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公开(公告)号:US20150224485A1
公开(公告)日:2015-08-13
申请号:US14616028
申请日:2015-02-06
Applicant: BASF Corporation
Inventor: Robert McGuire
IPC: B01J29/80 , B01J23/656 , B01J23/755 , B01J35/08 , B01J35/10 , C07C1/20 , B01J29/40 , B01J35/00 , B01J21/04 , C07C41/18 , C07C29/132 , B01J29/08 , B01J23/28
CPC classification number: B01J29/80 , B01J21/06 , B01J21/08 , B01J23/16 , B01J23/24 , B01J23/42 , B01J23/6567 , B01J23/755 , B01J29/061 , B01J29/084 , B01J29/166 , B01J29/40 , B01J29/48 , B01J29/87 , B01J35/0006 , B01J35/08 , B01J37/0205 , B01J37/04 , B01J2229/42 , C01B3/16 , C07C1/20 , C07C27/00 , C07C37/52 , C07C41/01 , C07C2521/04 , C07C2523/28 , C07C2523/36 , C07C2523/42 , C07C2523/656 , C07C2523/755 , C07C2529/40 , C07C2529/80 , C10G3/49 , C10G2300/1014 , C10G2400/30 , Y02P20/52 , Y02P20/588 , Y02P30/20 , C07C43/23 , C07C39/08 , C07C15/08 , C07C15/02
Abstract: A novel catalyst blend for processing of feedstocks into monoaromatics in a single stage, comprising at least one cracking catalyst, one heterogeneous transition metal catalyst, and optionally at least one hydrogenation catalyst. The process occurs in one-step or single stage with substantially no solvents or external additives, or when the feedstock contains less than 15% oxygen, the process includes additional water or steam to enable sufficient amounts of H2 being produced in-situ.
Abstract translation: 一种用于在单一阶段将原料加工成单芳族化合物的新型催化剂共混物,其包含至少一种裂化催化剂,一种非均相过渡金属催化剂和任选的至少一种氢化催化剂。 该方法在基本没有溶剂或外部添加剂的一步或单一阶段中发生,或者当原料含有小于15%的氧气时,该方法包括另外的水或蒸汽,以使得能够在原位产生足够量的H 2。
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公开(公告)号:US20170362513A1
公开(公告)日:2017-12-21
申请号:US15264428
申请日:2016-09-13
Applicant: BASF Corporation
Inventor: Robert McGuire , Gary M. Smith , Bilge Yilmaz , Sven Serneels
CPC classification number: C10G11/05 , B01J29/084 , B01J35/023 , B01J35/08 , B01J35/1009 , B01J35/1014 , B01J35/1019 , B01J2229/42 , C10G11/18 , C10G2300/205
Abstract: A zeolite fluid catalytic cracking catalyst is provided that passivates nickel and vanadium during catalytic cracking. The zeolite fluid catalytic cracking catalyst includes Y-faujasite crystallized in-situ from a metakaolin-containing calcined microsphere. The zeolite fluid catalytic cracking catalyst further includes an alumina-containing matrix obtained by calcination of a dispersible crystalline boehmite and a kaolin contained in the metakaolin-containing calcined microsphere, where the dispersible crystalline boehmite has a crystallite size of less than 500 Å. Also provided are a method of reducing contaminant coke and hydrogen yields and a method of catalytic cracking of heavy hydrocarbon feed stocks.
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公开(公告)号:US11224867B2
公开(公告)日:2022-01-18
申请号:US16605133
申请日:2018-05-15
Applicant: BASF Corporation
Inventor: Robert McGuire , Ahmad Moini , Ulrich Mueller
Abstract: A process for preparing a zeolitic material having framework type AEI and having a framework structure which comprises a tetravalent element Y, a trivalent element X, and oxygen, said process comprising (i) providing a zeolitic material having framework type CHA and having a framework structure comprising the tetravalent element Y, the trivalent element X, and oxygen; (ii) preparing a synthesis mixture comprising the zeolitic material provided in (i), water, a source of the tetravalent element Y other than the zeolitic material provided in (i), and an AEI framework structure directing agent; (ili) subjecting the synthesis mixture prepared in (ii) to hydrothermal synthesis conditions comprising heating the synthesis mixture to a temperature in the range of from 100 to 200° C. and keeping the synthesis mixture at a temperature in this range under autogenous pressure, obtaining the zeolitic material having framework type AEI; wherein Y is one or more of Si, Ge, Sn, Ti, Zr; wherein X is one or more of Al, B, Ga, In; wherein in the framework structure of the zeolitic material provided in (i), the molar ratio Y:X, calculated as YO2: X2O3, is at most 20:1 and, wherein; the process further comprises supporting a metal M selected from the transition metals of groups 7 to 12 of the periodic system of elements.
