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公开(公告)号：US08246914B2
公开(公告)日：2012-08-21
申请号：US12340945
申请日：2008-12-22
CPC分类号： C10G11/18 , C10G2300/1044 , C10G2300/1088 , C10G2300/301 , C10G2400/02 , C10G2400/20
摘要： One exemplary embodiment can be a fluid catalytic cracking system. The system can include a reaction zone operating at conditions to facilitate olefin production and including at least one riser. The at least one riser can receive a first feed having a boiling point of about 180-about 800° C., and a second feed having more than about 70%, by weight, of one or more C4+ olefins.
摘要翻译： 一个示例性实施方案可以是流化催化裂化系统。 该系统可以包括在促进烯烃生产的条件下操作并包括至少一个提升管的反应区。 所述至少一个提升管可以接收沸点为约180-约800℃的第一进料，以及具有大于约70重量％的一种或多种C 4 +烯烃的第二进料。
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公开(公告)号：US20100329946A1
公开(公告)日：2010-12-30
申请号：US12493662
申请日：2009-06-29
申请人： Robert L. Mehlberg
发明人： Robert L. Mehlberg
CPC分类号： B01D5/0006 , B01D3/14 , B01D3/32 , B01D5/0063 , B01D5/0078 , B01D5/0084 , B01J19/24 , B01J2219/00103 , B01J2219/24 , C07C2/66 , F28D15/00
摘要： One exemplary embodiment can be a process for cooling a vent stream from a receiver. Generally, the process may include providing a refrigerant including at least one compound contained in the receiver so the refrigerant leaking into the receiver can be compatible with the process.
摘要翻译： 一个示例性实施例可以是用于从接收器冷却排气流的过程。 通常，该方法可以包括提供包含接收器中包含的至少一种化合物的制冷剂，使得泄漏到接收器中的制冷剂可以与该方法兼容。
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63.发明申请ALKYLATION SYSTEM INCLUDING A CATALYST REGENERATION ZONE, AND A PROCESS RELATING THERETO 有权包括催化再生区的碱化系统及其相关过程公开(公告)号：US20100304956A1
公开(公告)日：2010-12-02
申请号：US12476235
申请日：2009-06-01
申请人： Robert L. Mehlberg
发明人： Robert L. Mehlberg
CPC分类号： B01J27/32 , C07C2/62 , C07C2527/1206 , Y02P20/584
摘要： One exemplary embodiment can be an alkylation system including a catalyst regeneration zone. Generally, the catalyst regeneration zone includes first and second columns. The first column can provide an overhead stream having a catalyst and a first hydrocarbon, a side-stream having the catalyst and water, and a bottom stream having a second hydrocarbon. Typically, the second column receives the side-stream as a feed.
摘要翻译： 一个示例性实施方案可以是包括催化剂再生区的烷基化系统。 通常，催化剂再生区包括第一和第二柱。 第一塔可以提供具有催化剂和第一烃，具有催化剂和水的侧流以及具有第二烃的塔底料流的塔顶料流。 通常，第二列接收侧流作为馈送。
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公开(公告)号：US20100168488A1
公开(公告)日：2010-07-01
申请号：US12344598
申请日：2008-12-29
CPC分类号： C07C4/06 , B01J8/26 , B01J29/084 , B01J29/40 , B01J29/80 , B01J29/90 , B01J38/30 , B01J2208/025 , C07C2529/48 , C10G51/00 , C10G51/026 , C10G51/06 , C10G2300/107 , C10G2300/1074 , C10G2300/301 , C10G2400/20
摘要： One exemplary embodiment can be a fluid catalytic cracking system. Generally, the fluid catalytic cracking system includes a first reaction vessel and a second reaction vessel. The first reaction vessel may contain a first catalyst having pores with openings greater than about 0.7 nm and a second catalyst having pores with smaller openings than the first catalyst. What is more, the second reaction vessel may contain the second catalyst. Generally, at least a portion of the second catalyst is directly communicated with the first reaction vessel.
摘要翻译： 一个示例性实施方案可以是流化催化裂化系统。 通常，流化催化裂化系统包括第一反应容器和第二反应容器。 第一反应容器可以含有具有大于约0.7nm的孔的孔的第一催化剂和具有比第一催化剂小的开口的孔的第二催化剂。 此外，第二反应容器可以含有第二催化剂。 通常，第二催化剂的至少一部分与第一反应容器直接连通。
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公开(公告)号：US20100158767A1
公开(公告)日：2010-06-24
申请号：US12340945
申请日：2008-12-22
IPC分类号： B01J8/24
CPC分类号： C10G11/18 , C10G2300/1044 , C10G2300/1088 , C10G2300/301 , C10G2400/02 , C10G2400/20
摘要： One exemplary embodiment can be a fluid catalytic cracking system. The system can include a reaction zone operating at conditions to facilitate olefin production and including at least one riser. The at least one riser can receive a first feed having a boiling point of about 180-about 800° C., and a second feed having more than about 70%, by weight, of one or more C4+ olefins.
