-
1.发明授权Process for regenerating or activating a n-paraffin isomerization mordenite-containing catalyst 失效用于再生或活化含有正构烷烃的异构化丝光沸石催化剂的方法
公开(公告)号：US4835129A
公开(公告)日：1989-05-30
申请号：US164945
申请日：1988-03-07
IPC分类号： B01J38/44 , B01J29/90 , B01J38/18 , B01J38/42 , C07C1/00 , C07C5/27 , C07C67/00 , C10G35/095 , C10G45/64
CPC分类号： C10G45/64 , B01J29/90 , B01J38/18 , C07C5/2791 , B01J38/42 , Y02P20/584
摘要： Process for regenerating or activating a catalyst for isomerizing n-paraffins, containing at least one group VIII metal supported on an acid mordenite, wherein, after having lost at least a part of its initial activity, said catalyst is treated in a first step with an oxygen-containing gas at a temperature lower than about 550.degree. C., so as to remove the major part of the catalyst coke content, and in a second step the resultant product from the first step is oxychlorinated to a temperature of about 200.degree.-500.degree. C. by means of a gas mixture containing oxygen, water and chlorine or at least one chlorinated compound, said chlorine or chlorinated compound being used in a total amount of 0.5-10% by weight, calculated as chlorine, in proportion to the mordenite weight.
摘要翻译： 用于再生或活化用于使正链烷烃异构化的催化剂的方法，所述催化剂含有负载在酸性丝光沸石上的至少一种VIII族金属，其中在损失了其初始活性的至少一部分之后，所述催化剂在第一步中用 在低于约550℃的温度下进行含氧气体，以除去催化剂焦炭含量的主要部分，在第二步中将得自第一步的产物氧氯化至约200℃ - 500℃，通过含有氧，水和氯的气体混合物或至少一种氯化化合物，所述氯或氯化合物的用量按氯计算为0.5-10重量％，按氯计 丝光沸石重量。
-
2.发明授权Catalyst of high mordenite content for isomerizing normal paraffins and process for producing the catalyst 失效用于使正构链烷烃异构化的高丝光沸石含量的催化剂和用于制备催化剂的方法
公开(公告)号：US4789655A
公开(公告)日：1988-12-06
申请号：US84944
申请日：1987-08-13
IPC分类号： B01J29/20 , B01J29/22 , B01J37/24 , C07C1/00 , C07C5/27 , C07C9/16 , C07C67/00 , C10G35/095 , C10G45/64 , B01J29/24
摘要： A catalyst for isomerizing a hydrocarbon cut of high n-paraffin content is disclosed. The catalyst is obtained by controlled oxychlorination of a solid containing at least one group VIII metal supported on an acid mordenite, said mordenite having a sodium content lower than 0.2% by weight, adsorbing molecules of a kinetic diameter larger than about 6.6 Angstroms, having a mesh volume, V, of the elementary mesh from 2.73 to 2.78 nm.sup.3 and a benzene adsorption capacity higher than 5% by weight, said oxychlorination being conducted at a temperature of about 200.degree.-500.degree. C. by means of a gas mixture containing oxygen, water, chlorine or at least one chlorinated compound used in a total amount from 0.5 to 10% by weight of chlorine, in proportion to the mordenite weight. The catalyst may further contain a matrix, the mordenite amount being at least 40% by weight of the total amount of mordenite and matrix.
摘要翻译： 公开了一种用于异构化高正链烷烃含量的烃馏分的催化剂。 催化剂是通过控制氧氯化含有负载在酸性丝光沸石上的至少一种VIII族金属的固体获得的，所述丝光沸石具有低于0.2重量％的钠含量，吸附动力学直径大于约6.6埃的分子，具有 所述基本网眼的网孔体积V为2.73〜2.78nm 3，苯吸附容量高于5重量％，所述氧氯化在约200-500℃的温度下通过含氧气体混合物进行 ，水，氯或至少一种氯化合物，其总量为0.5至10重量％的氯，与丝光沸石重量成比例。 催化剂还可以含有基质，丝光沸石量为丝光沸石和基体总量的至少40重量％。
-
公开(公告)号：US4722780A
公开(公告)日：1988-02-02
申请号：US38561
申请日：1987-04-15
IPC分类号： B01J23/00 , B01J23/64 , B01J23/656 , B01J27/00 , B01J27/13 , C10G35/085 , C10G35/09 , C10G59/02 , C10G35/06
CPC分类号： B01J23/6567 , C10G35/09 , C10G59/02
摘要： A catalytic reforming process using catalysts containing a carrier, platinum, rhenium and optionally at least one metal selected from the group consisting of tin, germanium, lead, indium, thallium and titanium, arranged in several successive catalyst beds wherein the catalyst of the first bed has a Re/Pt ratio higher than the Re/Pt ratio of the catalyst used in the last bed, said catalyst of the last bed containing at least 0.08% of rhenium in proportion to the carrier.The catalysts preferably contain at least one halogen in an amount, expressed in proportion to the carrier, from 0.1 to 15%, said carrier preferably consisting mainly of alumina.In a preferred embodiment 3 successive catalyst beds are used wherein the Re/Pt ratios are, as a whole, decreasing from the first bed to the last bed.
