09 , C01B3/24 , C01B3/323 , C01B3/50 , C01B3/506 , C01B2203/0233 , C01B2203/0266 , C01B2203/04 , C01B2203/048 , C01B2203/0495 , C07C5/333 , F25J3/063 , F25J3/0655 , F28B3/00 , F28B9/06 , Y10S585/921 , C07C11/20 , C07C15/46 , C07C11/18
摘要： Methods and systems for the dehydrogenation of hydrocarbons include a direct contact condenser to remove compounds from an offgas process stream. The reduction of compounds can decrease duty on the offgas compressor by removing steam and aromatics from the offgas. The dehydrogenation reaction system can be applicable for reactions such as the dehydrogenation of ethylbenzene to produce styrene, the dehydrogenation of isoamiline to produce isoprene, or the dehydrogenation of n-pentene to produce piperylene.
摘要翻译： 用于烃脱氢的方法和系统包括直接接触冷凝器以从废气处理流中除去化合物。 通过从废气中除去蒸气和芳烃，化合物的还原可以减少废气压缩机的负荷。 脱氢反应体系可适用于乙苯脱氢生产苯乙烯，异戊胺脱氢生产异戊二烯等反应，或正戊烯脱氢生成戊间二烯等反应。
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14.发明申请PROCESS AND APPARATUS FOR PRODUCTION OF AMMONIA SYNTHESIS GAS AND PURE METHANE BY CRYOGENIC SEPARATION 审中-公开通过低温分离生产氨合成气和纯甲烷的方法和装置公开(公告)号：US20130298600A1
公开(公告)日：2013-11-14
申请号：US13979491
申请日：2011-01-17
申请人： Antoine Hernandez , Yuan-Jun Hu , Yanfang Liu , Jean-Marc Tsevery
发明人： Antoine Hernandez , Yuan-Jun Hu , Yanfang Liu , Jean-Marc Tsevery
IPC分类号： F25J3/08
CPC分类号： F25J3/08 , C01B3/506 , C07C7/09 , F25J3/0223 , F25J3/0233 , F25J3/0276 , F25J2200/70 , F25J2200/72 , F25J2205/02 , F25J2205/04 , F25J2205/30 , F25J2210/06 , F25J2210/42 , F25J2215/02 , F25J2220/02 , F25J2260/02 , F25J2270/904 , C07C9/04
摘要： A process for the production of ammonia synthesis gas and pure methane by cryogenic separation of a feed gas containing at least 75% hydrogen as well as methane and nitrogen, the feed gas is cooled in a heat exchanger and partially condensed, the partially condensed feed is sent to a phase separator, the gas from the phase separator is sent to a nitrogen wash column, liquid nitrogen is sent to the top of the nitrogen wash column and ammonia synthesis gas is removed from the top of the nitrogen wash column, the liquid from the phase separator is expanded and sent to a separation column, a nitrogen enriched gas stream is removed from the top of the column and a nitrogen depleted liquid stream rich in methane is removed from the bottom of the column and the nitrogen depleted liquid stream rich in methane is vaporized to form a pure methane product.
摘要翻译： 通过低温分离含有至少75％氢气以及甲烷和氮气的进料气体来生产氨合成气和纯甲烷的方法，将进料气在热交换器中冷却并部分冷凝，部分冷凝的进料为 送到相分离器，将来自相分离器的气体送至氮气洗涤塔，将液氮送至氮气洗涤塔的顶部，氨氮合成气从氮气洗涤塔的顶部除去，液体从 将相分离器膨胀并送入分离塔，从塔顶部除去富氮气流，从塔的底部除去富含甲烷的贫氮液体，富含氮的液态物流 甲烷蒸发形成纯甲烷产物。
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公开(公告)号：US08563793B2
公开(公告)日：2013-10-22
申请号：US12493374
申请日：2009-06-29
CPC分类号： C07C7/04 , C07C5/05 , C07C5/09 , C07C5/333 , C07C5/3337 , C07C7/09 , C07C2521/04 , C07C2523/42 , C07C2523/755 , C07C2527/02 , C10G2400/20 , Y02P20/125 , C07C11/06
摘要： Processes utilizing the integration of (i) processes and the associated equipment used to purify and recover propylene from propane- and/or C4+-containing refinery hydrocarbon streams, with (ii) catalytic dehydrogenation are disclosed. This integration allows for elimination of some or all of the conventional fractionation section of the dehydrogenation process, normally used to purify propylene from unconverted propane in the reactor effluent. Significant capital and utility savings are therefore attained.
