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公开(公告)号：EP2690160A4
公开(公告)日：2014-09-03
申请号：EP12764115
申请日：2012-03-23
发明人： YANAGAWA SHINICHIRO , IDA RYOJI , IWASA YASUYUKI , KOBAYASHI MASAHIDE , YASUI SUSUMU , SUGI YOSHISHIGE , FUKUI ATSUSHI , NAGUMO ATSURO
CPC分类号： C07C5/10 , C07C4/06 , C10G11/05 , C10G35/095 , C10G61/02 , C10G69/04 , C10G2300/4081 , C10G2300/802 , C10G2400/30 , Y02P20/132
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公开(公告)号：EP2690159A4
公开(公告)日：2014-09-03
申请号：EP12762799
申请日：2012-03-23
发明人： YANAGAWA SHINICHIRO , KOBAYASHI MASAHIDE , IDA RYOJI , YASUI SUSUMU , SUGI YOSHISHIGE , FUKUI ATSUSHI , NAGUMO ATSURO
IPC分类号： C10G69/04 , C07B61/00 , C07C4/18 , C07C5/13 , C07C15/04 , C07C15/06 , C07C15/08 , C10G11/05 , C10G11/10 , C10G11/18 , C10G45/44
CPC分类号： C07C4/06 , C10G69/04 , C10G69/10 , C10G2300/4081 , C10G2400/30 , Y02P20/582
摘要： A method for producing monocyclic aromatic hydrocarbons includes a cracking/reforming reaction step of introducing the feedstock oil into a cracking/reforming reactor, bringing the feedstock oil into contact with the catalyst, and causing the feedstock oil to react, thereby obtaining a product, a purification/recovery step of purifying and recovering the monocyclic aromatic hydrocarbons separated from the product produced in the cracking/reforming reaction step, a hydrogenation reaction step of hydrogenating a heavy fraction separated from the product produced in the cracking/reforming reaction step, and a recycling step of returning a hydrogenation reactant of the heavy fraction obtained in the hydrogenation reaction step to the cracking/reforming reaction step. In the recycling step, the hydrogenation reactant of the heavy fraction is introduced at a location different from an introduction location of the feedstock oil into the cracking/reforming reactor so that a time during which the hydrogenation reactant of the heavy fraction is in contact with the catalyst for monocyclic aromatic hydrocarbon production in the cracking/reforming reactor becomes shorter than a time during which the feedstock oil is in contact with the catalyst for monocyclic aromatic hydrocarbon production in the cracking/reforming reactor.
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公开(公告)号：EP2716737A4
公开(公告)日：2014-11-05
申请号：EP12790261
申请日：2012-05-24
发明人： YANAGAWA SHINICHIRO , IWASA YASUYUKI , IDA RYOJI , KOBAYASHI MASAHIDE , YASUI SUSUMU , SUGI YOSHISHIGE , FUKUI ATSUSHI , UTATSU AKIRA
IPC分类号： C10G11/05 , B01J29/06 , C07B61/00 , C07C4/08 , C07C5/10 , C07C5/41 , C07C6/12 , C07C7/04 , C07C15/04 , C07C15/06 , C07C15/08 , C10G35/095 , C10G45/44 , C10G47/00 , C10G69/04
CPC分类号： C07C5/02 , B01J23/44 , B01J23/755 , B01J23/883 , B01J23/888 , B01J29/405 , C07C4/02 , C07C6/126 , C07C7/00 , C10G11/05 , C10G11/18 , C10G35/04 , C10G35/065 , C10G35/095 , C10G35/10 , C10G45/44 , C10G2300/1044 , C10G2300/1048 , C10G2300/301 , C10G2300/4081 , C10G2400/20 , C10G2400/30 , Y02P20/132 , Y02P20/52 , C07C15/06 , C07C15/04
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公开(公告)号：EP2716735A4
公开(公告)日：2014-11-12
申请号：EP12789136
申请日：2012-05-24
发明人： YANAGAWA SHINICHIRO , FUJIYAMA YUICHIRO , IWASA YASUYUKI , IDA RYOJI , KOBAYASHI MASAHIDE , YASUI SUSUMU , SUGI YOSHISHIGE , FUKUI ATSUSHI , NAGUMO ATSURO
IPC分类号： C10G11/05 , B01J29/40 , B01J29/70 , B01J29/87 , C07B61/00 , C07C4/00 , C07C7/04 , C07C15/04 , C07C15/06 , C07C15/08 , C10G35/14
CPC分类号： C07C4/06 , B01D45/12 , B01J8/005 , B01J29/40 , B01J29/70 , B01J29/87 , C10G35/04 , C10G35/065 , C10G35/10 , C10G35/14 , C10G2300/1044 , C10G2300/1048 , C10G2300/301 , C10G2400/30
摘要： A method for producing monocyclic aromatic hydrocarbons includes a cracking and reforming reaction step of obtaining products containing monocyclic aromatic hydrocarbons having 6 to 8 carbon atoms and a heavy fraction having 9 or more carbon atoms by bringing the feedstock oil into contact with a catalyst for producing monocyclic aromatic hydrocarbons containing crystalline aluminosilicate to cause a reaction, a catalyst separation step of separating and removing the catalyst for producing monocyclic aromatic hydrocarbons together with tricyclic aromatic hydrocarbons contained in the products from a mixture of the products and a small amount of the catalyst for producing monocyclic aromatic hydrocarbons carried by the products, both of which are derived in the cracking and reforming reaction step, and a purification and recovery step of purifying and recovering the monocyclic aromatic hydrocarbons having 6 to 8 carbon atoms which are separated from the products formed in the cracking and reforming reaction step.
