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公开(公告)号：US09140447B2
公开(公告)日：2015-09-22
申请号：US13713572
申请日：2012-12-13
Applicant: Lummus Technology Inc.
Inventor： Shuncheng Ji
CPC classification number: F23B5/025 , C10J3/54 , C10J3/56 , C10J3/721 , C10J3/84 , C10J2300/093 , C10J2300/165 , C10J2300/1807 , C10J2300/1884 , C10J2300/1892 , Y02E20/18 , Y02E50/32 , Y02P20/142
Abstract: A dry feed two stage gasification system and process is disclosed for gasifying feedstock such as carbonaceous materials with improved energy efficiency, along with reductions in feedstock consumption and carbon dioxide emissions. The feedstock is first dried and pretreated with the hot syngas in the upper section of the gasifier to generate a dry char that is low in volatile-matter content. This dry char is sent to the first stage of a two stage gasifier where it reacts with oxygen in the presence of steam to produce a hot syngas stream.
Abstract translation: 公开了干饲料两阶段气化系统和方法，用于气化原料，例如具有改善的能量效率的碳质材料，以及原料消耗和二氧化碳排放的减少。 原料首先被干燥并用气化器上部的热合成气进行预处理以产生挥发物含量低的干焦炭。 将该干燥焦炭送入二级气化器的第一阶段，其中在蒸汽存在下与氧气反应产生热合成气流。
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公开(公告)号：US09139491B2
公开(公告)日：2015-09-22
申请号：US13070722
申请日：2011-03-24
Applicant: Stephen De Haan
Inventor： Stephen De Haan
CPC classification number: C07C1/20 , B01J19/24 , B01J2219/00103 , B01J2219/24 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2205/50 , F25J2210/12 , F25J2215/04 , F25J2215/62 , F25J2245/02 , F25J2270/02 , F25J2290/34 , F25J2290/62 , Y02P30/42 , Y02P30/462 , C07C11/04
Abstract: A process for chilling ethylene to required storage temperatures is disclosed, the process including: cooling an ethylene product from at least one of an ethylene production process and an ethylene recovery process via indirect heat exchange with a coolant at a temperature less than about −100° C. to decrease the temperature of the ethylene product; mixing a portion of the cooled ethylene product with methane to form the coolant; expanding at least one of the coolant, the methane, and the portion of the cooled ethylene to reduce a temperature of the coolant to less than −100° C. prior to the cooling; and feeding the heat exchanged coolant to at least one of the ethylene production process, the ethylene recovery process, and an open-loop refrigeration system.
Abstract translation: 公开了一种将乙烯冷却至所需储存温度的方法，该方法包括：通过在低于约-100℃的温度下与冷却剂进行间接热交换从乙烯生产方法和乙烯回收方法中的至少一种冷却乙烯产物 C.降低乙烯产品的温度; 将一部分冷却的乙烯产物与甲烷混合以形成冷却剂; 在冷却之前将冷却剂，甲烷和冷却的乙烯的部分中的至少一个膨胀以将冷却剂的温度降低到小于-100℃; 以及将热交换的冷却剂供给至乙烯生产工艺，乙烯回收工艺和开环制冷系统中的至少一个。
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23.发明授权Catalyst for metathesis of ethylene and 2-butene and/or double bond isomerization 有权用于复分解乙烯和2-丁烯和/或双键异构化的催化剂公开(公告)号：US09040764B2
公开(公告)日：2015-05-26
申请号：US14076613
申请日：2013-11-11
Applicant: Lummus Technology Inc.
Inventor： Bala Ramachandran , Sukwon Choi , Robert J. Gartside , Marvin I. Greene
CPC classification number: C07C5/2512 , B01J21/08 , B01J21/10 , C07C6/04 , C07C2521/04 , C07C2521/08 , C07C2521/10 , C07C2521/16 , C07C2523/02 , C07C2523/04 , C07C2523/30 , Y02P20/52 , C07C11/08 , C07C11/06
Abstract: A process for the double-bond isomerization of olefins is disclosed. The process may include contacting a fluid stream comprising olefins with a fixed bed comprising an activated basic metal oxide isomerization catalyst to convert at least a portion of the olefin to its isomer. The isomerization catalysts disclosed herein may have a reduced cycle to cycle deactivation as compared to conventional catalysts, thus maintaining higher activity over the complete catalyst life cycle.
