专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明申请

WO1993002794A1 REGENERATION OF FLUIDIZED CATALYTIC CRACKING CATALYST 审中-公开
标题翻译：流化催化裂化催化剂的再生
公开(公告)号：WO1993002794A1
公开(公告)日：1993-02-18
申请号：PCT/US1991005532
申请日：1991-08-05
申请人： MOBIL OIL CORPORATION
发明人： MOBIL OIL CORPORATION , OWEN, Hartley , SCHIPPER, Paul, Herbert
IPC分类号： B01J38/38
CPC分类号： C10G11/182 , B01J29/90 , B01J38/34 , B01J38/38
摘要： A process is disclosed for simultaneously heating and cooling spent FCC catalyst during regeneration in a high efficiency FCC regenerator using a fast fluidized bed coke combustor (50). The coke combustor (50) burns coke from the spent catalyst in a turbulent or fast fluidized bed (52), and discharges catalyst and flue gas up into a dilute phase transport riser (56), where the catalyst is separated from the flue gas and flows to a bubbling dense bed (75) of catalyst. The coke combustor (50) is heated by recyling hot catalyst from the bubbling dense bed (75) and simultaneously cooled by a backmixed heat exchanger (203). Catalyst flows from the combustor (50) to the heat exchanger (203), and is displaced back into the combustor (50) by adding air to the catalyst in the cooler (203). Heating promotes rapid coke combustion, while cooling reduces thermal and hydrothermal deactivation of the spent catalyst. High superficial vapor velocities in the heat exchanger (203) promote heat transfer without disrupting flow in the fast fluidized bed coke combustor (50), and without increasing catalyst traffic in the flue gas above the bubbling dense bed (75).
摘要翻译：公开了一种用于在使用快速流化床焦炭燃烧器（50）的高效FCC再生器中再生期间同时加热和冷却废FCC催化剂的方法。焦炭燃烧器（50）在湍流或快速流化床（52）中从废催化剂燃烧焦炭，并将催化剂和烟道气排放到稀相运输提升器（56）中，其中催化剂与烟道气分离，流入催化剂的鼓泡密床（75）。焦炭燃烧器（50）通过从发泡致密床（75）再循环热催化剂而加热，并同时由反混热交换器（203）冷却。催化剂从燃烧器（50）流到热交换器（203），并通过向冷却器（203）中的催化剂添加空气而返回到燃烧器（50）中。加热促进快速焦炭燃烧，而冷却减少废催化剂的热和水热失活。热交换器（203）中的高表观蒸气速度促进热传递而不破坏快速流化床焦炭燃烧器（50）中的流动，并且不增加在起泡致密床（75）上方的烟道气中的催化剂流量。

2. 发明申请

WO2017196586A1 A PROCESS FOR REACTING OXYGEN CARRYING REGENERATED CATALYST PRIOR TO USE IN A FLUIDIZED BED REACTOR 审中-公开
标题翻译：在流化床反应器中使用之前用于使负载氧的再生催化剂反应的方法
公开(公告)号：WO2017196586A1
公开(公告)日：2017-11-16
申请号：PCT/US2017/030582
申请日：2017-05-02
申请人： DOW GLOBAL TECHNOLOGIES LLC
发明人： PRETZ, Matthew T. , LI, Liwei
IPC分类号： C10G11/18 , B01J8/24 , B01J38/30 , B01J38/18 , B01J38/38
摘要： A process to react an oxygen containing regenerated catalyst stream prior to use in a fluidized bed reactor comprising providing a regenerated catalyst stream which comprises at least 0.001 wt% oxygen; reacting the regenerated catalyst stream with a fuel source thereby forming oxides and reducing the amount of oxygen in the regenerated catalyst stream to produce a usable regenerated catalyst stream; and injecting the usable regenerated catalyst stream into a hydrocarbon fluidized bed reactor is provided.
摘要翻译：在用于流化床反应器之前使含氧的再生催化剂物流反应的方法，包括提供包含至少0.001重量％氧的再生催化剂物流; 使再生催化剂流与燃料源反应，从而形成氧化物并减少再生催化剂流中的氧量以产生可用的再生催化剂流; 并将可用的再生催化剂物流注入烃流化床反应器中。

