公开(公告)号：US11958046B1

公开(公告)日：2024-04-16

申请号：US18336936

申请日：2023-06-16

申请人： KELLOGG BROWN & ROOT LLC

发明人： Rajeev Ranjan ,  Anubhav Kapil

IPC分类号： B01J8/04 ,  C07C2/54 ,  C07C2/56 ,  C07C2/58 ,  C07C2/76

CPC分类号： B01J8/0492 ,  B01J8/0446 ,  C07C2/76 ,  B01J2208/00752 ,  B01J2208/00761 ,  C07C2/54 ,  C07C2/56 ,  C07C2/58

摘要： Methods and systems for alkylate production involving a multi-zone alkylation reactor. The multi-zone alkylation reactor includes a plurality of alkylation zones spaced vertically in a series configuration and a partition splitting the plurality of alkylation zones into at least two mechanically separated catalytic volumes.

公开(公告)号：US11261139B2

公开(公告)日：2022-03-01

申请号：US16590328

申请日：2019-10-01

申请人： Exelus Inc.

发明人： Mitrajit Mukherjee ,  Eric Daniel Gauthier ,  Kelly Ann Coley

IPC分类号： C07C2/58 ,  B01J29/08 ,  B01J29/70 ,  B01J37/30 ,  B01J37/02 ,  C01B39/20 ,  C01B39/02 ,  C01B39/46 ,  C10G29/20 ,  B01J29/90 ,  B01J29/12 ,  B01J38/10 ,  B01J29/74 ,  C07C2/56 ,  C07C2/54 ,  C07C9/14 ,  C07C9/16 ,  B01J29/14 ,  B01J37/08 ,  C10G99/00

摘要： Improved alkylation catalysts, alkylation methods, and methods of making alkylation catalysts are described. The alkylation method comprises reaction over a solid acid, zeolite-based catalyst and can be conducted for relatively long periods at steady state conditions. The alkylation catalyst comprises a crystalline zeolite structure, a Si/Al molar ratio of 20 or less, less than 0.5 weight percent alkali metals, and further having a characteristic catalyst life property. Some catalysts may contain rare earth elements in the range of 10 to 35 wt %. One method of making a catalyst includes a calcination step following exchange of the rare earth element(s) conducted at a temperature of at least 575° C. to stabilize the resulting structure followed by an deammoniation treatment. An improved method of deammoniation uses low temperature oxidation.

公开(公告)号：US11203726B1

公开(公告)日：2021-12-21

申请号：US16835639

申请日：2020-03-31

申请人： The United States of America, as represented by the Secretary of the Navy

发明人： Benjamin G. Harvey ,  Matthew C. Davis

IPC分类号： C10L1/04 ,  C07C13/615 ,  C07C7/14 ,  C10L1/00 ,  C07C7/11 ,  C07C2/86 ,  C07C7/04 ,  C07C2/56 ,  C08L45/00 ,  C07C22/00 ,  C06B43/00 ,  C10L10/12

摘要： A diamondoid fuel comprising a cage structure including 10, 14, 18, or 22 carbons. The diamondoid fuel also includes one of one to four cyclopropyl groups bonded to the cage structure or two to four functional groups bonded to the cage structure where the functional groups are an alkyl group, an allyl group, a cyclopropyl group, or combinations thereof. Additionally, at least one functional group is an allyl group and at least one functional group is a cyclopropyl group.

公开(公告)号：US10995045B2

公开(公告)日：2021-05-04

申请号：US16154985

申请日：2018-10-09

申请人： UOP LLC

发明人： Christopher DiGiulio ,  Charles P. Luebke ,  David J. Shecterle

IPC分类号： C07C5/327 ,  C07C2/56 ,  C07C5/27

摘要： An alkylation process including an upfront isomerization zone is described. 100% n-butane or field butanes can be converted into a blend of approximately 60 wt % isobutane and 40 wt % n-butane in the isomerization zone. This blend can be used as the feed to all types of alkylation zones. It stabilizes the feed composition so that the dehydrogenation zone and alkylation zone always operate with the same feed.