摘要翻译： 一个示例性实施方案可以是流化催化裂化系统。 该系统可以包括在促进烯烃生产的条件下操作并包括至少一个提升管的反应区。 所述至少一个提升管可以接收沸点为约180-约800℃的第一进料，以及具有大于约70重量％的一种或多种C 4 +烯烃的第二进料。
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公开(公告)号：US20100155299A1
公开(公告)日：2010-06-24
申请号：US12340291
申请日：2008-12-19
申请人： Robert L. Mehlberg
发明人： Robert L. Mehlberg
CPC分类号： C07C4/06 , C07C2529/40 , C10G11/18 , C10G2400/20
摘要： One exemplary embodiment can be a fluid catalytic cracking system. The system can include a reaction zone, in turn including a reactor receiving, a fluidizing stream, a fuel gas stream, a fluidizable catalyst, a stream having an effective amount of oxygen for combusting the fuel gas stream, and a feed.
摘要翻译： 一个示例性实施方案可以是流化催化裂化系统。 该系统可以包括反应区，反过来又包括反应器接收流化流，燃料气流，可流化的催化剂，具有有效量的用于燃烧燃料气流的氧的流和进料。
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公开(公告)号：US06943276B1
公开(公告)日：2005-09-13
申请号：US10172297
申请日：2002-06-12
CPC分类号： C07C2/58 , Y02P20/582 , C07C9/16
摘要： An alkylation process in which a recycle stream is cooled by heat exchange with the alkylation reactor effluent is disclosed.
摘要翻译： 公开了通过与烷基化反应器流出物进行热交换来冷却循环物流的烷基化方法。
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公开(公告)号：US6111159A
公开(公告)日：2000-08-29
申请号：US203019
申请日：1998-12-01
CPC分类号： C07C2/18 , C07C2/70 , C10G50/00 , C07C2527/173
摘要： A method is provided for putting a fresh bed of solid phosphoric acid catalyst into service to catalyze a hydrocarbon conversion process. The method involves establishing hydrocarbon conversion conditions of temperature and pressure in the catalyst bed while it is immersed in a hydrocarbon liquid which is substantially free of water and compounds which can yield water upon contact with the catalyst. Thereafter, the catalyst bed is used to catalyze the conversion of a hydrocarbon feedstock which contains a minor amount of a hydrating agent which is effective to provide a desired level of catalyst hydration. The method permits the catalyst to be rapidly brought to an optimum level of activity for the specific hydrocarbon conversion process.
摘要翻译： 提供了一种将新鲜的固体磷酸催化剂床用于催化烃转化过程的方法。 该方法包括在浸入基本上不含水的烃液体中和在与催化剂接触时可产生水的化合物时，在催化剂床中建立温度和压力的烃转化条件。 此后，催化剂床用于催化含有少量水合剂的烃原料的转化，其有效提供所需水平的催化剂水合。 该方法允许催化剂快速地达到特定烃转化过程的最佳活性水平。
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公开(公告)号：US06025534A
公开(公告)日：2000-02-15
申请号：US56212
申请日：1998-04-07
CPC分类号： C10G50/00 , C07C2/18 , C08F10/00 , C07C2527/173 , Y02P20/584
摘要： A method is provided for regenerating a fixed bed of olefin polymerization catalyst which can be performed without taking the catalyst bed out of service. The method involves the use of two different olefin-containing feedstocks, wherein the first feedstock is a conventional olefin-containing feedstock which contains little if any content of aromatic compounds. The second feedstock contains a significant concentration of aromatic compounds. In the practice of the invention, the second feedstock is substituted for the first feedstock whenever catalyst regeneration is deemed appropriate, and the flow of the second feedstock to the catalyst bed is continued for a period of time which is effective to at least partially regenerate the catalyst.
摘要翻译： 提供了一种用于再生烯烃聚合催化剂固定床的方法，其可以在不使催化剂床停止使用的情况下进行。 该方法涉及使用两种不同的含烯烃原料，其中第一种原料是常规的含烯烃原料，其含有少量芳族化合物。 第二原料含有显着浓度的芳族化合物。 在本发明的实践中，当催化剂再生被认为合适时，第二原料代替第一原料，并且将第二原料流向催化剂床的流程持续一段时间，这一时间段至少部分地再生 催化剂。
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70.发明授权Oxidative coupling process for converting methane and/or natural gas to more transportable products 失效将甲烷和/或天然气转化为更多可运输产品的氧化偶合方法
公开(公告)号：US5015799A
公开(公告)日：1991-05-14
申请号：US376307
申请日：1989-07-06
申请人： Robert H. Walker , Paul A. Willems , George A. Huff , Lewis E. Grimes , David F. Tatterson , Robert L. Mehlberg
发明人： Robert H. Walker , Paul A. Willems , George A. Huff , Lewis E. Grimes , David F. Tatterson , Robert L. Mehlberg
IPC分类号： C07C2/82
CPC分类号： C07C2/82 , Y10S585/943
摘要： A method for converting methane to higher molecular weight hydrocarbons wherein hot oxidative coupling reactor effluent is briefly contacted with a C.sub.2 to C.sub.20 alkane quench material to remove part of the heat contained in the raw reactor effluent, and is then further quenched by thermal quenching means to achieve a temperature which discourages retrograde reactions.
摘要翻译： 一种将甲烷转化为较高分子量烃的方法，其中热氧偶联反应器流出物与C2至C20烷烃淬火材料短暂接触以除去生反应器流出物中所含的一部分热量，然后通过热淬火装置进一步淬火 达到避免逆行反应的温度。
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