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公开(公告)号：EP2072602B1
公开(公告)日：2018-05-02
申请号：EP07806230.4
申请日：2007-08-29
CPC分类号： C10G9/36 , C10G7/12 , C10G9/20 , C10G51/06 , C10G2300/807
摘要： The present invention relates to a process for thermal cracking of heavy petroleum oil, in which when a thermal cracking facility having a cracking furnace, two or more of trains each comprising two reaction vessels and one distillation tower is operated, each train is operated by repeating a cycle comprising drawing the heavy petroleum oil from the cracking furnace, feeding the drawn heavy petroleum oil into the first reaction vessel and then feeding the drawn heavy petroleum oil into the second reaction vessel, steam is directly brought in contact with the heavy petroleum oil to be thermally cracked, and gaseous cracked substances produced and steam are introduced into the distillation tower to be distilled and separated, wherein phase delay is provided for the cycle repeated in each train so that the thermal cracking facility is operated with the different initiation time of feeding to the first reaction vessel in each train. According to the present invention, the instability of the flow-in quantity of the gaseous substances to the distillation tower is improved, and the improvement of separation performance, the increase of processing capacity of the facility and the like can be achieved.
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公开(公告)号：EP2111439B1
公开(公告)日：2016-11-23
申请号：EP08708615.3
申请日：2008-02-04
发明人： CALIS, Hans Peter Alexander , HADJIGEORGE, Georghios Agamemnonons , MO, Weijian , RANGANATHAN, Easwar Santhosh
CPC分类号： C10G51/06 , C10G11/18 , C10G51/026 , C10G57/005 , C10G2300/1022 , C10G2300/807 , C10G2400/04 , C10G2400/06 , C10G2400/08
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3.发明公开INTEGRATED HYDROPROCESSING, STEAM PYROLYSIS CATALYTIC CRACKING PROCESS TO PRODUCE PETROCHEMICALS FROM CRUDE OIL 审中-公开具有集成HYDRO处理催化蒸汽裂解-破解方法对石化产品从原油生产
公开(公告)号：EP2828361A1
公开(公告)日：2015-01-28
申请号：EP13714166.9
申请日：2013-03-20
发明人： ABBA, Ibrahim, A. , SHAFI, Raheel , BOURANE, Abdennour , SAYED, Essam , AKHRAS, Abdul Rahman, Zafer
IPC分类号： C10G69/06 , C10G69/04 , C10G9/16 , C10G55/04 , C10G55/06 , C10G51/02 , C10G51/06 , B01D17/02 , B01D19/00 , B01D53/24 , C10G47/00 , C10G45/00
CPC分类号： C10G69/06 , C10G9/16 , C10G11/00 , C10G45/00 , C10G47/00 , C10G49/007 , C10G51/02 , C10G51/04 , C10G51/06 , C10G55/04 , C10G55/06 , C10G67/10 , C10G69/00 , C10G69/04 , C10G2300/201 , C10G2300/308 , C10G2400/20 , C10G2400/22 , C10G2400/30
摘要： An integrated hydrotreating, steam pyrolysis and catalytic cracking process for the production of olefins and aromatic petrochemicals from a crude oil feedstock is provided. Crude oil and hydrogen are charged to a hydroprocessing zone under conditions effective to produce a hydroprocessed effluent, which is thermally cracked in the presence of steam in a steam pyrolysis zone to produce a mixed product stream. Heavy components are catalytically cracked, which are derived from one or more of the hydroprocessed effluent, a heated stream within the steam pyrolysis zone, or the mixed product stream catalytically cracking. Catalytically cracked products are produced, which are combined with the mixed product stream and the combined stream is separated, and olefins and aromatics are recovered as product streams.
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4.发明公开PROCESS FOR MAXIMUM DISTILLATE PRODUCTION FROM FLUID CATALYTIC CRACKING UNITS (FCCU) 审中-公开用于生产最大馏出物催化FLUIDCRACKING单位
公开(公告)号：EP2780305A1
公开(公告)日：2014-09-24
申请号：EP12849160.2
申请日：2012-11-15
发明人： GBORDZOE, Eusebius , BORIES, Marc , LETZSCH, Warren Stewart , LEROY, Patrick , SANTNER, Chris , ROSS, Joseph, L., Jr.