摘要翻译： 公开了利用（i）工艺和用于从具有（ii）催化脱氢的丙烷和/或含C4 +的炼油厂烃流中纯化和回收丙烯的方法和相关设备的整合的方法。 该整合允许消除通常用于在反应器流出物中从未转化的丙烷纯化丙烯的脱氢过程的一些或全部常规分馏部分。 因此，实现了大量的资本和效用节省。
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公开(公告)号：US08492605B2
公开(公告)日：2013-07-23
申请号：US13629623
申请日：2012-09-28
申请人： Derek McPhee
发明人： Derek McPhee
IPC分类号： C07C7/00
摘要： A method for producing isoprene comprising an aqueous medium including genetically modified host cells capable of producing isoprene, where the resulting isoprene composition is processed through at least one separation and/or purification process to provide an isoprene enriched composition and a system for doing the same.
摘要翻译： 一种生产异戊二烯的方法，其包括含有能够产生异戊二烯的经遗传修饰的宿主细胞的水性介质，其中所得到的异戊二烯组合物通过至少一种分离和/或纯化方法加工以提供富含异戊二烯的组合物及其制备方法。
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17.发明授权Process for cooling the stream leaving an ethylbenzene dehydrogenation reactor 有权用于冷却离开乙苯脱氢反应器的流的方法公开(公告)号：US08450547B2
公开(公告)日：2013-05-28
申请号：US12744683
申请日：2008-11-21
IPC分类号： C07C5/327
CPC分类号： C07C7/09 , C07C5/333 , C07C2523/745 , C07C15/46
摘要： The present invention is a process for the production of styrene monomer from ethylbenzene comprising the steps of: a) catalytically dehydrogenating said ethylbenzene in the presence of steam thereby catalytically producing a dehydrogenation effluent gas containing essentially unreacted ethylbenzene, styrene monomer, hydrogen, steam and divinylbenzene; b) quenching said effluent gas with an aqueous reflux in at least a quenching column to cool said effluent gas, and thereby obtaining a gas at the overhead and in the bottom a liquid stream warmer than the aqueous reflux; c) condensing said overhead gas thereby producing a liquid organic phase, an aqueous phase and a gaseous phase; d) using a portion or the whole of said aqueous phase of step c) as reflux for said step b) of quenching; e) sending to a decanter the liquid stream obtained at step b) to recover an aqueous phase and an organic phase.
摘要翻译： 本发明是一种由乙苯生产苯乙烯单体的方法，包括以下步骤：a）在蒸汽存在下催化脱氢所述乙苯，从而催化产生基本上未反应的乙苯，苯乙烯单体，氢气，蒸汽和二乙烯基苯的脱氢流出气体 ; b）在至少一个淬火塔中用含水回流淬火所述流出气体以冷却所述流出气体，从而在顶部和底部获得比含水回流加热的液体流的气体; c）冷凝所述塔顶气体，从而产生液体有机相，水相和气相; d）使用步骤c）的所述水相的一部分或全部作为所述步骤b）的回流淬火; e）将在步骤b）中获得的液体流送至滗析器以回收水相和有机相。
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公开(公告)号：US20130030227A1
公开(公告)日：2013-01-31
申请号：US13629623
申请日：2012-09-28
申请人： DEREK MCPHEE
发明人： DEREK MCPHEE
摘要： A method for producing isoprene comprising an aqueous medium including genetically modified host cells capable of producing isoprene, where the resulting isoprene composition is processed through at least one separation and/or purification process to provide an isoprene enriched composition and a system for doing the same.
