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公开(公告)号：US5203988A
公开(公告)日：1993-04-20
申请号：US747897
申请日：1991-08-19
IPC分类号： C10G59/02
CPC分类号： C10G59/02
摘要： Disclosed is a process for catalytically reforming a gasoline boiling range hydrocarbonaceous feedstock. The reforming is conducted in multiple stages with heavy aromatics removal between the first and second stages.
摘要翻译： 公开了一种催化重整汽油沸程烃原料的方法。 重整在多个阶段进行，在第一和第二阶段之间除去重的芳族化合物。
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公开(公告)号：US5354451A
公开(公告)日：1994-10-11
申请号：US805360
申请日：1991-12-09
申请人： Stuart S. Goldstein , Paul W. Kamienski , David W. Staubs , Gerrit S. Swart , George A. Swan, III
发明人： Stuart S. Goldstein , Paul W. Kamienski , David W. Staubs , Gerrit S. Swart , George A. Swan, III
CPC分类号： C10G59/02
摘要： A two stage process for catalytically reforming a gasoline boiling range hydrocarbonaceous feedstock. The reforming is conducted in two stages wherein the first stage is operated in a fixed-bed mode, and the second stage is operated in a moving-bed continual catalyst regeneration mode. A gaseous stream comprised of hydrogen and predominantly C.sub.4.sup.-- hydrocarbon gases are separated between stages. A portion of the hydrogen-rich gaseous stream is recycled and the remaining portion along with the C.sub.5.sup.+ stream are sent to second stage reforming.
摘要翻译： 催化重整汽油沸程烃原料的两阶段方法。 重整在两个阶段进行，其中第一阶段以固定床模式操作，第二阶段以移动床连续催化剂再生模式操作。 由氢和主要是C4-烃气体组成的气流在两个阶段之间分离。 一部分富氢气流被再循环，剩余部分与C5 +流一起送入第二级重整。
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3.发明授权
公开(公告)号：US5196110A
公开(公告)日：1993-03-23
申请号：US805349
申请日：1991-12-09
申请人： Gerrit S. Swart , Paul W. Kamienski , Stuart S. Goldstein , David W. Staubs , George A. Swan, III
发明人： Gerrit S. Swart , Paul W. Kamienski , Stuart S. Goldstein , David W. Staubs , George A. Swan, III
IPC分类号： C10G59/02
CPC分类号： C10G59/02
摘要： A two stage catalytic reforming process. The first stage is comprised of two separate fixed-bed reforming units each comprised of one or more serially connected fixed-bed reforming zones. The second stage is comprised of one or more moving-bed reforming zones with continual catalyst regeneration. A hydrogen-rich gaseous stream is separated after each fixed-bed unit and a portion is recycled to the respective fixed-bed reforming zones.
摘要翻译： 二阶段催化重整过程。 第一阶段由两个单独的固定床重整单元组成，每个固定床重整单元均由一个或多个串联连接的固定床重整区组成。 第二阶段由具有连续催化剂再生的一个或多个移动床重整区组成。 在每个固定床单元之后分离富氢气流，一部分再循环到相应的固定床重整区。
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公开(公告)号：US20070232847A1
公开(公告)日：2007-10-04
申请号：US11731871
申请日：2007-03-30
IPC分类号： C07C7/144
CPC分类号： C10G70/045 , C10G31/11
摘要： Liquefied Petroleum Gas (LPG) can be recovered from various streams using a multiple membrane recovery process producing hydrogen stream at high yield and high purity and a C3+ LPG stream at high yield with low energy expenditure.
摘要翻译： 液化石油气（LPG）可以使用多重膜回收方法从各种物流中回收，该方法以高产率和高纯度产生氢气流，并在高温下产生C 3 H 3 O + 产能低能耗。
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公开(公告)号：US4839023A
公开(公告)日：1989-06-13
申请号：US97122
申请日：1987-09-16
摘要： Disclosed is a process for converting heavy hydrocarbonaceous feedstock to more valuable products. The feedstock is introduced into a coking unit containing a coking zone and a scrubbing zone. The bottoms fraction from the scrubbing zone is passed through a microfiltration unit, thus removing fine coke particles which are recycled to the coking zone. The substantially solids-free filtrate is hydrotreated, then passed to a catalytic cracking unit.
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公开(公告)号：US4834864A
公开(公告)日：1989-05-30
申请号：US97117
申请日：1987-09-16
摘要： Disclosed is a process wherein a scrubber bottom stream from a fluid coker is departiculated by passing it through a microfiltration system. The substantially solids-free filtrate is then upgraded by hydrotreating.
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公开(公告)号：US07799964B2
公开(公告)日：2010-09-21
申请号：US11731871
申请日：2007-03-30
IPC分类号： C07C7/144
CPC分类号： C10G70/045 , C10G31/11
摘要： Liquefied Petroleum Gas (LPG) can be recovered from various streams using a multiple membrane recovery process producing hydrogen stream at high yield and high purity and a C3+ LPG stream at high yield with low energy expenditure.
摘要翻译： 液化石油气（LPG）可以使用多重膜回收方法从各种物流中回收，该方法以高产率和高纯度产生氢气流，并以低能量消耗高产率的C3 + LPG流。
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公开(公告)号：US4368113A
公开(公告)日：1983-01-11
申请号：US297721
申请日：1981-08-31
摘要： A hydrocracking process is provided in which the heavy bottoms fraction recovered from the hydrocracked product is heat treated prior to being recycled to the hydrocracking zone. The resulting hydrocracked product has an increased amount of constituents boiling in the middle distillate range.
摘要翻译： 提供加氢裂化方法，其中从加氢裂化产物回收的重塔底馏分在再循环到加氢裂化区之前进行热处理。 所得到的加氢裂化产物在中间馏分范围内具有沸腾的成分的量增加。
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