摘要翻译： 一种使用催化剂的催化重整方法，其中催化剂含有载体，铂，铼和任选的至少一种选自锡，锗，铅，铟，铊和钛的金属，其布置在几个连续的催化剂床中，其中第一床的催化剂 Re / Pt比高于最后一个床中使用的催化剂的Re / Pt比，最后一个床的催化剂含有与载体成比例的至少0.08％的铼。 催化剂优选含有至少一种与载体成比例地表示的卤素，为0.1至15％，所述载体优选主要由氧化铝组成。 在优选的实施方案中，使用连续的催化剂床，其中Re / Pt比率总体上从第一床到最后一床减小。
-
4.发明授权Process for the catalytic reforming of a charge passing through at least two catalyst beds 失效用于催化重整通过至少两个催化剂床的电荷的方法
公开(公告)号：US4737262A
公开(公告)日：1988-04-12
申请号：US10596
申请日：1987-02-03
IPC分类号： B01J27/00 , B01J27/13 , B01J31/00 , B01J31/12 , B01J31/22 , C10G35/04 , C10G35/085 , C10G35/09 , C10G50/00 , C10G59/02
摘要： A process for the catalytic reforming of a hydrocarbon charge wherein the charge passes successively through at least two catalyst beds, the first one being a bed of a first catalyst whose carrier contains platinum, rhenium and at least one halogen, at least the last bed being a moving bed of a second catalyst whose carrier contains platinum, at least one additional metal M selected from the group consisting of tin, gallium, germanium, indium, lead and thallium and at least one halogen, said metal M being introduced onto this carrier by means of an organometallic compound and the proportion by weight of said second catalyst being from 25 to 55% of the total catalyst mass used in all the catalyst beds. The charge preferably passes through at least two fixed beds of the first catalyst and at least one moving bed of the second catalyst, the carrier of the two catalysts being preferably alumina.By this process high grade gasolines (of Research Octane Number higher than 95) are produced over long periods.
摘要翻译： 一种用于烃电荷的催化重整的方法，其中电荷依次通过至少两个催化剂床，第一个是载体包含铂，铼和至少一个卤素的第一催化剂的床，至少最后一个床是 载体包含铂的第二催化剂的移动床，选自锡，镓，锗，铟，铅和铊的至少一种另外的金属M和至少一种卤素，所述金属M通过 有机金属化合物的手段和所述第二催化剂的重量比例在所有催化剂床中使用的总催化剂质量的25-55％。 电荷优选通过第一催化剂的至少两个固定床和第二催化剂的至少一个移动床，两种催化剂的载体优选为氧化铝。 通过这种方法，高品质汽油（研究辛烷值高于95）长期生产。
-
公开(公告)号：US4588495A
公开(公告)日：1986-05-13
申请号：US704456
申请日：1985-02-22
CPC分类号： C10G59/02
摘要： In a catalytic reforming process wherein a charge is circulated successively through a first catalyst bed and then at least one further catalyst bed, the improvement wherein the catalyst of the first bed comprises a carrier of alumina base and, by weight in proportion to the carrier, 0.05-0.6% of platinum, 0.005-3% of rhenium and 0.1-15% of at least one halogen and wherein each catalyst of the other beds contains a carrier of alumina base and, by weight with respect to the carrier, 0.05-0.6% of platinum, 0.05-3% of at least one metal promoter selected from the group consisting of tin, thallium and indium and 0.1-15% of at least one halogen, the proportion by weight of the catalyst containing platinum and rhenium ranging from 8 to 40% with respect to the total catalyst mass used in all the catalyst beds.
