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公开(公告)号：EP2617697B1
公开(公告)日：2017-01-18
申请号：EP11825182.6
申请日：2011-09-14
IPC分类号： C07C7/04 , C07C15/04 , C07C15/06 , C07C15/067 , C07C15/24 , C10G11/05 , C07B61/00 , C10G35/095 , C10G45/44 , C10G63/02 , C10G69/00 , C10G69/08
CPC分类号： C10G11/05 , C10G35/095 , C10G45/44 , C10G63/02 , C10G69/00 , C10G69/08 , C10G2300/203 , C10G2300/301 , C10G2400/30
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公开(公告)号：EP2660227B1
公开(公告)日：2015-12-23
申请号：EP11853615.0
申请日：2011-12-28
IPC分类号： C07C4/00 , B01J29/80 , C07C4/26 , C07C15/02 , C10G11/05 , C10G11/18 , C07B61/00 , C10G45/68 , C10G69/04 , B01J37/04 , B01J29/40 , B01J29/65 , B01J29/82 , B01J29/87 , B01J35/10 , B01J29/70 , B01J37/00
CPC分类号： C10G11/05 , B01J29/40 , B01J29/65 , B01J29/703 , B01J29/7042 , B01J29/7046 , B01J29/80 , B01J29/82 , B01J29/87 , B01J35/10 , B01J37/0009 , B01J37/04 , B01J2229/18 , B01J2229/20 , B01J2229/42 , C10G11/18 , C10G45/68 , C10G69/04 , C10G2300/1037 , C10G2300/301 , C10G2400/30
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公开(公告)号：EP2716736A1
公开(公告)日：2014-04-09
申请号：EP12789643.9
申请日：2012-05-24
发明人： YANAGAWA, Shinichiro , FUJIYAMA, Yuichiro , IWASA, Yasuyuki , IDA, Ryoji , YASUI, Susumu , SUGI, Yoshishige , FUKUI, Atsushi , UTATSU, Akira
CPC分类号： C07C2/70 , C07C6/126 , C07C2529/87 , C10G11/05 , C10G29/205 , C10G35/065 , C10G45/64 , C10G69/04 , C10G2300/301 , C10G2400/30 , C07C15/08
摘要： The present method is a method for producing xylene from feedstock oil having a 10 vol% distillation temperature of 135°C or higher and a 90 vol% distillation temperature of 380°C or lower. This method includes a cracking/reforming reaction step of bringing the feedstock oil into contact with a catalyst to produce monocyclic aromatic hydrocarbons, a separation/recovery step of separating and recovering, from a product obtained by the cracking/reforming reaction step, a fraction A containing monocyclic aromatic hydrocarbons having a 10 vol% distillation temperature of 75°C or higher and a 90 vol% distillation temperature of 140°C or lower, a xylene fraction containing xylene, and a fraction B containing monocyclic aromatic hydrocarbons having a 10 vol% distillation temperature of 145°C or higher and a 90 vol% distillation temperature of 215°C or lower, and a xylene conversion step of bringing a mixed fraction obtained by mixing the fractions A and B with each other into contact with a catalyst containing a solid acid to convert the mixed fraction into xylene.
摘要翻译： 本方法是由10体积％蒸馏温度为135℃或更高和90体积％蒸馏温度为380℃或更低的原料油生产二甲苯的方法。 该方法包括使原料油与催化剂接触而生成单环芳香族烃的裂化/重整反应工序，从裂化重整反应工序得到的生成物中分离回收馏分A的分离回收工序 含有10体积％馏出温度75℃以上，90体积％馏出温度140℃以下的含氟单环芳香族烃，含二甲苯的二甲苯馏分和含有10体积％以上的单环芳香族烃的馏分B， 蒸馏温度为145℃以上，且90体积％的蒸馏温度为215℃以下的二甲苯转化工序和使混合工序A和工序B得到的混合馏分与含有 固体酸将混合部分转化成二甲苯。
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14.发明公开
公开(公告)号：EP2659972A1
公开(公告)日：2013-11-06
申请号：EP11853109.4
申请日：2011-12-28
CPC分类号： B01J29/70 , B01J29/85 , B01J37/0009 , B01J37/0036 , B01J2229/186 , C01B39/10 , C01B39/48 , C07C4/06 , C07C2529/06 , C07C2529/40 , C10G11/05 , C10G11/18 , C10G47/16 , C10G2300/1033 , C10G2300/1048 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/301 , C10G2400/30
摘要： The catalyst for producing aromatic hydrocarbon is for producing monocyclic aromatic hydrocarbon having 6 to 8 carbon number from oil feedstock having a 10 volume% distillation temperature of 140°C or higher and a 90 volume% distillation temperature of 380°C or lower and contains crystalline aluminosilicate and phosphorus. A molar ratio (P/Al ratio) between phosphorus contained in the crystalline aluminosilicate and aluminum of the crystalline aluminosilicate is from 0.1 to 1.0. The production method of monocyclic aromatic hydrocarbon is a method of bringing oil feedstock having a 10 volume% distillation temperature of 140°C or higher and a 90 volume% distillation temperature of 380°C or lower into contact with the catalyst for producing monocyclic aromatic hydrocarbon.
摘要翻译： 该芳香族烃制造用催化剂是由10体积％的馏出温度为140℃以上，90体积％的馏出温度为380℃以下的油原料制造碳原子数为6〜8的单环芳香族烃的催化剂， 铝硅酸盐和磷。 结晶硅铝酸盐中含有的磷和结晶硅铝酸盐中铝之间的摩尔比（P / Al比）为0.1-1.0。 单环芳香族烃的制造方法是使10体积％馏出温度为140℃以上，90体积％馏出温度为380℃以下的油原料与单环芳香族烃制造用催化剂接触的方法 。
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