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公开(公告)号：US20240317657A1
公开(公告)日：2024-09-26
申请号：US18614527
申请日：2024-03-22
发明人： Shikha SALUJA , Gadari SAIDULU , Madhusudan SAU , Sadhullah MUKTHIYAR , Terapalli Hari Venkata Devi PRASAD , Reshmi MANNA
CPC分类号： C07C5/3332 , B01J8/384 , B01J21/12 , B01J21/20 , B01J38/38 , C07C11/04 , C07C2521/12
摘要： The present disclosure provides a process for high conversion residue cracking in a circulating fluidized bed reactor while integrating it with the dehydration of ethanol. More particularly, the present disclosure relates to an integrated circulating fluidized bed process for the simultaneous dehydration of ethanol and cracking of a hydrocarbon feedstock. By integrating the cracking reactor with ethanol dehydration reactor, more conradson carbon residue feedstock can be processed in cracking reactor while limiting the coke combustor temperature.
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2.发明申请公开(公告)号：US20130072376A1
公开(公告)日：2013-03-21
申请号：US13636406
申请日：2011-02-18
IPC分类号： B01J38/38
CPC分类号： B01J38/38 , B01J8/125 , B01J38/00 , B01J38/02 , B01J38/12 , B01J38/14 , B01J38/20 , B01J38/24 , B01J38/32 , B01J38/34 , B01J38/44 , B01J2208/00371 , B01J2208/00504 , C10G11/00 , C10G11/187 , C10G35/00 , C10G45/00 , C10G45/58 , C10G2300/70 , C10G2300/708 , Y10S502/514 , Y10S502/515 , Y10S502/518
摘要： The present invention describes a combustion zone for a regenerative catalytic unit for the continuous regeneration of catalyst, said combustion zone having an annular shape and being divided into at least two combustion stages, each stage being divided into a number N of radial sectors, which are substantially equal, the catalyst flowing under gravity from one sector of the first combustion stage to the sector located in vertical alignment with the second combustion stage by means of drop legs, and the movement of the combustion gas being such that the combustion gas passes in succession through all of the sectors of the first combustion stage in any order, then all of the sectors of the second stage in any order.
摘要翻译： 本发明描述了一种用于催化剂连续再生的再生催化装置的燃烧区，所述燃烧区具有环形形状并被分成至少两个燃烧级，每一级分为N个径向扇区， 基本上相同的是，催化剂在重力作用下从第一燃烧级的一个部分流到位于与第二燃烧级垂直对准的部分，并且燃烧气体的运动使得燃烧气体连续通过 通过所有阶段的第一燃烧阶段的任何顺序，然后第二阶段的所有部门按任何顺序。
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3.发明申请公开(公告)号：US20180222814A1
公开(公告)日：2018-08-09
申请号：US15936754
申请日：2018-03-27
发明人： Zhongmin Liu , Zhihui Lv , Changqing He , Yu Liu , Yue Qi , Xiaojian Min , Gongwei Wang , Xiangao Wang , Jinling Zhang , Mao Ye
CPC分类号： C07C1/24 , B01J8/1872 , B01J8/26 , B01J29/061 , B01J38/38 , B01J2208/00716 , B01J2229/126 , C07C1/20 , C07C11/04 , C07C11/06 , C07C2529/06 , C07C2529/85 , Y02P20/52 , Y02P30/42
摘要： Disclosed is a method for starting up fluidized reaction apparatus that is used for producing lower olefins from methanol or/and dimethyl ether. Said method includes after heating the catalyst bed of circulating fluidized catalytic reaction apparatus to above 200° C. or 300° C. by using a starting-up auxiliary heat source, feeding methanol or dimethyl ether raw materials to a reactor, whereby heat released by the reaction makes the temperature of the reaction system apparatus increase quickly to a designed temperature, consequently making the system reach normal operation state rapidly. Said method is suitable for starting up an exothermic fluidized catalytic reaction apparatus and can simplify the apparatus and operation, accordingly lowering the cost.