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公开(公告)号:US11878293B2
公开(公告)日:2024-01-23
申请号:US17274809
申请日:2019-09-10
Applicant: BASF Corporation
Inventor: Robert McGuire , Faruk Oezkirim , Ulrich Mueller
CPC classification number: B01J29/76 , B01D53/8628 , B01J35/1019 , C01B39/026 , C01B39/48 , B01D2255/20761 , B01D2255/50 , B01J2229/186 , C01P2002/72 , C01P2004/03 , C01P2006/12
Abstract: The present disclosure relates to a process for preparing a zeolitic material having framework type AEI and having a framework structure which comprises a tetravalent element Y, a trivalent element X, and O. Further, the present disclosure relates to a zeolitic material having framework type AEI and having a framework structure which comprises a tetravalent element Y, a trivalent element X, and O, preferably obtained by the process, and further relates to the use of the zeolitic material as a catalytically active material, as a catalyst, or as a catalyst component.
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公开(公告)号:US11254878B2
公开(公告)日:2022-02-22
申请号:US16824061
申请日:2020-03-19
Applicant: BASF Corporation
Inventor: Robert McGuire , Gary Smith , Bilge Yilmaz , Sven Serneels
Abstract: A zeolite fluid catalytic cracking catalyst is provided that passivates nickel and vanadium during catalytic cracking. The zeolite fluid catalytic cracking catalyst includes Y-faujasite crystallized in-situ from a metakaolin-containing calcined microsphere. The zeolite fluid catalytic cracking catalyst further includes an alumina-containing matrix obtained by calcination of a dispersible crystalline boehmite and a kaolin contained in the metakaolin-containing calcined microsphere, where the dispersible crystalline boehmite has a crystallite size of less than 500 Å. Also provided are a method of reducing contaminant coke and hydrogen yields and a method of catalytic cracking of heavy hydrocarbon feed stocks.
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公开(公告)号:US11148954B2
公开(公告)日:2021-10-19
申请号:US16605069
申请日:2018-05-15
Applicant: BASF Corporation
Inventor: Ahmad Moini , Robert McGuire , Ulrich Mueller
Abstract: A process for preparing a zeolitic material comprising a metal M, having framework type AEI, and having a framework structure which comprises a tetravalent element Y, a trivalent element X, and oxygen, said process comprising (i) providing a zeolitic material comprising the metal M, having a framework type other than AEI, and having a framework structure comprising the trivalent element X, and oxygen; (ii) preparing a synthesis mixture comprising the zeolitic material provided in (i), water, a source of the tetravalent element Y, and an AEI framework structure directing agent; (iii) subjecting the synthesis mixture prepared in (ii) to hydrothermal synthesis conditions comprising heating the synthesis mixture to a temperature in the range of from 100 to 200° C. and keeping the synthesis mixture at a temperature in this range under autogenous pressure, obtaining the zeolitic material having framework type AEI; wherein Y is one or more of Si, Ge, Sn, Ti, Zr; wherein X is one or more of Al, B, Ga, In; wherein M is a transition metal of groups 7 to 12 of the periodic table of elements.
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公开(公告)号:US20200224102A1
公开(公告)日:2020-07-16
申请号:US16824061
申请日:2020-03-19
Applicant: BASF Corporation
Inventor: Robert McGuire , Gary Smith , Bilge Yilmaz , Sven Serneels
Abstract: A zeolite fluid catalytic cracking catalyst is provided that passivates nickel and vanadium during catalytic cracking. The zeolite fluid catalytic cracking catalyst includes Y-faujasite crystallized in-situ from a metakaolin-containing calcined microsphere. The zeolite fluid catalytic cracking catalyst further includes an alumina-containing matrix obtained by calcination of a dispersible crystalline boehmite and a kaolin contained in the metakaolin-containing calcined microsphere, where the dispersible crystalline boehmite has a crystallite size of less than 500 Å. Also provided are a method of reducing contaminant coke and hydrogen yields and a method of catalytic cracking of heavy hydrocarbon feed stocks.
