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1. 发明授权

US09815047B2 Catalyst for producing monocyclic aromatic hydrocarbon and production method of monocyclic aromatic hydrocarbon 有权
公开(公告)号：US09815047B2
公开(公告)日：2017-11-14
申请号：US13976655
申请日：2011-12-28
申请人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
发明人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
IPC分类号： C07C4/06 , B01J29/70 , C10G11/18 , C10G47/16 , C10G11/05 , B01J29/85 , B01J37/00 , C01B39/48 , C01B39/10
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.

2. 发明申请

US20130281756A1 PRODUCTION METHOD OF MONOCYCLIC AROMATIC HYDROCARBONS 有权
标题翻译：单环芳烃的生产方法
公开(公告)号：US20130281756A1
公开(公告)日：2013-10-24
申请号：US13976701
申请日：2011-12-28
申请人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
发明人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
IPC分类号： C10G11/05
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
摘要： In the production method of monocyclic aromatic hydrocarbons, oil feedstock having a 10 volume % distillation temperature of 140° C. or higher and a 90 volume % distillation temperature of 380° C. or lower is brought into contact with a catalyst for producing monocyclic aromatic hydrocarbons that includes a mixture containing a first catalyst which contains crystalline aluminosilicate containing gallium and/or zinc and phosphorus and a second catalyst which contains crystalline aluminosilicate containing phosphorus.
摘要翻译：在单环芳烃的制造方法中，使具有140℃或更高的10体积％蒸馏温度和380℃或更低的90体积％蒸馏温度的油原料与用于制备单环芳族化合物的催化剂接触包括含有含有含有镓和/或锌和磷的结晶硅铝酸盐的第一催化剂和含有含磷结晶硅铝酸盐的第二催化剂的混合物的烃。

3. 发明申请

US20130281755A1 CATALYST FOR PRODUCING MONOCYCLIC AROMATIC HYDROCARBONS AND PRODUCTION METHOD OF MONOCYCLIC AROMATIC HYDROCARBONS 审中-公开
标题翻译：生产单环芳烃的催化剂和单环芳烃的生产方法
公开(公告)号：US20130281755A1
公开(公告)日：2013-10-24
申请号：US13976581
申请日：2011-12-28
申请人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
发明人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
IPC分类号： B01J29/70 , C07C4/06
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
摘要： The catalyst for producing monocyclic aromatic hydrocarbons is for producing monocyclic aromatic hydrocarbons 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. The catalyst contains crystalline aluminosilicate and a rare earth element, in which the amount of the rare earth element expressed in terms of the element is 0.1 to 10 mass % based on the crystalline aluminosilicate. In the production method of monocyclic aromatic hydrocarbons, oil feed stock having a 10 volume % distillation temperature of 140° C. or higher and a 90 volume % distillation temperature of 380° C. or lower is brought into contact with the catalyst for producing monocyclic aromatic hydrocarbons.
摘要翻译：用于生产单环芳烃的催化剂用于生产具有10体积％蒸馏温度为140℃或更高，90体积％蒸馏温度为380℃或更低的油原料具有6至8个碳数的单环芳烃。催化剂含有结晶硅铝酸盐和稀土元素，其中以元素表示的稀土元素的量相对于结晶铝硅酸盐为0.1〜10质量％。在单环芳香烃的制造方法中，将具有10体积％蒸馏温度为140℃以上，90体积％蒸馏温度为380℃以下的原料原料与用于制造单环芳烃的催化剂接触芳烃。

4. 发明申请

US20130184506A1 METHOD FOR PRODUCING AROMATIC HYDROCARBONS 审中-公开
标题翻译：生产芳香烃的方法
公开(公告)号：US20130184506A1
公开(公告)日：2013-07-18
申请号：US13822556
申请日：2011-09-14
申请人： Shinichiro Yanagawa , Ryoji Ida , Masahide Kobayashi , Yasuyuki Iwasa
发明人： Shinichiro Yanagawa , Ryoji Ida , Masahide Kobayashi , Yasuyuki Iwasa
IPC分类号： C10G11/05
CPC分类号： C10G11/05 , C10G35/095 , C10G45/44 , C10G63/02 , C10G69/00 , C10G69/08 , C10G2300/203 , C10G2300/301 , C10G2400/30
摘要： Disclosed is a method for producing aromatic hydrocarbons including a cracking reforming reaction step of bringing a feedstock 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 to cause the feedstock to react with the catalyst, and thereby obtaining a product including monocyclic aromatic hydrocarbons having 6 to 8 carbon numbers and a heavy oil fraction having 9 or more carbon numbers; a step of separating the monocyclic aromatic hydrocarbons and the heavy oil fraction from the product obtained from the cracking reforming reaction step; a step of purifying the monocyclic aromatic hydrocarbons separated in the separating step, and collecting the hydrocarbons; and a step of separating naphthalene compounds from the heavy oil fraction separated in the separating step, and collecting the naphthalene compounds.
摘要翻译：本发明公开了一种芳烃化合物的制造方法，其特征在于，包括裂解重整反应步骤，使10vol％蒸馏温度为140℃以上，90体积％蒸馏温度为380℃以下的原料与含有结晶硅铝酸盐以使原料与催化剂反应的单环芳香烃生产催化剂，从而得到包括具有6至8个碳数的单环芳烃和具有9个或更多个碳数的重油馏分的产物; 从裂解重整反应步骤获得的产物中分离单环芳烃和重油馏分的步骤; 纯化在分离步骤中分离的单环芳烃并收集烃的步骤; 以及从分离步骤中分离的重油馏分中分离萘化合物的步骤，并收集萘化合物。