Abstract translation: 公开了烯烃双键异构化的方法。 该方法可以包括将包含烯烃的流体流与包含活化的碱性金属氧化物异构化催化剂的固定床接触以将至少一部分烯烃转化为其异构体。 与常规催化剂相比，本文公开的异构化催化剂可以具有减少的循环至循环失活，因此在整个催化剂生命周期内保持更高的活性。
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公开(公告)号：US20150141722A1
公开(公告)日：2015-05-21
申请号：US14548509
申请日：2014-11-20
Applicant: Lummus Technology Inc.
Inventor： Bala Ramachandran , Sukwon Choi
CPC classification number: C07C6/04 , B01J8/0453 , B01J2208/025 , B01J2219/00006 , C07C5/2512 , C07C11/02 , C07C11/08
Abstract: Processes for the production of high purity alpha olefins from a mixture of olefins are disclosed. The processes may include: contacting propylene and a hydrocarbon mixture comprising a mixture of olefins having a carbon number n with a first metathesis catalyst to form a metathesis product comprising a beta-olefin having a carbon number n+1, an alpha-olefin having a carbon number n−1, as well as any unreacted propylene and olefins having a carbon number n. The metathesis product may be fractionated to recover a fraction comprising the beta-olefin having a carbon number n+1. Ethylene and the fraction comprising the beta-olefin having a carbon number n+1 may then be contacted with a second metathesis catalyst to form a second metathesis product comprising an alpha-olefin having a carbon number n and propylene, which may be fractionated to form a propylene fraction and a fraction comprising the alpha olefin having a carbon number n.
Abstract translation: 公开了从烯烃混合物生产高纯度α-烯烃的方法。 所述方法可以包括：使丙烯和包含碳数为n的烯烃混合物的烃混合物与第一复分解催化剂接触以形成包含碳数为n + 1的β-烯烃的复分解产物，具有碳原子数为n + 碳数n-1，以及任何未反应的丙烯和碳数为n的烯烃。 复分解产物可以分馏以回收包含碳数为n + 1的β-烯烃的级分。 然后可以将乙烯和包含碳数为n + 1的β-烯烃的馏分与第二复分解催化剂接触以形成包含碳数为n的α-烯烃和丙烯的第二复分解产物，其可以分馏以形成 丙烯馏分和包含碳数为n的α-烯烃的馏分。
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公开(公告)号：US08888876B2
公开(公告)日：2014-11-18
申请号：US13889463
申请日：2013-05-08
Applicant: Lummus Technology Inc.
Inventor： Albert C. Tsang , Chancelor L. Williams , Max W. Thompson , David L. Breton
Abstract: The present invention relates to a system and process for gasifying feedstock such as carbonaceous materials. The invention includes partial combustion of dry solids and pyrolysis of carbonaceous material slurry in two separate reactor sections and produce mixture products comprising synthesis gas. The invention employs one or more catalytic or sorbent bed for removing tar from the synthesis gas. The inventive system and process allow a gasification to be carried out under higher slurry feeding rate and lower temperature with the provision to manage the tar being produced, therefore to increase the conversion efficiency of the overall gasification.
Abstract translation: 本发明涉及用于气化诸如碳质材料的原料的系统和方法。 本发明包括干固体的部分燃烧和碳质材料浆料在两个分离的反应器部分中的热解，并产生包含合成气的混合物。 本发明采用一种或多种催化剂或吸附剂床来从合成气中除去焦油。 本发明的系统和方法允许在更高的浆料进料速率和较低温度下进行气化，同时提供管理所生产的焦油，从而提高整体气化的转化效率。
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Patent Agency Ranking
26.发明申请公开(公告)号：US20140275676A1
公开(公告)日：2014-09-18
申请号：US14184099
申请日：2014-02-19
Applicant: Lummus Technology Inc.
