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1.发明授权Hydrocracking catalyst for hydrocarbon oil, method for producing hydrocracking catalyst, and method for hydrocracking hydrocarbon oil with hydrocracking catalyst 有权烃油加氢裂化催化剂，加氢裂化催化剂的制备方法，加氢裂化催化剂加氢裂化烃油的方法公开(公告)号：US09221036B2
公开(公告)日：2015-12-29
申请号：US13809297
申请日：2011-08-02
申请人： Omer Refa Koseoglu , Adnan Al-Hajji , Ali Mahmood Al-Somali , Ali H. Al-Abdul'Al , Mishaal Al-Thukair , Masaru Ushio , Ryuzo Kuroda , Takashi Kameoka , Koji Nakano , Yuichi Takamori
发明人： Omer Refa Koseoglu , Adnan Al-Hajji , Ali Mahmood Al-Somali , Ali H. Al-Abdul'Al , Mishaal Al-Thukair , Masaru Ushio , Ryuzo Kuroda , Takashi Kameoka , Koji Nakano , Yuichi Takamori
CPC分类号： B01J29/166 , B01J23/755 , B01J29/088 , B01J29/80 , B01J29/89 , B01J35/1019 , B01J35/1023 , B01J37/0201 , B01J2229/16 , B01J2229/183 , B01J2229/37 , B01J2229/42 , C10G47/16 , C10G47/20 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/06 , C10G2400/08
摘要： The present invention relates to a hydrocracking catalyst for hydrocarbon oil comprising a support containing a framework-substituted zeolite-1 in which zirconium atoms and/or hafnium atoms form a part of a framework of an ultrastable y-type zeolite and a hydrogenative metal component carried thereon and a method for producing the same. The hydrocracking catalyst of the present invention makes it easy to diffuse heavy hydrocarbon oils such as VGO, DAO and the like into mesopores, is improved in a cracking activity and makes it possible to obtain a middle distillate at a high yield as compared with catalysts prepared by using zeolite comprising titanium and/or zirconium carried thereon.
摘要翻译： 本发明涉及一种用于烃油的加氢裂化催化剂，其包括含有骨架取代的沸石-1的载体，其中锆原子和/或铪原子构成超稳定型y型沸石的框架的一部分和携带的氢化金属组分 及其制造方法。 本发明的加氢裂化催化剂易于将诸如VGO，DAO等的重质烃油扩散到中孔中，裂化活性提高，与制备的催化剂相比，可以高收率地获得中间馏分 通过使用其上载有钛和/或锆的沸石。
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公开(公告)号：US09803148B2
公开(公告)日：2017-10-31
申请号：US13559846
申请日：2012-07-27
CPC分类号： C10G67/02 , C10G65/12 , C10G2300/301 , C10G2300/4093 , C10G2300/807 , C10G2400/02 , C10G2400/04
摘要： In a hydrocracking process, the product from the first stage reactor passes through a steam stripper to remove hydrogen, H2S, NH3, light gases (C1-C4), naphtha and diesel products. The stripper bottoms are separated from hydrogen, H2S, NH3, light gases (C1-C4), naphtha, and diesel products and treated in a second stage reactor. The effluent stream from the second stage reactor, along with the stream of separated hydrogen, H2S, NH3, light gases (C1-C4), naphtha, and diesel products, are passed to a separation stage for separating petroleum fractions. Preferably, the effluent stream from the first stage reactor is passed through a steam generator prior to the steam stripping step. In an alternate embodiment, the effluent stream from the first stage reactor is passed through a vapor/liquid separator stripper vessel prior to the steam stripping step.