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5.发明公开OLEFIN AND SINGLE-RING AROMATIC HYDROCARBON PRODUCTION METHOD, AND ETHYLENE PRODUCTION DEVICE 审中-公开制备烯烃和芳烃单环烃及乙烯生产装置的方法
公开(公告)号：EP2913383A4
公开(公告)日：2016-07-13
申请号：EP13848235
申请日：2013-10-25
IPC分类号： C10G51/04 , C07B61/00 , C07C4/06 , C07C7/04 , C07C11/04 , C07C11/06 , C07C11/08 , C07C15/04 , C07C15/06 , C07C15/08 , C10G9/00 , C10G11/05 , C10G35/095 , C10G45/50 , C10G63/04 , C10G69/06 , C10G69/08
CPC分类号： C10G11/05 , B01J19/245 , B01J2219/24 , C10G35/04 , C10G35/095 , C10G63/04 , C10G69/04 , C10G69/06 , C10G69/08 , C10G2300/1051 , C10G2300/1055 , C10G2400/20 , C10G2400/22 , C10G2400/30
摘要： A method for producing an olefin and a monocyclic aromatic hydrocarbon of the present invention includes a cracking and reforming reaction step of obtaining a product containing an olefin and a monocyclic aromatic hydrocarbon by bringing a feedstock oil which is a thermally-cracked heavy oil obtained from an apparatus for producing ethylene which includes a cracking furnace and a product collection device that separates and collects an olefin and an aromatic hydrocarbon from a cracked product produced in the cracking furnace and which has a 90 volume% distillate temperature, as a distillation characteristic, of 390°C or lower into contact with a catalyst and reacting the feedstock oil; and a product collection step of collecting the olefin and the monocyclic aromatic hydrocarbon respectively by treating the product obtained in the cracking and reforming reaction step using the product collection device in the apparatus for producing ethylene.
摘要翻译： 本发明的烯烃和单环芳香族烃的制造方法包括裂化和重整反应步骤，通过将作为热裂化重质油的原料油（由 用于生产乙烯的装置包括裂解炉和从裂解炉中产生的裂化产物中分离和收集烯烃和芳烃并且具有90体积％馏出物温度作为蒸馏特性的产物收集装置，其为390 ℃以下与催化剂接触并使原料油反应; 以及通过在乙烯生产装置中使用产品收集装置处理在裂化和重整反应步骤中获得的产物分别收集烯烃和单环芳烃的产物收集步骤。
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公开(公告)号：EP2617797A4
公开(公告)日：2015-10-28
申请号：EP11825186
申请日：2011-09-14
IPC分类号： C10G65/12 , B01J29/40 , C07B61/00 , C07C4/18 , C07C6/06 , C07C15/02 , C10G9/00 , C10G35/095 , C10G45/68 , C10G47/20 , C10G69/08
CPC分类号： C07C4/06 , B01J23/882 , B01J29/06 , B01J29/061 , B01J29/405 , B01J35/023 , B01J37/0009 , B01J37/0045 , B01J2229/186 , C01B39/065 , C01B39/40 , C07C4/18 , C07C2529/40 , C10G9/00 , C10G29/205 , C10G35/095 , C10G45/68 , C10G51/04 , C10G57/005 , C10G63/04 , C10G65/046 , C10G69/04 , C10G69/06 , C10G69/08 , C10G2300/301 , C10G2300/4012 , C10G2300/4018 , C10G2400/30 , Y02P20/52 , C07C15/02
摘要： Provided is a method for producing aromatic hydrocarbons, by which a feedstock containing a hydrogenation-treated oil of a thermally cracked heavy oil obtainable from an ethylene production apparatus is brought into contact with a catalyst for monocyclic aromatic hydrocarbon production containing a crystalline aluminosilicate, and thereby aromatic hydrocarbons are produced. A raw material having an end point of the distillation characteristics of 400°C or lower is used as the feedstock. The contact between the feedstock and the catalyst for monocyclic aromatic hydrocarbon production is carried out at a pressure of 0.1 MPaG to 1.5 MPaG.