Inventor： Gary Sieli , Ahmad Faegh , Ujjal K. Mukherjee , Mario C. Baldassari , Marvin I. Greene
CPC classification number: C07C4/06 , C10G9/005 , C10G69/06 , C10G2300/202
Abstract: A process for upgrading residuum hydrocarbon feedstocks that may include: contacting a residuum hydrocarbon and hydrogen with a hydroconversion catalyst in a residuum hydroconversion reactor system; recovering an effluent from the residuum hydroconversion reactor system; separating the effluent to recover two or more hydrocarbon fractions including at least a vacuum residuum fraction and a heavy vacuum gas oil fraction; combining at least a portion of the heavy vacuum gas oil fraction and at least a portion of the vacuum residuum fraction to form a mixed heavy hydrocarbon fraction; feeding at least a portion of the mixed heavy hydrocarbon fraction to a coker; operating the coker at conditions to produce anode grade green coke and distillate hydrocarbons; recovering the distillate hydrocarbons from the coker; fractionating the distillate hydrocarbons to recover hydrocarbon fractions including a light distillates fraction, a heavy coker gas oil fraction, and a coker recycle fraction.
Abstract translation: 一种用于升级残油烃原料的方法，其可以包括：在残渣加氢转化反应器系统中使残油烃和氢与加氢转化催化剂接触; 从渣油加氢转化反应器系统回收污水; 分离出流出物以回收两个或多个烃馏分，包括至少一个真空渣油馏分和一个重质真空瓦斯油馏分; 将至少一部分重质减压瓦斯油馏分和至少一部分真空残渣馏分组合以形成混合的重质烃馏分; 将至少一部分混合的重质烃部分进料至焦化器; 在生产阳极级绿色焦炭和馏出物烃的条件下操作焦化器; 从焦化器回收馏出物烃; 馏分馏分烃以回收烃馏分，包括轻馏分馏分，重焦油瓦斯油馏分和焦化循环馏分。
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公开(公告)号：US08815080B2
公开(公告)日：2014-08-26
申请号：US12359931
申请日：2009-01-26
Applicant: Kandasamy Meenakshi Sundaram
Inventor： Kandasamy Meenakshi Sundaram
CPC classification number: C07C2/78 , B01J19/0026 , C10G2300/1025 , C10G2300/807 , C10G2400/20 , Y02P30/40 , C07C11/24 , C07C11/04
Abstract: Processes for production of olefins from hydrocarbon feedstocks are provided. In one aspect, the processes of the present invention utilize coils passing through a pyrolysis furnace to partially convert a hydrocarbon feedstock to olefins, followed by further conversion of the hydrocarbon feedstock in an adiabatic reactor. A portion of the coils in the pyrolysis furnace carry the hydrocarbon feedstock and the remainder carry steam only. After a selected period of time, the material flowing through the coils is switched. By flowing steam through the coils that had previously contained the hydrocarbon feedstock, on-line decoking can occur. In another aspect, a high temperature reactor is used to convert methane or natural gas to olefins.
Abstract translation: 提供了从烃原料生产烯烃的方法。 在一个方面，本发明的方法利用通过热解炉的线圈将烃原料部分地转化为烯烃，随后在绝热反应器中进一步转化烃原料。 热解炉中的一部分线圈携带烃原料，其余部分仅带有蒸汽。 在选定的时间段之后，流过线圈的材料被切换。 通过使蒸汽流过先前含有烃原料的线圈，可能发生在线除焦。 另一方面，使用高温反应器将甲烷或天然气转化为烯烃。
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公开(公告)号：US20140221709A1
公开(公告)日：2014-08-07
申请号：US13758554
申请日：2013-02-04
Applicant: LUMMUS TECHNOLOGY INC.