摘要翻译： 在催化重整过程中，其中电荷依次通过第一催化剂床和至少一个另外的催化剂床循环，其中第一床的催化剂包含氧化铝碱的载体，并且按载体的重量比例， 0.05-0.6％的铂，0.005-3％的铼和0.1-15％的至少一种卤素，其中每个催化剂的其它床层含有氧化铝基质的载体，相对于载体的重量比为0.05-0.6 铂的含量为0.05-3％，选自锡，铊和铟的至少一种金属促进剂和0.1-15％的至少一种卤素，含有铂和铼的催化剂的重量比为8 相对于在所有催化剂床中使用的总催化剂质量至40％。
-
公开(公告)号：US4909924A
公开(公告)日：1990-03-20
申请号：US84726
申请日：1987-08-13
申请人： Francis Raatz , Laurent Petit , Christian Marcilly , Jean-Paul Bournonville , Christine Travers , Pierre Dufresne
发明人： Francis Raatz , Laurent Petit , Christian Marcilly , Jean-Paul Bournonville , Christine Travers , Pierre Dufresne
CPC分类号： C10G11/05 , B01J29/60 , C10G47/16 , B01J2229/16 , B01J2229/26 , B01J2229/42
摘要： The present invention concerns a new decationized, dealuminated and stabilized zeolite of L type, characterized particularly by:a total SiO.sub.2 /Al.sub.2 O.sub.3 molar ratio of at least 8,a potassium content lower than 2.9% by weight,parameters a and c of the elementary mesh respectively lower than 1.836 nm and 0.754 nm,a nitrogen adsorption capacity at 77 K, for a partial pressure P/Ps of 0.19, higher than 11% by weight,a benzene adsorption capacity at 30.degree. C., for a partial pressure P/Ps of 0.25, higher than 8.5% by weight, anda lattice of mesopores whose radii, measured by nitrogen adsorption-desorption at 77 K according to the BJH method, range from 0.8 nm to 20 nm.
摘要翻译： 本发明涉及一种新型的分解，脱铝和稳定的L型沸石，其特征在于特征在于：总SiO 2 / Al 2 O 3摩尔比至少为8，钾含量低于2.9重量％，基本网格的参数a和c 分别低于1.836nm和0.754nm，对于分压P / Ps为0.19，高于11重量％，在30℃下的苯吸附容量为77K时的氮吸附容量，对于分压P / Ps为0.25，高于8.5重量％，并且根据BJH方法在77K下通过氮吸附 - 解吸测定的半径为0.8nm〜20nm的中孔的晶格。
-
7.发明授权
公开(公告)号：US4514515A
公开(公告)日：1985-04-30
申请号：US597288
申请日：1984-04-06
IPC分类号： C07C29/136 , B01J23/00 , B01J23/62 , B01J31/00 , C07B61/00 , C07C27/00 , C07C29/149 , C07C67/00 , B01J21/04 , B01J21/08
CPC分类号： C07C29/149 , B01J23/622 , Y02P20/52
摘要： A catalyst comprising a carrier, rhodium and at least one element selected from the group consisting of tin, germanium and lead is prepared from a rhodium compound and an alkyl, cycloalkyl or aryl tin, germanium or lead compound.
摘要翻译： 由铑化合物和烷基，环烷基或芳基锡，锗或铅化合物制备包含载体，铑和至少一种选自锡，锗和铅的元素的催化剂。
-
8.发明授权
公开(公告)号：US4456775A
公开(公告)日：1984-06-26
申请号：US497631
申请日：1983-05-24
IPC分类号： C07C29/136 , B01J23/00 , B01J23/62 , B01J31/00 , C07B61/00 , C07C27/00 , C07C29/149 , C07C67/00
CPC分类号： C07C29/149 , B01J23/622 , Y02P20/52
摘要： Alcohols and particularly fatty alcohols are manufactured by hydrogenolysis of carboxylic esters in the presence of a catalyst comprising a carrier, rhodium and at least one second element selected from the group consisting of tin, germanium and lead. The rhodium content is from 0.1 to 5% b.w. and the content of the second element is from 0.1 to 10% b.w.