5. 发明申请

US20140024871A1 METHOD OF PRODUCING MONOCYCLIC AROMATIC HYDROCARBONS 有权
标题翻译：生产单环芳香烃的方法
公开(公告)号：US20140024871A1
公开(公告)日：2014-01-23
申请号：US14006986
申请日：2012-03-23
申请人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
发明人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
IPC分类号： C07C4/06
CPC分类号： C07C4/06 , C10G11/18 , C10G45/60 , C10G45/70 , C10G47/00 , C10G47/20 , C10G2300/1044 , C10G2300/1048 , C10G2300/1051 , C10G2300/1055 , C10G2300/1096 , C10G2300/301 , C10G2300/4025 , C10G2400/30
摘要： A method of producing monocyclic aromatic hydrocarbons includes bringing 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 feedstock oil is adjusted to 10 mass % to 90 mass %, by mixing a hydrocarbon oil A having a 10 vol % distillation temperature of 140° C. or higher and a 90 vol % distillation temperature of 380° C. or lower with a hydrocarbon oil B containing more monocyclic naphthenobenzenes than the hydrocarbon oil A.
摘要翻译：制造单环芳烃的方法包括将10体积％蒸馏温度为140℃以上，90体积％蒸馏温度为380℃以下的原料油与单环式芳烃的催化剂接触将含有10质量％蒸馏温度为140℃以上的烃油A与140℃以上的烃油混合，将原料油中的单环式萘并苯的含有比例调整为10质量％〜90质量％的结晶性硅铝酸盐的制造与含有比烃油A更多的单环萘并苯的烃油B的90体积％蒸馏温度为380℃以下。

6. 发明授权

US09382484B2 Production method of monocyclic aromatic hydrocarbons 有权
标题翻译：单环芳烃的生产方法
公开(公告)号：US09382484B2
公开(公告)日：2016-07-05
申请号：US13976701
申请日：2011-12-28
申请人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
发明人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
IPC分类号： C07C4/18 , C07C5/00 , C10G11/05 , C10G11/18 , B01J37/04 , B01J29/80 , B01J37/00 , C10G45/68 , C10G69/04 , B01J29/40 , B01J29/65 , B01J29/70 , B01J29/82 , B01J29/87 , B01J35/10
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
摘要： In the production method of monocyclic aromatic hydrocarbons, oil feedstock having a 10 volume % distillation temperature of 140° C. or higher and a 90 volume % distillation temperature of 380° C. or lower is brought into contact with a catalyst for producing monocyclic aromatic hydrocarbons that includes a mixture containing a first catalyst which contains crystalline aluminosilicate containing gallium and/or zinc and phosphorus and a second catalyst which contains crystalline aluminosilicate containing phosphorus.
摘要翻译：在单环芳烃的制造方法中，使具有140℃或更高的10体积％蒸馏温度和380℃或更低的90体积％蒸馏温度的油原料与用于制备单环芳族化合物的催化剂接触包括含有含有含有镓和/或锌和磷的结晶硅铝酸盐的第一催化剂和含有含磷结晶硅铝酸盐的第二催化剂的混合物的烃。