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公开(公告)号：US09884314B2
公开(公告)日：2018-02-06
申请号：US14420677
申请日：2013-07-31
发明人： Lin Luo , Brien A. Stears
IPC分类号： B01J21/04 , B01J21/08 , B01J21/12 , B01J23/54 , B01J23/56 , B01J23/58 , B01J23/62 , B01J23/63 , B01J23/64 , B01J23/76 , B01J23/78 , B01J23/825 , B01J23/83 , B01J23/84 , B01J23/86 , B01J23/89 , B01J38/02 , B01J38/12 , B01J38/18 , B01J38/38 , B01J23/96 , B01J23/648 , B01J23/652 , C07C5/333
CPC分类号： B01J23/96 , B01J23/648 , B01J23/6482 , B01J23/652 , B01J23/6522 , B01J23/8906 , B01J23/8993 , B01J38/02 , B01J38/12 , B01J38/18 , B01J38/38 , C07C5/3337 , C07C2521/04 , C07C2521/08 , C07C2521/12 , C07C2523/02 , C07C2523/04 , C07C2523/08 , C07C2523/10 , C07C2523/22 , C07C2523/26 , C07C2523/42 , C07C2523/44 , C07C2523/46 , C07C2523/652 , C07C2523/745 , C07C2523/89 , Y02P20/52 , Y02P20/584 , C07C11/04 , C07C11/06 , C07C11/08
摘要： A catalyst comprising a Group IIIA metal, a Group VIII noble metal, and an optional promoter metal, on a support selected from silica, alumina, silica-alumina compositions, rare earth modified alumina, and combinations thereof, doped with iron, a Group VIB metal, a Group VB metal, or a combination thereof, offers decreased reactivation time under air soak in comparison with otherwise identical catalysts. Reducing reactivation time may, in turn, reduce costs, both in inventory and capital.
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5.发明授权Catalyst regeneration zone divided into sectors for regenerative catalytic units 有权催化剂再生区分为再生催化装置的部分公开(公告)号：US08901025B2
公开(公告)日：2014-12-02
申请号：US13636406
申请日：2011-02-18
IPC分类号： B01J38/38 , B01J38/44 , B01J38/20 , B01J38/32 , C10G45/00 , C10G45/58 , B01J38/24 , C10G11/00 , B01J38/14 , B01J38/34 , B01J38/12 , C10G11/18 , B01J38/00 , C10G35/00 , B01J8/12 , B01J38/02
CPC分类号： B01J38/38 , B01J8/125 , B01J38/00 , B01J38/02 , B01J38/12 , B01J38/14 , B01J38/20 , B01J38/24 , B01J38/32 , B01J38/34 , B01J38/44 , B01J2208/00371 , B01J2208/00504 , C10G11/00 , C10G11/187 , C10G35/00 , C10G45/00 , C10G45/58 , C10G2300/70 , C10G2300/708 , Y10S502/514 , Y10S502/515 , Y10S502/518
摘要： The present invention describes a combustion zone for a regenerative catalytic unit for the continuous regeneration of catalyst, said combustion zone having an annular shape and being divided into at least two combustion stages, each stage being divided into a number N of radial sectors, which are substantially equal, the catalyst flowing under gravity from one sector of the first combustion stage to the sector located in vertical alignment with the second combustion stage by means of drop legs, and the movement of the combustion gas being such that the combustion gas passes in succession through all of the sectors of the first combustion stage in any order, then all of the sectors of the second stage in any order.
摘要翻译： 本发明描述了一种用于催化剂连续再生的再生催化装置的燃烧区，所述燃烧区具有环形形状并被分成至少两个燃烧级，每一级分为N个径向扇区， 基本上相同的是，催化剂在重力作用下从第一燃烧级的一个部分流到位于与第二燃烧级垂直对准的部分，并且燃烧气体的运动使得燃烧气体连续通过 通过所有阶段的第一燃烧阶段的任何顺序，然后第二阶段的所有部门按任何顺序。
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公开(公告)号：US20140303414A1
公开(公告)日：2014-10-09
申请号：US14207474
申请日：2014-03-12
申请人： Anellotech, Inc.
发明人： Terry J. Mazanec , Jeffrey P. Whiting , Fred Pesa , Yu-Ting Cheng , Ruozhi Song
CPC分类号： B01J29/90 , B01J29/405 , B01J38/12 , B01J38/16 , B01J38/26 , B01J38/32 , B01J38/38 , B01J38/48 , B01J38/50 , B01J38/60 , B01J38/62 , B01J38/66 , C10B53/02 , C10B57/06 , Y02E50/14 , Y02E50/32 , Y02P20/145
摘要： Catalyst that is used in the catalytic pyrolysis of biomass is regenerated by oxidation and washing with a liquid to remove minerals and restore catalyst activity and selectivity to aromatics.
摘要翻译： 用于生物质的催化裂解的催化剂通过氧化和用液体洗涤来再生以除去矿物质并恢复催化剂活性和对芳族化合物的选择性。
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公开(公告)号：US20120259132A1
公开(公告)日：2012-10-11
申请号：US13440323
申请日：2012-04-05
IPC分类号： C07C1/20 , C07C41/14 , C07C27/00 , B01J37/02 , C07C209/00 , B01J23/02 , B01J23/72 , C07D301/22 , C07C41/02
CPC分类号： C07D301/22 , B01J21/04 , B01J23/50 , B01J23/52 , B01J23/66 , B01J23/72 , B01J23/78 , B01J23/83 , B01J23/94 , B01J23/96 , B01J35/0013 , B01J35/0033 , B01J35/006 , B01J35/1019 , B01J37/0201 , B01J37/031 , B01J38/38 , C07C1/24 , C07C41/09 , C07C45/38 , C07C2523/04 , C07C2523/10 , C07C2523/50 , C07C2523/52 , C07C2523/66 , C07C2523/72 , C07C2523/78 , C07C2523/83 , Y02P20/52 , Y02P20/584 , C07C43/06 , C07C47/06 , C07C11/04
摘要： The invention is directed to a process to prepare an ethanol-derivate compound or compounds by reacting ethanol in the presence of molecular oxygen and a catalyst comprising a gamma-alumina carrier, metal nano-particles wherein the metal is selected from silver, copper or gold. The invention is also directed to processes to prepare such a catalyst.