摘要翻译： 醇，特别是脂肪醇通过在包含载体，铑和至少一种选自锡，锗和铅的第二元素的催化剂存在下羧酸酯的氢解来制备。 铑含量为0.1〜5％b.w。 并且第二元素的含量为0.1至10％b.w。
-
9.发明授权Process for manufacturing supported bimetallic or plurimetallic catalysts comprising one or more metals from group VIII and at least one metal from group IV and the resultant catalysts thereof 失效制备支持的双金属或多金属催化剂的方法，其包含一种或多种来自VIII族的金属和至少一种IV族金属及其所得催化剂
公开(公告)号：US4504593A
公开(公告)日：1985-03-12
申请号：US573279
申请日：1984-01-24
IPC分类号： C10G49/06 , B01J23/14 , B01J23/62 , B01J23/64 , B01J23/652 , B01J23/835 , B01J23/88 , B01J31/28 , C07B31/00 , C07B61/00 , C07C1/00 , C07C5/05 , C07C5/09 , C07C7/163 , C07C11/00 , C07C11/10 , C07C67/00 , C10G45/40 , C10G45/48 , C10G45/52 , B01J31/12 , B01J31/34
CPC分类号： B01J23/835 , B01J23/622 , C10G45/40
摘要： For the selective hydrogenation of a hydrocarbon charge containing at least one acetylenic and/or diolefinic hydrocarbon, there is used a catalyst comprising at least one group VIII metal selected from the platinum, palladium, nickel and cobalt group, or a compound thereof, and at least one metal from the group comprising germanium, tin and lead or a compound thereof, wherein at least one compound from one of the above-defined group VIII metals and at least one compound of metal from the germanium, tin and lead group is incorporated in a carrier, e.g., alumina, and wherein the compound of metal from the germanium, tin and lead group is incorporated in the carrier as a hydrocarbyl compound of said metal.
摘要翻译： 对于含有至少一个炔属和/或二烯烃的烃装料的选择性氢化，使用包含至少一种选自铂，钯，镍和钴基团的Ⅷ族金属或其化合物的催化剂， 包含锗，锡和铅或其化合物的至少一种金属，其中至少一种来自上述定义的VIII族金属的化合物和至少一种来自锗，锡和铅基团的金属化合物掺入 载体，例如氧化铝，其中来自锗，锡和铅基团的金属化合物作为所述金属的烃基化合物引入载体中。
-
10.发明授权
公开(公告)号：US4973401A
公开(公告)日：1990-11-27
申请号：US382886
申请日：1989-07-21
CPC分类号： C10G35/12 , B01J8/087 , B01J2208/0007 , B01J2208/00221 , B01J2208/00504 , B01J2208/0053
摘要： The present invention relates to a process and a reactor for low pressure catalytic reforming of gasolines with heating by smoke gases.The reactor of the invention comprises:at least one means for introducing and removing the charge,at least one means for introducing and removing the catalyst,at least two elementary reaction cells not adjacent each other, substantially vertical and parallelepipedic, substantially parallel to each other, each of said cells being formed of three substantially parallelepipedic enclosures (an individual charge distributor, an individual processed charge collector, a catalytic bed),at least one general charge distributor,at least one general processed charge collector.The reforming process of the invention may be used in this reactor, smokes-based heating gases, coming from the combustion in air of a hydrocarbon mixture, flowing between the elementary reaction cells and thus bringing the heat required for the reforming reaction.
摘要翻译： 本发明涉及一种通过烟雾气体加热汽油进行低压催化重整的方法和反应器。 本发明的反应器包括：用于引入和除去电荷的至少一种装置，至少一种用于引入和除去催化剂的装置，至少两个彼此不相邻的基本上垂直和平行六面体的基本反应元件，基本上彼此平行 每个所述电池由三个基本上平行六面体的外壳（单个电荷分布器，单独的处理电荷收集器，催化床），至少一个通用电荷分配器，至少一个通用处理的电荷收集器形成。 本发明的重整方法可用于该反应器中，来自烃类混合物的空气中的燃烧的基于烟雾的加热气体，其在元素反应池之间流动，从而产生重整反应所需的热量。
-
-
-
-
-
-
-
-
-
搜索结果
26 条记录 (耗时 0.02 秒)