摘要翻译： 一种生产异戊二烯的方法，其包括含有能够产生异戊二烯的经遗传修饰的宿主细胞的水性介质，其中通过至少一种分离和/或纯化方法处理所得异戊二烯组合物以提供富含异戊二烯的组合物及其制备方法。
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公开(公告)号：US08129577B2
公开(公告)日：2012-03-06
申请号：US12554052
申请日：2009-09-04
申请人： Timothy John Maykut , Suhas Narayan Ketkar , Benjamin James Arthur Inman , John Irven , Eugene Joseph Karwacki, Jr. , Neil Alexander Downie
发明人： Timothy John Maykut , Suhas Narayan Ketkar , Benjamin James Arthur Inman , John Irven , Eugene Joseph Karwacki, Jr. , Neil Alexander Downie
IPC分类号： B65B1/04
摘要： A system and a process for providing acetylene, preferably at a high purity level (e.g., comprising 100 parts per million (“ppm”), or 10 ppm, or 1 ppm, or 100 parts per billion (“ppb”), or 10 ppb, or 1 ppb or less of solvent), to a point of use, such as a semiconductor manufacturing process, is described herein. In one aspect, there is provided a process for providing a process for providing a high purity acetylene comprising 100 ppm or less solvent to a point of use comprising: providing an acetylene feed stream comprising acetylene and solvent at a temperature ranging from 20° C. to −50° C.; and introducing the acetylene feed stream to a purifier at a temperature ranging from −50° C. to 30° C. to remove at least a portion of the solvent contained therein and provide the high purity acetylene.
摘要翻译： 用于提供乙炔的系统和方法，优选在高纯度水平（例如，包括100ppm（“ppm”）或10ppm，或1ppm，或100ppm（“ppb”）或10 ppb或1ppb或更少的溶剂），到本文中描述的诸如半导体制造工艺的使用点。 在一个方面，提供了一种方法，用于提供一种方法，该方法提供包含100ppm或更少溶剂的高纯度乙炔到使用点，包括：在20℃的温度下提供包含乙炔和溶剂的乙炔进料流 至-50℃。 并在-50℃至30℃的温度范围内将乙炔进料流引入净化器中以除去其中所含溶剂的至少一部分，并提供高纯度乙炔。
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公开(公告)号：US20100069689A1
公开(公告)日：2010-03-18
申请号：US12554052
申请日：2009-09-04
申请人： Timothy John Maykut , Suhas Narayan Ketkar , Benjamin James Arthur Inman , John Irven , Eugene Joseph Karwacki, JR. , Neil Alexander Downie
发明人： Timothy John Maykut , Suhas Narayan Ketkar , Benjamin James Arthur Inman , John Irven , Eugene Joseph Karwacki, JR. , Neil Alexander Downie
摘要： A system and a process for providing acetylene, preferably at a high purity level (e.g., comprising 100 parts per million (“ppm”), or 10 ppm, or 1 ppm, or 100 parts per billion (“ppb”), or 10 ppb, or 1 ppb or less of solvent), to a point of use, such as a semiconductor manufacturing process, is described herein. In one aspect, there is provided a process for providing a process for providing a high purity acetylene comprising 100 ppm or less solvent to a point of use comprising: providing an acetylene feed stream comprising acetylene and solvent at a temperature ranging from 20° C. to −50° C.; and introducing the acetylene feed stream to a purifier at a temperature ranging from −50° C. to 30° C. to remove at least a portion of the solvent contained therein and provide the high purity acetylene.
摘要翻译： 用于提供乙炔的系统和方法，优选在高纯度水平（例如，包括100ppm（“ppm”）或10ppm，或1ppm，或100ppm（“ppb”）或10 ppb或1ppb或更少的溶剂），到本文中描述的诸如半导体制造工艺的使用点。 在一个方面，提供了一种方法，用于提供一种方法，该方法提供包含100ppm或更少溶剂的高纯度乙炔到使用点，包括：在20℃的温度下提供包含乙炔和溶剂的乙炔进料流 至-50℃。 并在-50℃至30℃的温度范围内将乙炔进料流引入净化器中以除去其中所含溶剂的至少一部分，并提供高纯度乙炔。
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