IPC分类号： C07C4/02
CPC分类号： B01J21/08 , B01J21/04 , B01J21/066 , B01J21/12 , B01J21/20 , B01J23/02 , B01J23/92 , B01J29/04 , B01J29/08 , B01J29/40 , B01J29/90 , C10G11/182 , C10G51/026 , C10G51/06 , C10G2300/701 , C10G2400/04 , Y02P20/582
摘要： The present invention provides an improved fluidized catalytic cracking process coupled with a two stage regeneration process in which the activity of the circulating catalyst is independently controlled for cracking hydrocarbon feedstocks or the vapors at low severity to produce maximum light cycle oil/distillate in one riser whilst cracking recycle streams comprising heavy cycle oil (HCO), light cracked naphtha (LCN) etc. in a second riser operating at high severity to produce LPG.
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5.发明公开UPFLOW REGENERATION OF FCC CATALYST FOR MULTI STAGE CRACKING 审中-公开AUFSTROMREGENERATION EINES FCC-KATALYSATORSFÜRMEHRSTUFIGES CRACKEN
公开(公告)号：EP2591071A1
公开(公告)日：2013-05-15
申请号：EP11741289.0
申请日：2011-07-04
CPC分类号： B01J38/30 , B01J8/0025 , B01J8/30 , B01J8/388 , C10G11/182 , C10G51/06 , C10G2300/708
摘要： This invention relates to a process and an apparatus for regeneration of spent FCC catalyst using multiple reactors operation resulting in wide variation of coke on spent catalyst are disclosed. This process uses an up flow regenerator with divided injection of spent catalyst based on their coke content to control the residence time for its efficient regeneration and reduced hydrothermal deactivation. This system has the advantage of minimizing the exposure to the high temperature of low coked catalyst to the minimum possible time and high coke contained catalyst to the required time for its complete regeneration.
摘要翻译： 本发明涉及一种使用多个反应器操作再生废FCC催化剂的方法和装置，其导致废催化剂上焦炭的广泛变化。 该方法使用上流再生器，其基于其焦炭含量分配注入废催化剂以控制其有效再生的停留时间和减少的热液失活。 该系统具有将低焦化催化剂的高温暴露最小化至最少可能时间和将含焦炭的催化剂高达完全再生所需时间的优点。
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6.发明授权
公开(公告)号：EP1556462B1
公开(公告)日：2012-06-13
申请号：EP03809774.7
申请日：2003-10-29
CPC分类号： C10G51/06 , C10G11/05 , C10G11/18 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/202 , C10G2300/301 , C10G2300/308 , C10G2400/02 , C10G2400/28 , C10L1/04 , C10L2200/0438
摘要： A process is described for fluid catalytic cracking of hydrocarbons with high levels of basic nitrogen, where hydrocarbon feedstocks A and B with different levels of basic nitrogen are injected in a segregated fashion, into different risers of a multiple riser FCCU that possesses at least two risers. The injection of the feedstocks is made in such a way that feedstock A, to be injected in the riser with greater volume—main riser 7—possessing a level of basic nitrogen at least 200 ppm lower than the level of feedstock B to be injected into the riser with lower volume—secondary riser (8).
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7.发明授权
公开(公告)号：EP1532228B1
公开(公告)日：2011-12-14
申请号：EP02807530.7
申请日：2002-06-14
发明人： CANTRELL, Joel, G.
CPC分类号： C10G51/06 , C10G29/205 , C10G57/005
摘要： An improved process for the conversion of normally gaseous methane-hydrocarbon mixtures (1), such as natural gas, to a normally liquid hydrocarbon product (10) comprises separating the methane component of the gaseous mixture from the heavier hydrocarbon component, cracking the separated heavier hydrocarbon component (3) at a relatively low temperature and optionally cracking the methane component at a relatively high temperature. The low temperature cracking product and any high temperature cracking product (11) are separated into a light product (31) of principally hydrogen and a heavy product (7) comprising unsaturated hydrocarbons. This heavy product is reacted with methane in the presence of an acidic alkalization catalyst. The resulting product mixture (9) is separated into a light product (61), a portion of which is recycled, and the normally liquid hydrocarbon product (10).