公开(公告)号：US10710941B1

公开(公告)日：2020-07-14

申请号：US16178273

申请日：2018-11-01

申请人： The United States of America, as Represented by the Secretary of the Navy

发明人： Benjamin G. Harvey ,  Matthew C. Davis

IPC分类号： C07C13/615 ,  C07C22/00 ,  C07C2/56 ,  C07C2/86 ,  C08L45/00 ,  C07C7/11 ,  C07C7/04 ,  C07C7/14

摘要： A diamondoid fuel comprising a cage structure including 10, 14, 18, or 22 carbons. The diamondoid fuel also includes one of one to four cyclopropyl groups bonded to the cage structure or two to four functional groups bonded to the cage structure where the functional groups are an alkyl group, an allyl group, a cyclopropyl group, or combinations thereof. Additionally, at least one functional group is an allyl group and at least one functional group is a cyclopropyl group.

公开(公告)号：US10584079B2

公开(公告)日：2020-03-10

申请号：US15877988

申请日：2018-01-23

申请人： UOP LLC

发明人： Eric Leeton

IPC分类号： C07C2/58 ,  C07C2/56 ,  C07C2/60 ,  B01J31/02 ,  C10G29/20 ,  C10L1/06 ,  B01J35/12

摘要： An alkylation process and apparatus are described. The alkylation process includes pre-mixing a paraffin stream with an ionic liquid catalyst stream from a settler. The premixed paraffin and ionic liquid catalyst stream is mixed in a low-efficiency pump to form a paraffin and ionic liquid catalyst mixture. An olefin feed stream is introduced into a riser reactor. The paraffin and ionic liquid catalyst mixture is introduced into the riser reactor to form a reaction mixture comprising alkylate and the ionic liquid catalyst. The reaction mixture is separated in a settler into an ionic liquid catalyst stream and a hydrocarbon stream.

公开(公告)号：US10370311B2

公开(公告)日：2019-08-06

申请号：US15165882

申请日：2016-05-26

申请人： Evonik Degussa GmbH

发明人： Stephan Peitz ,  Guido Stochniol ,  Dietrich Maschmeyer ,  Helene Reeker ,  Reiner Bukohl

IPC分类号： C07C7/12 ,  C07C7/00 ,  B01D15/00 ,  B01J20/06 ,  B01J20/08 ,  C10G25/00 ,  C07C2/06 ,  C07C2/56 ,  C07C5/327 ,  C07C7/04 ,  C07C7/10 ,  C07C7/163 ,  C07C7/167 ,  C07C41/09 ,  C07D307/60 ,  C10G45/04 ,  C10G45/22 ,  C07C2/58 ,  C07C5/48

摘要： The invention relates to a process for purifying hydrocarbon mixtures, in which a contaminated hydrocarbon mixture comprising olefins having three to eight carbon atoms is at least partly freed of sulphur-containing contaminants by contacting it with a solid sorbent, the hydrocarbon mixture being exclusively in the liquid state during the contact with the sorbent. The problem that it addressed was that of virtually completely removing sulphur compounds present in the mixture without forming new sulphur compounds again at the same time. At the same time, 1-butene present therein was not to be lost in the purification of the mixture. Finally, the sorbent used was to have a high sorption capacity, be very substantially free of carcinogenic constituents and be readily available. This problem is solved by using a sorbent based on copper oxide, zinc oxide and aluminium oxide in a particular composition, and by conducting the purification in the presence of a small amount of hydrogen.

公开(公告)号：US09856185B2

公开(公告)日：2018-01-02

申请号：US14515196

申请日：2014-10-15

申请人： LytOil, Inc.

发明人： Joe Griffith Cruz ,  Scott Ray Mobley ,  Philip David Fulmer

IPC分类号： C07C5/03 ,  C07C2/56 ,  B01J19/08 ,  B01J19/12 ,  B01J19/24 ,  B01J10/00

CPC分类号： C07C5/03 ,  B01J10/00 ,  B01J19/087 ,  B01J19/088 ,  B01J19/129 ,  B01J19/24 ,  B01J19/245 ,  B01J2219/0004 ,  B01J2219/00065 ,  B01J2219/00067 ,  B01J2219/00094 ,  B01J2219/00132 ,  B01J2219/00135 ,  B01J2219/00159 ,  B01J2219/00173 ,  B01J2219/0875 ,  B01J2219/0894 ,  B01J2219/0898 ,  B01J2219/1203 ,  C07C2/56

摘要： Methods and apparatus for refining feedstocks, such as crude or synthetic oil, and like feedstocks, are disclosed herein. In some embodiments, a reactor for refining a feedstock includes: a chamber having an inner volume to hold a liquid feedstock, a feedstock inlet port, a process gas inlet port, and an outlet port; a gas diffuser housed within the chamber and coupled to the process gas inlet port; and a radical generator coupled in fluid communication with the inner volume via the gas diffuser. In some embodiments, a method for refining feedstock includes: providing liquid feedstock to an inner volume of a reactor; flowing a radicalized process gas from a radical generator into the inner volume and into contact with the feedstock via a gas diffuser to fractionate the feedstock and produce one or more fractions of product in a vaporous mixture; and collecting a desired product from the vaporous mixture.