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公开(公告)号:US10137442B2
公开(公告)日:2018-11-27
申请号:US15604942
申请日:2017-05-25
Applicant: BASF CORPORATION
Inventor: Robert McGuire
IPC: B01J29/80 , B01J23/24 , B01J37/04 , B01J23/656 , B01J35/00 , C07C1/20 , C07C37/52 , C07C41/01 , C07C27/00 , B01J29/06 , C10G3/00 , C01B3/16 , B01J29/08 , B01J23/755 , B01J35/08 , B01J29/40 , B01J21/08 , B01J21/06 , B01J23/42 , B01J23/16 , B01J37/02 , B01J29/16 , B01J29/48 , B01J29/87
Abstract: A novel catalyst blend for processing of feedstocks into monoaromatics in a single stage, comprising at least one cracking catalyst, one heterogeneous transition metal catalyst, and optionally at least one hydrogenation catalyst. The process occurs in one-step or single stage with substantially no solvents or external additives, or when the feedstock contains less than 15% oxygen, the process includes additional water or steam to enable sufficient amounts of H2 being produced in-situ.
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公开(公告)号:US20170259252A1
公开(公告)日:2017-09-14
申请号:US15604942
申请日:2017-05-25
Applicant: BASF CORPORATION
Inventor: Robert McGuire
IPC: B01J29/80
CPC classification number: B01J29/80 , B01J21/06 , B01J21/08 , B01J23/16 , B01J23/24 , B01J23/42 , B01J23/6567 , B01J23/755 , B01J29/061 , B01J29/084 , B01J29/166 , B01J29/40 , B01J29/48 , B01J29/87 , B01J35/0006 , B01J35/08 , B01J37/0205 , B01J37/04 , B01J2229/42 , C01B3/16 , C07C1/20 , C07C27/00 , C07C37/52 , C07C41/01 , C07C2521/04 , C07C2523/28 , C07C2523/36 , C07C2523/42 , C07C2523/656 , C07C2523/755 , C07C2529/40 , C07C2529/80 , C10G3/49 , C10G2300/1014 , C10G2400/30 , Y02P20/52 , Y02P20/588 , Y02P30/20 , C07C43/23 , C07C39/08 , C07C15/08 , C07C15/02
Abstract: A novel catalyst blend for processing of feedstocks into monoaromatics in a single stage, comprising at least one cracking catalyst, one heterogeneous transition metal catalyst, and optionally at least one hydrogenation catalyst. The process occurs in one-step or single stage with substantially no solvents or external additives, or when the feedstock contains less than 15% oxygen, the process includes additional water or steam to enable sufficient amounts of H2 being produced in-situ.
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公开(公告)号:US09687829B2
公开(公告)日:2017-06-27
申请号:US14616028
申请日:2015-02-06
Applicant: BASF Corporation
Inventor: Robert McGuire
IPC: B01J23/00 , B01J20/18 , B01J21/00 , B01J29/80 , B01J23/656 , B01J35/00 , C07C1/20 , C07C37/52 , C07C41/01 , C07C27/00 , B01J37/04 , B01J29/06 , C10G3/00 , C01B3/16 , B01J29/08 , B01J23/755 , B01J35/08 , B01J29/40 , B01J21/08 , B01J21/06 , B01J23/24 , B01J23/42 , B01J23/16 , B01J37/02 , B01J29/16 , B01J29/48 , B01J29/87
CPC classification number: B01J29/80 , B01J21/06 , B01J21/08 , B01J23/16 , B01J23/24 , B01J23/42 , B01J23/6567 , B01J23/755 , B01J29/061 , B01J29/084 , B01J29/166 , B01J29/40 , B01J29/48 , B01J29/87 , B01J35/0006 , B01J35/08 , B01J37/0205 , B01J37/04 , B01J2229/42 , C01B3/16 , C07C1/20 , C07C27/00 , C07C37/52 , C07C41/01 , C07C2521/04 , C07C2523/28 , C07C2523/36 , C07C2523/42 , C07C2523/656 , C07C2523/755 , C07C2529/40 , C07C2529/80 , C10G3/49 , C10G2300/1014 , C10G2400/30 , Y02P20/52 , Y02P20/588 , Y02P30/20 , C07C43/23 , C07C39/08 , C07C15/08 , C07C15/02
Abstract: A novel catalyst blend for processing of feedstocks into monoaromatics in a single stage, comprising at least one cracking catalyst, one heterogeneous transition metal catalyst, and optionally at least one hydrogenation catalyst. The process occurs in one-step or single stage with substantially no solvents or external additives, or when the feedstock contains less than 15% oxygen, the process includes additional water or steam to enable sufficient amounts of H2 being produced in-situ.
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