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3.发明申请公开(公告)号：US20130175202A1
公开(公告)日：2013-07-11
申请号：US13809297
申请日：2011-08-02
申请人： Omer Refa Koseoglu , Adnan Al-Hajji , Ali Mahmood Al-Somali , Ali H. Al-Abdul'Al , Mishaal Al-Thukair , Masaru Ushio , Ryuzo Kuroda , Takashi Kameoka , Koji Nakano , Yuichi Takamori
发明人： Omer Refa Koseoglu , Adnan Al-Hajji , Ali Mahmood Al-Somali , Ali H. Al-Abdul'Al , Mishaal Al-Thukair , Masaru Ushio , Ryuzo Kuroda , Takashi Kameoka , Koji Nakano , Yuichi Takamori
CPC分类号： B01J29/166 , B01J23/755 , B01J29/088 , B01J29/80 , B01J29/89 , B01J35/1019 , B01J35/1023 , B01J37/0201 , B01J2229/16 , B01J2229/183 , B01J2229/37 , B01J2229/42 , C10G47/16 , C10G47/20 , C10G2300/107 , C10G2300/1074 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/06 , C10G2400/08
摘要： The present invention relates to a hydrocracking catalyst for hydrocarbon oil comprising a support containing a framework-substituted zeolite-1 in which zirconium atoms and/or hafnium atoms form a part of a framework of an ultrastable y-type zeolite and a hydrogenative metal component carried thereon and a method for producing the same. The hydrocracking catalyst of the present invention makes it easy to diffuse heavy hydrocarbon oils such as VGO, DAO and the like into mesopores, is improved in a cracking activity and makes it possible to obtain a middle distillate at a high yield as compared with catalysts prepared by using zeolite comprising titanium and/or zirconium carried thereon.
摘要翻译： 本发明涉及一种用于烃油的加氢裂化催化剂，其包括含有骨架取代的沸石-1的载体，其中锆原子和/或铪原子构成超稳定型y型沸石的框架的一部分和携带的氢化金属组分 及其制造方法。 本发明的加氢裂化催化剂易于将诸如VGO，DAO等的重质烃油扩散到中孔中，裂化活性提高，与制备的催化剂相比，可以高收率地获得中间馏分 通过使用其上载有钛和/或锆的沸石。
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公开(公告)号：US20130098802A1
公开(公告)日：2013-04-25
申请号：US13559846
申请日：2012-07-27
IPC分类号： C10G67/02
CPC分类号： C10G67/02 , C10G65/12 , C10G2300/301 , C10G2300/4093 , C10G2300/807 , C10G2400/02 , C10G2400/04
摘要： In a hydrocracking process, the product from the first stage reactor passes through a steam stripper to remove hydrogen, H2S, NH3, light gases (C1-C4), naphtha and diesel products. The stripper bottoms are separated from hydrogen, H2S, NH3, light gases (C1-C4), naphtha, and diesel products and treated in a second stage reactor. The effluent stream from the second stage reactor, along with the stream of separated hydrogen, H2S, NH3, light gases (C1-C4), naphtha, and diesel products, are passed to a separation stage for separating petroleum fractions. Preferably, the effluent stream from the first stage reactor is passed through a steam generator prior to the steam stripping step. In an alternate embodiment, the effluent stream from the first stage reactor is passed through a vapor/liquid separator stripper vessel prior to the steam stripping step.
摘要翻译： 在加氢裂化过程中，来自第一级反应器的产物通过蒸汽汽提器除去氢气，H 2 S，NH 3，轻质气体（C 1 -C 4），石脑油和柴油产物。 汽提器底部与氢气，H2S，NH3，轻质气体（C1-C4），石脑油和柴油产品分离，并在第二级反应器中进行处理。 来自第二级反应器的流出物流以及分离的氢气，H 2 S，NH 3，轻质气体（C 1 -C 4），石脑油和柴油产物的流被送入用于分离石油馏分的分离阶段。 优选地，来自第一级反应器的流出物流在汽提步骤之前通过蒸汽发生器。 在替代实施例中，来自第一级反应器的流出物流在蒸汽汽提步骤之前通过气/液分离器剥离器。
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