摘要翻译： 本发明涉及通过在分子氧存在下使乙醇反应制备乙醇衍生化合物或化合物的方法，所述催化剂包括γ-氧化铝载体，金属纳米颗粒，其中金属选自银，铜或金 。 本发明还涉及制备这种催化剂的方法。
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公开(公告)号：US20060217581A1
公开(公告)日：2006-09-28
申请号：US11089965
申请日：2005-03-25
申请人： Teng Xu , Stephen Vaughn , Kenneth Clem , James Beech , Pete Loezos
发明人： Teng Xu , Stephen Vaughn , Kenneth Clem , James Beech , Pete Loezos
IPC分类号： C07C1/00
CPC分类号： B01J29/90 , B01J29/85 , B01J38/12 , B01J38/38 , C10G3/45 , C10G3/49 , C10G3/62 , C10G2300/4006 , C10G2300/708 , C10G2300/802 , C10G2300/805 , C10G2400/20 , Y02P30/20 , Y10S502/514
摘要： This invention is directed to methods of converting oxygenates to olefin products. The methods provided include steps for protecting against deactivation of active molecular sieve catalysts during the conversion process. In particular, the invention provides for methods of regenerating coked catalyst to minimize catalyst deactivation due to contact with moisture.
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公开(公告)号：US20170297979A1
公开(公告)日：2017-10-19
申请号：US15509902
申请日：2015-09-09
发明人： Zeeshan Nawaz
CPC分类号： C07C5/3337 , B01J8/062 , B01J8/065 , B01J8/067 , B01J8/087 , B01J23/26 , B01J23/42 , B01J23/626 , B01J23/92 , B01J23/96 , B01J35/0006 , B01J38/04 , B01J38/06 , B01J38/10 , B01J38/12 , B01J38/16 , B01J38/38 , B01J2208/00194 , B01J2208/06 , B01J2208/065 , C07C5/321 , C07C5/3332 , C07C5/3335 , C07C5/48 , C07C2523/26 , C07C2523/42 , F23C2900/05081 , F27B1/005 , F27B1/08 , F27B1/10 , F27D99/0033 , Y02P20/584 , C07C11/02
摘要： Systems for dehydrogenating an alkane are provided. An exemplary system includes a furnace and further includes alkane heating chambers, regeneration mixture heating chambers, and two groups of reaction chambers, all located within the furnace. The alkane heating chambers and regeneration mixture heating chambers can preheat an alkane feed and a regeneration mixture feed, respectively. The two groups of reaction chambers can be switchably coupled to an alkane feed and a regeneration mixture feed such that an alkane can flow through one group of reaction chambers while a regeneration mixture flows through the other group of reaction chambers. Processes for dehydrogenating an alkane are also provided.
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公开(公告)号：US09085501B2
公开(公告)日：2015-07-21
申请号：US13298115
申请日：2011-11-16
申请人： Guozhen Qi , Zhe Yang , Huiming Zhang , Li Wang , Ju Wang , Xiaohong Li , Huawen Wang
发明人： Guozhen Qi , Zhe Yang , Huiming Zhang , Li Wang , Ju Wang , Xiaohong Li , Huawen Wang
CPC分类号： C07C1/20 , B01J29/85 , B01J29/90 , B01J38/30 , B01J38/38 , C07C2529/85 , Y02P20/52 , Y02P20/584 , Y02P30/42 , C07C11/04 , C07C11/06
摘要： A process for increasing the yield of ethylene and propylene, comprising: (1) feeding a feedstock into a reaction zone with a catalyst to produce (i) a product stream and a catalyst to be regenerated; (2) stripping and then dividing the catalyst to be regenerated into at least two parts, wherein a first part is recycled into the reaction zone at a first position, and a second part is regenerated in the regenerator to form a regenerated catalyst and then recycled into the reaction zone at a second position; and (3) controlling the temperature increase in the reaction zone.
摘要翻译： 一种提高乙烯和丙烯产率的方法，包括：（1）将原料与催化剂一起加入到反应区中以产生（i）产物流和待再生催化剂; （2）汽提然后将要再生的催化剂分成至少两部分，其中第一部分在第一位置再循环到反应区中，第二部分在再生器中再生以形成再生催化剂，然后再循环 在第二位置进入反应区; （3）控制反应区的温度升高。
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