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公开(公告)号：EP2690157A4
公开(公告)日：2014-12-10
申请号：EP12762798
申请日：2012-03-23
CPC分类号： C07C4/06 , C10G35/065 , C10G45/64 , C10G63/04 , C10G2300/1033 , C10G2300/301 , C10G2400/30
摘要： A method of producing monocyclic aromatic hydrocarbons of the present invention includes bringing a light feedstock oil having a 10 vol% distillation temperature of 140°C to 205 °C and a 90 vol% distillation temperature of 300°C or lower, which has been prepared from a feedstock oil having a 10 vol% distillation temperature of 140°C or higher and a 90 vol% distillation temperature of 380°C or lower, into contact with a catalyst for monocyclic aromatic hydrocarbon production containing a crystalline aluminosilicate, in which a content ratio of monocyclic naphthenobenzenes in the light feedstock oil is adjusted by distillation of the feedstock oil such that the content ratio of monocyclic naphthenobenzenes in the light feedstock oil is higher than a content ratio of monocyclic naphthenobenzenes in the feedstock oil. According to the present invention, a method of producing a BTX fraction from a fraction containing a light cycle oil (LCO) produced by a FCC apparatus, which enables a more efficient production of the BTX fraction than conventional methods without the coexistence of high-pressure molecular hydrogen, can be provided.
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8.发明公开
公开(公告)号：EP2659971A4
公开(公告)日：2014-09-10
申请号：EP11852917
申请日：2011-12-28
IPC分类号： B01J29/40 , B01J29/70 , C07B61/00 , C07C4/06 , C07C15/04 , C07C15/06 , C07C15/067 , C10G11/05 , C10G45/68 , C10G69/04
CPC分类号： B01J29/7049 , B01J29/061 , B01J29/405 , B01J29/655 , B01J29/70 , B01J29/7073 , B01J29/708 , B01J29/7092 , B01J29/7096 , B01J37/0045 , B01J2229/36 , B01J2229/42 , C10G45/68 , C10G69/04 , C10G2300/301 , C10G2400/30
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9.发明公开CATALYST FOR PRODUCTION OF HYDROCARBONS AND PROCESS FOR PRODUCTION OF HYDROCARBONS 审中-公开催化剂用于烃的用于烃的制造生产和工艺
公开(公告)号：EP2527035A4
公开(公告)日：2014-02-26
申请号：EP11734730
申请日：2011-01-20
CPC分类号： B01J29/18 , B01J29/06 , B01J29/061 , B01J29/08 , B01J29/082 , B01J29/084 , B01J29/085 , B01J29/087 , B01J29/088 , B01J29/7007 , B01J29/7057 , B01J37/0009 , B01J37/28 , B01J2229/18 , B01J2229/183 , B01J2229/186 , B01J2229/36 , B01J2229/37 , C10G11/18 , C10G2300/107 , C10G2400/20 , C10G2400/30
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10.发明公开
公开(公告)号：EP2659970A4
公开(公告)日：2014-09-24
申请号：EP11852815
申请日：2011-12-28
CPC分类号： B01J29/7049 , B01J23/10 , B01J29/061 , B01J29/40 , B01J29/405 , B01J35/023 , B01J37/0009 , B01J37/0036 , B01J37/0201 , B01J2229/186 , B01J2229/42 , C07C4/06 , C10G11/05 , C10G47/16 , C10G47/20 , C10G69/04 , C10G2300/301 , C10G2400/30
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