Inventor： Mario C. Baldassari , Ujjal K. Mukherjee , Ann-Marie Olsen , Marvin I. Greene
IPC: C10G65/12
Abstract: A process for upgrading residuum hydrocarbons is disclosed. The process may include: contacting a residuum hydrocarbon fraction and hydrogen with a first hydroconversion catalyst in a first ebullated bed hydroconversion reactor system; recovering a first effluent from the first ebullated bed hydroconversion reactor system; solvent deasphalting a vacuum residuum fraction to produce a deasphalted oil fraction and an asphalt fraction; contacting the deasphalted oil fraction and hydrogen with a second hydroconversion catalyst in a second hydroconversion reactor system; recovering a second effluent from the second hydroconversion reactor system; and fractionating the first effluent from the first ebullated bed hydroconversion reactor system and the second effluent from the second hydroconversion reactor system to recover one or more hydrocarbon fractions and the vacuum residuum fraction in a common fractionation system.
Abstract translation: 公开了一种用于升级残油烃的方法。 该方法可以包括：在第一沸腾床加氢转化反应器系统中使残油烃馏分和氢与第一加氢转化催化剂接触; 从第一沸腾床加氢转化反应器系统回收第一流出物; 溶剂脱沥青真空残渣馏分以产生脱沥青油馏分和沥青馏分; 在第二加氢转化反应器系统中使脱沥青油馏分和氢气与第二加氢转化催化剂接触; 从第二加氢转化反应器系统回收第二流出物; 并将来自第一沸腾床加氢转化反应器系统的第一流出物和来自第二加氢转化反应器系统的第二流出物分馏，以在普通分馏系统中回收一种或多种烃馏分和真空残渣馏分。
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公开(公告)号：US20140114101A1
公开(公告)日：2014-04-24
申请号：US14052972
申请日：2013-10-14
Applicant: Lummus Technology Inc.
Inventor： Marvin I. Greene , Ruozhi Song , Arvids Judzis, JR.
CPC classification number: C07C1/24 , C07C2/06 , C07C5/13 , C10G3/42 , C10G3/49 , C10G45/58 , C10G50/00 , C10G69/126 , C10L1/08 , Y02P30/20
Abstract: A process for the production of jet and other heavy fuels from alcohols and mixture of alcohols is disclosed. The process may include contacting in a reaction zone at least one C2 to C11 alcohol with a solid catalyst having activity for the simultaneous dehydration of the alcohols to form olefins, isomerization of the olefins to form internal olefins, and oligomerization of the olefins produced in situ via the dehydration reaction to form an effluent comprising mono-olefinic hydrocarbons. Preferably, the alcohol feed is a mixture of alcohols, such as C2 to C7 alcohols or C4 and C6 alcohols, enabling the production of a mixture of branched hydrocarbons that may be used directly as a jet fuel without blending.
Abstract translation: 公开了一种从醇和醇的混合物生产射流和其它重质燃料的方法。 该方法可以包括在反应区中使至少一种C 2至C 11醇与固体催化剂接触，所述固体催化剂具有用于同时脱水醇形成烯烃的活性，烯烃异构化以形成内烯烃，以及原位生产的烯烃的低聚 通过脱水反应形成包含单烯烃的流出物。 优选地，醇进料是醇，例如C 2至C 7醇或C 4和C 6醇的混合物，使得能够生产可直接用作喷气燃料而不混合的支链烃混合物。
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公开(公告)号：US08685151B2
公开(公告)日：2014-04-01
申请号：US13958815
申请日：2013-08-05
Applicant: Lummus Technology Inc.
Inventor： Ronald E. Brown , Daniel T. Fernald
IPC: B01D53/02
CPC classification number: B01D53/12 , B01D2253/1124 , B01D2256/16 , B01D2256/24 , B01D2257/30 , B01D2257/80
Abstract: The present disclosure relates generally to contaminant removal from gas streams. In certain embodiments, the present disclosure relates to a process for removing one or more contaminants from a gas stream via contact with a regenerable sorbent at high temperature and pressure, utilizing a unique arrangement of reactors operating in parallel.
Abstract translation: 本公开一般涉及从气流中去除污染物。 在某些实施方案中，本公开内容涉及通过使用并行操作的反应器的独特布置，在高温和高压下通过与可再生吸附剂接触从气流中除去一种或多种污染物的方法。
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