3. 发明申请

WO2014165223A3 REGENERATION OF CATALYTIC FAST PYROLYSIS CATALYST 审中-公开
公开(公告)号：WO2014165223A3
公开(公告)日：2014-10-09
申请号：PCT/US2014/024855
申请日：2014-03-12
申请人： ANELLOTECH, INC.
发明人： MAZANEC, Terry J. , WHITING, Jeffrey P. , PESA, Fred , CHENG, Yu-Ting , SONG, Ruozhi
IPC分类号： B01J38/12 , B01J38/16 , B01J38/26 , B01J38/32 , B01J38/38 , B01J38/48 , B01J38/50 , B01J38/60 , B01J38/62 , B01J38/66 , B01J29/40 , B01J29/90 , C10J3/20 , C10B53/02 , C10G2/00
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.

4. 发明申请

WO2014035590A1 CATALYST COMPOSITION AND REACTIVATION PROCESS USEFUL FOR ALKANE DEHYDROGENATIONS 审中-公开
标题翻译：用于碱脱氢酶的催化剂组合物和反应过程
公开(公告)号：WO2014035590A1
公开(公告)日：2014-03-06
申请号：PCT/US2013/052830
申请日：2013-07-31
申请人： DOW GLOBAL TECHNOLOGIES LLC
发明人： LUO, Lin , STEARS, Brien A.
IPC分类号： B01J38/02 , B01J38/12 , B01J38/38 , B01J23/89 , B01J23/652 , B01J23/648 , B01J23/96 , C07C5/32 , 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.
摘要翻译：在选自二氧化硅，氧化铝，二氧化硅 - 氧化铝组合物，稀土改性氧化铝及其组合的载体上，掺杂有铁的催化剂，包含IIIA族金属，VIII族贵金属和任选的助催化剂金属，VIB族金属，VB族金属或其组合，与其他相同的催化剂相比，在空气浸泡下提供降低的再活化时间。反过来，减少重新启动时间可能会降低库存和资本成本。

5. 发明申请

WO1993008912A1 A PROCESS FOR REGENERATING SPENT FLUIDIZED CATALYTIC CRACKING CATALYST 审中-公开
标题翻译：一种再生流态流化催化裂化催化剂的方法
公开(公告)号：WO1993008912A1
公开(公告)日：1993-05-13
申请号：PCT/US1991007980
申请日：1991-10-30
申请人： MOBIL OIL CORPORATION
发明人： MOBIL OIL CORPORATION , OWEN, Hartley , SCHIPPER, Paul, Herbert
IPC分类号： B01J38/38
CPC分类号： B01J38/34 , B01J29/90 , C10G11/182 , C10G11/187
摘要： In a process for controlled, multi-stage regeneration of FCC catalyst, a modified high efficiency catalyst regenerator (80), with a fast fluidized bed coke combustor (62), dilute phase transport riser (83), and second fluidized bed (82) regenerates the catalyst in at least two stages. The primary stage of regeneration is in the coke combustor (62), whereas a second stage catalyst regeneration occurs in the second fluidized bed (82). The amount of combustion air added to, and conditions in, the coke combustor (62) are controlled to limit CO combustion, while the second stage of regeneration, in the second fluidized bed (82), achieves complete CO combustion. Controlled multi-stage regeneration reduces steaming or deactivation of a catalyst during regeneration, increase coke burning capacity, and reduces NOx emissions.
摘要翻译：在FCC催化剂的受控多级再生过程中，使用快速流化床焦炭燃烧器（62），稀相运输提升器（83）和第二流化床（82）的改进的高效催化剂再生器（80）在至少两个阶段再生催化剂。再生的主要阶段在焦炭燃烧器（62）中，而第二阶段催化剂再生发生在第二流化床（82）中。控制焦炭燃烧器（62）中的燃烧空气量和条件，以限制CO燃烧，而第二流化床（82）中的第二再生阶段实现完全的CO燃烧。受控的多级再生减少了再生期间催化剂的蒸发或失活，增加了焦炭燃烧能力，并且减少了NOx排放。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式