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8.发明公开METHOD OF THERMAL CRACKING FOR PETROLEUM-DERIVED HEAVY OIL AND THERMAL CRACKING APPARATUS THEREFOR 有权方法油的重油热裂解THEREOF热裂解获得和设备
公开(公告)号：EP2072602A1
公开(公告)日：2009-06-24
申请号：EP07806230.4
申请日：2007-08-29
IPC分类号： C10G9/36
CPC分类号： C10G9/36 , C10G7/12 , C10G9/20 , C10G51/06 , C10G2300/807
摘要： The present invention relates to a process for thermal cracking of heavy petroleum oil, in which when a thermal cracking facility having a cracking furnace, two or more of trains each comprising two reaction vessels and one distillation tower is operated, each train is operated by repeating a cycle comprising drawing the heavy petroleum oil from the cracking furnace, feeding the drawn heavy petroleum oil into the first reaction vessel and then feeding the drawn heavy petroleum oil into the second reaction vessel, steam is directly brought in contact with the heavy petroleum oil to be thermally cracked, and gaseous cracked substances produced and steam are introduced into the distillation tower to be distilled and separated, wherein phase delay is provided for the cycle repeated in each train so that the thermal cracking facility is operated with the different initiation time of feeding to the first reaction vessel in each train. According to the present invention, the instability of the flow-in quantity of the gaseous substances to the distillation tower is improved, and the improvement of separation performance, the increase of processing capacity of the facility and the like can be achieved.
摘要翻译： 本发明涉及石油系重质油的热裂解的方法，其中当具有裂解炉，两个或更多个各自的列车包括两个反应容器和一个蒸馏塔的操作的热裂解处理装置中，每个列车通过重复操作 一个周期包括从所述裂化炉绘制石油系重质油，所绘制的石油系重质油进料至所述第一反应容器中，然后供给绘制石油系重质油进入第二反应容器中，蒸汽被直接带到接触的石油系重质油 被热裂化，和生成的气态物质和蒸汽被引入到蒸馏塔中进行蒸馏，分离，提供了一种用于重复每列车所以没有热裂解处理装置与进料的不同起始时间操作的周期worin相位延迟 在每个系的第一反应容器中。 。根据本发明，所述气态物质向蒸馏塔中的流入量中的不稳定性提高，分离性能，的设施的处理能力等，可以实现增加的改善。
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公开(公告)号：EP2591071B1
公开(公告)日：2018-12-12
申请号：EP11741289.0
申请日：2011-07-04
CPC分类号： B01J38/30 , B01J8/0025 , B01J8/30 , B01J8/388 , C10G11/182 , C10G51/06 , C10G2300/708
摘要： This invention relates to a process and an apparatus for regeneration of spent FCC catalyst using multiple reactors operation resulting in wide variation of coke on spent catalyst are disclosed. This process uses an up flow regenerator with divided injection of spent catalyst based on their coke content to control the residence time for its efficient regeneration and reduced hydrothermal deactivation. This system has the advantage of minimizing the exposure to the high temperature of low coked catalyst to the minimum possible time and high coke contained catalyst to the required time for its complete regeneration.
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10.发明授权FLUID CATALYTIC CRACKING PROCESS FOR MAXIMIZING LIGHT OLEFINS OR MIDDLE DISTILLATES AND LIGHT OLEFINS 有权流体催化裂化工艺最大限度地发挥轻质烯烃或中间馏分油和轻质烯烃
公开(公告)号：EP2872602B1
公开(公告)日：2018-02-14
申请号：EP13816487.6
申请日：2013-07-10
CPC分类号： C10G51/026 , B01J8/0015 , B01J8/0055 , B01J8/1809 , B01J8/1827 , B01J8/26 , B01J2208/00769 , C10G11/18 , C10G11/182 , C10G11/187 , C10G51/06 , C10G2300/1044 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/70 , C10G2400/02 , C10G2400/04 , C10G2400/20 , C10G2400/30
摘要： A fluid catalytic cracking apparatus and process is disclosed, providing for efficient conversion of heavy hydrocarbon feeds to light olefins, aromatics, and gasoline. A countercurrent flow reactor operating in bubbling or turbulent fluidization regimes is integrated with a fluid catalytic cracking riser reactor. A heavy hydrocarbon feed is catalytically cracked to naphtha and light olefins in the riser reactor, a co-current flow reactor. To enhance the yields and selectivity to light olefins, cracked hydrocarbon products from the riser reactor, such as C4 and naphtha range hydrocarbons, may be recycled and processed in the countercurrent flow reactor. The integration of the countercurrent flow reactor with a conventional FCC riser reactor and catalyst regeneration system may overcome heat balance issues commonly associated with two-stage cracking processes, may substantially increase the overall conversion and light olefins yield, and/or may increases the capability to process heavier feedstocks.
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