公开(公告)号：US20160368848A1

公开(公告)日：2016-12-22

申请号：US15173042

申请日：2016-06-03

申请人： Lyondell Chemical Technology, L.P.

发明人： Michael G. Axelrod ,  Steven T. Coleman

IPC分类号： C07C41/06 ,  C07C4/02 ,  C07C2/56 ,  C07C5/25 ,  C07C29/50 ,  C07C5/327 ,  C07C2/36

CPC分类号： C07C41/06 ,  C07C2/22 ,  C07C4/04 ,  C07C5/2775 ,  C07C29/1518 ,  C07C2529/65 ,  C07C2531/14 ,  C07C2531/24 ,  C10L1/06 ,  Y02P20/52 ,  C07C11/08 ,  C07C11/09 ,  C07C43/046 ,  C07C11/04 ,  C07C31/04 ,  C07C43/04

摘要： A process for manufacturing methyl t-butyl ether (MTBE) including (A) an optional first step including cracking raw material made from or containing ethane and/or propane, to form ethylene and recovering the residual uncracked raw material, (B) a second step including dimerizing ethylene to form n-butylene, (C) a third step including isomerizing the n-butylene to form isobutylene, (D) an optional fourth step including oxidizing methane to form methanol, (E) a fifth step including etherifying the isobutylene with methanol to form methyl t-butyl ether, and (F) a sixth step including collecting the methyl t-butyl ether is provided. The process can also be used to prepare gasoline alkylate, a higher molecular weight ethylene oligomer, a higher-molecular-weight-ethylene-oligomer-based methyl ether, an isomerized higher molecular weight ethylene oligomer, or an isomerized-higher-molecular-weight-ethylene-oligomer-based methyl ether.

摘要翻译： 一种制备甲基叔丁基醚（MTBE）的方法，包括（A）任选的第一步骤，包括由乙烷和/或丙烷制备或包含乙烯和/或丙烷制成的裂化原料，以形成乙烯并回收残留未裂化的原料，（B）第二步 （C）第三步骤，包括使正丁烯异构化形成异丁烯;（D）任选的第四步骤，包括使甲烷氧化形成甲醇;（E）第五步，包括醚化异丁烯 与甲醇形成甲基叔丁基醚，（F）第六步，包括收集甲基叔丁基醚。 该方法也可用于制备烷基化汽油，较高分子量乙烯低聚物，较高分子量 - 乙烯 - 低聚物基甲基醚，异构化较高分子量乙烯低聚物或异构化 - 高分子量 - 乙烯 - 低聚物基甲基醚。

公开(公告)号：US07692054B2

公开(公告)日：2010-04-06

申请号：US11872786

申请日：2007-10-16

申请人： Mark G. Riley

发明人： Mark G. Riley

IPC分类号： C07C2/56

CPC分类号： C07C2/66 ,  C07C15/107

摘要： Continuous processes for monoalkylating aromatic compound with an aliphatic feedstock comprising aliphatic olefin of 8 to 18 carbon atoms per molecule are effected using at least 3 reaction zones in series, each containing solid alkylation catalyst with effluent cooling between reaction zones, each of which reaction zones is supplied a portion of the fresh aliphatic feedstock, such that the Reaction Zone Delta T in each reaction zone is less than about 15° C. The overall aromatic compound to olefin molar ratio is less than about 20:1. The alkylation product has desirable linearity and low amounts of dimers, dealkylated compounds and diaryl compounds even though a low aromatic compound to olefin molar ratio is used.

摘要翻译： 使烷基化芳族化合物与包含每个分子具有8至18个碳原子的脂族烯烃的单烷基化的连续方法使用至少3个串联的反应区进行，每个反应区均含有固体烷基化催化剂，反应区之间的流出物冷却，每个反应区为 提供一部分新鲜的脂肪原料，使得每个反应区中的反应区Delta T小于约15℃。芳族化合物与烯烃的总摩尔比小于约20:1。 尽管使用低芳族化合物与烯烃的摩尔比，烷基化产物具有所需的线性和低二聚体，脱烷基化合物和二芳基化合物的量。