7. 发明申请

US20140200377A1 METHOD FOR PRODUCING MONOCYCLIC AROMATIC HYDROCARBONS 有权
标题翻译：生产单环芳香烃的方法
公开(公告)号：US20140200377A1
公开(公告)日：2014-07-17
申请号：US14119576
申请日：2012-05-24
申请人： Shinichiro Yanagawa , Yasuyuki Iwasa , Ryoji Ida , Masahide Kobayashi , Susumu Yasui , Yoshishige Sugi , Atsushi Fukui , Akira Utatsu
发明人： Shinichiro Yanagawa , Yasuyuki Iwasa , Ryoji Ida , Masahide Kobayashi , Susumu Yasui , Yoshishige Sugi , Atsushi Fukui , Akira Utatsu
IPC分类号： C07C5/02 , C07C4/02 , C07C7/00
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
摘要： The present method for producing monocyclic aromatic hydrocarbons is a method for producing monocyclic aromatic hydrocarbons having 6 to 8 carbon atoms. This method includes a cracking and reforming reaction step of bringing oil feedstock into contact with a catalyst to cause a reaction and obtain a product containing monocyclic aromatic hydrocarbons having 6 to 8 carbon atoms and a heavy fraction having 9 or more carbon atoms, a purification and recovery step of purifying and recovering the monocyclic aromatic hydrocarbons having 6 to 8 carbon atoms separated from the product formed by the cracking and reforming reaction step, and a first returning step of returning at least a portion of toluene obtained by the purification and recovery step to the cracking and reforming reaction step.
摘要翻译：本发明的单环芳烃的制造方法是制造碳原子数为6〜8的单环芳烃的方法。该方法包括使油原料与催化剂接触以引起反应的裂化和重整反应步骤，并获得含有具有6至8个碳原子的单环芳族烃和具有9个或更多个碳原子的重馏分的产物，纯化和纯化和回收由裂解和重整反应步骤形成的产物分离出的具有6至8个碳原子的单环芳烃的回收步骤，和将至少一部分通过纯化和回收步骤获得的甲苯返回至裂化和重整反应步骤。

8. 发明申请

US20140012055A1 METHOD FOR PRODUCING MONOCYCLIC AROMATIC HYDROCARBONS 有权
标题翻译：生产单环芳香烃的方法
公开(公告)号：US20140012055A1
公开(公告)日：2014-01-09
申请号：US14006778
申请日：2012-03-23
申请人： Shinichiro Yanagawa , Masahide Kobayashi , Ryoji Ida , Yasuyuki Iwasa
发明人： Shinichiro Yanagawa , Masahide Kobayashi , Ryoji Ida , Yasuyuki Iwasa
IPC分类号： C07C4/06
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 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.
摘要翻译：一种制备单环芳烃的方法包括将10vol％蒸馏温度为140℃至205℃的轻质原料油和300℃或更低的90vol％蒸馏温度，具有10体积％蒸馏温度为140℃以上且90体积％蒸馏温度为380℃以下的原料油与含有结晶性硅铝酸盐的单环芳烃生产用催化剂接触，其中，通过蒸馏原料油调节轻质原料油中单环式萘并苯的含量比，使得轻质原料油中的单环萘并苯的含量比例高于原料油中的单环萘并苯的含量比。

9. 发明申请

US20130289325A1 CATALYST FOR PRODUCING MONOCYCLIC AROMATIC HYDROCARBON AND PRODUCTION METHOD OF MONOCYCLIC AROMATIC HYDROCARBON 有权
标题翻译：单环芳烃生产催化剂及单环芳烃生产方法
公开(公告)号：US20130289325A1
公开(公告)日：2013-10-31
申请号：US13976655
申请日：2011-12-28
申请人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
发明人： Shinichiro Yanagawa , Masahide Kobayashi , Yasuyuki Iwasa , Ryoji Ida
IPC分类号： B01J29/70
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：用于制备芳族烃的催化剂用于制备具有10体积％蒸馏温度为140℃或更高的蒸馏温度为90℃或更低的90℃的蒸馏温度为380℃或更低的油原料的具有6至8个碳数的单环芳烃，含有结晶硅铝酸盐和磷。结晶硅铝酸盐中所含的磷与结晶硅铝酸盐的铝之间的摩尔比（P / Al比）为0.1〜1.0。单环芳烃的制造方法是将具有140体积％以上的10体积％蒸馏温度和380℃以下的90体积％蒸馏温度的油原料与用于制造单环芳烃的催化剂接触的方法芳烃。

10. 发明授权

US09828309B2 Method for producing monocyclic aromatic hydrocarbons 有权
公开(公告)号：US09828309B2
公开(公告)日：2017-11-28
申请号：US14119281
申请日：2012-05-24
申请人： Shinichiro Yanagawa , Yuichiro Fujiyama , Yasuyuki Iwasa , Ryoji Ida , Masahide Kobayashi , Susumu Yasui , Yoshishige Sugi , Atsushi Fukui , Atsuro Nagumo
发明人： Shinichiro Yanagawa , Yuichiro Fujiyama , Yasuyuki Iwasa , Ryoji Ida , Masahide Kobayashi , Susumu Yasui , Yoshishige Sugi , Atsushi Fukui , Atsuro Nagumo
IPC分类号： C07C4/06 , C10G35/06 , B01D45/12 , B01J8/00 , C10G35/14 , C10G35/04 , C10G35/10 , B01J29/40 , B01J29/70 , B01J29/87
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： 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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