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1. 发明申请

WO1991000843A1 ZEOLITE SSZ-33 审中-公开
公开(公告)号：WO1991000843A1
公开(公告)日：1991-01-24
申请号：PCT/US1990002316
申请日：1990-04-26
申请人： CHEVRON RESEARCH COMPANY
发明人： CHEVRON RESEARCH COMPANY , ZONES, Stacey, I. , HOLTERMANN, Dennis, L. , SANTILLI, Donald, S. , JOSSENS, Lawrence, W. , KENNEDY, James, V. , RAINIS, Andrew
IPC分类号： C01B33/00
CPC分类号： B01J29/74 , B01J29/04 , B01J29/70 , B01J29/7049 , B01J2229/26 , B01J2229/36 , B01J2229/42 , C01B39/12
摘要： A crystalline zeolite SSZ-33 is prepared using a quaternary ion as a template.

2. 发明申请

WO1990004567A1 NEW ZEOLITE SSZ-31 审中-公开
标题翻译：新ZEOLITE SSZ-31
公开(公告)号：WO1990004567A1
公开(公告)日：1990-05-03
申请号：PCT/US1989004638
申请日：1989-10-17
申请人： CHEVRON RESEARCH COMPANY
发明人： CHEVRON RESEARCH COMPANY , ZONES, Stacey, I. , HARRIS, Thomas, V. , RAINIS, Andrew , SANTILLI, Donald, S.
IPC分类号： C01B33/34
CPC分类号： C10G35/095 , B01J29/04 , B01J29/70 , B01J2229/26 , B01J2229/36 , B01J2229/42 , C01B33/185 , C01B39/48 , C01P2002/72 , C01P2002/74 , C07C4/06 , C07C211/38 , C07C211/62 , C07C2529/70 , C07C2603/66 , C10G11/05 , C10G47/16
摘要： A crystalline zeolite SSZ-31 is prepared using a tricyclodecane quaternary ammonium ion as a template.
摘要翻译：使用三环癸烷季铵离子作为模板制备结晶沸石SSZ-31。

3. 发明公开

EP0394434A1 NEW ZEOLITE SSZ-31 失效
标题翻译： ZEOLITH SSZ-31。
公开(公告)号：EP0394434A1
公开(公告)日：1990-10-31
申请号：EP89912717.0
申请日：1989-10-17
申请人： CHEVRON RESEARCH COMPANY
发明人： ZONES, Stacey, I. , HARRIS, Thomas, V. , RAINIS, Andrew , SANTILLI, Donald, S.
IPC分类号： B01J29 , C01B37 , C01B39 , C07C4 , C07C211 , C10G11 , C10G35 , C10G47
CPC分类号： C10G35/095 , B01J29/04 , B01J29/70 , B01J2229/26 , B01J2229/36 , B01J2229/42 , C01B33/185 , C01B39/48 , C01P2002/72 , C01P2002/74 , C07C4/06 , C07C211/38 , C07C211/62 , C07C2529/70 , C07C2603/66 , C10G11/05 , C10G47/16
摘要： A zeolite cristallin SSZ-31 est préparé en utilisant un ion ammonium quaternaire de tricyclodécane en tant que gabarit.
摘要翻译：使用三环癸烷季铵离子作为模板制备结晶沸石SSZ-31。

4. 发明公开

EP0277117A1 PROCESS FOR THE MANUFACTURE OF SHPERICAL BODIES BY SELECTIVE AGGLOMERATION 失效
标题翻译：用于生产球体通过选择性卫星城。
公开(公告)号：EP0277117A1
公开(公告)日：1988-08-10
申请号：EP86904615.0
申请日：1986-07-02
申请人： CHEVRON RESEARCH COMPANY
发明人： RAINIS, Andrew
IPC分类号： B01J37
CPC分类号： B01J37/0009
摘要： Preparation of small substantially spherical solid catalysts. More particularly, the process produces strong solid substantially spherical agglomerates comprising inorganic materials, which process comprises: (a) mixing at high speed a portion of an inorganic material in the form of hydrophilic micron-sized particles in a water-immiscible liquid thereby forming a dispersion; (b) gradually adding to the dispersion an aqueous phase while continuing the high speed mixing until substantially spherical microagglomerates form within the water-immiscible liquid; (c) subjecting the microagglomerates to agitation in a vessel having a hydrophobic inner surface at a speed low enough to achieve substantially uniformly sized spherical agglomerates; (d) drying the agglomerates to produce hardened substantially spherical uniformly sized agglomerates; and (e) optionally further separating the agglomerates by size. Optionally, the aqueous phase in step (b) may include the soluble salts of catalytic metals, acids and bases and/or colloidal-sized inorganic particles. These spherical particles have diameters generally between 1 to 5 millimeters and are useful as catalysts, or catalyst supports, where the catalytic components are subsequently deposited on the support.

5. 发明授权

EP0277117B1 PROCESS FOR THE MANUFACTURE OF SHPERICAL BODIES BY SELECTIVE AGGLOMERATION 失效
标题翻译：通过选择性组合制造精密体的方法
公开(公告)号：EP0277117B1
公开(公告)日：1990-04-11
申请号：EP86904615.1
申请日：1986-07-02
申请人： CHEVRON RESEARCH COMPANY
发明人： RAINIS, Andrew
IPC分类号： B01J35/08
CPC分类号： B01J37/0009
摘要： Preparation of small substantially spherical solid catalysts. More particularly, the process produces strong solid substantially spherical agglomerates comprising inorganic materials, which process comprises: (a) mixing at high speed a portion of an inorganic material in the form of hydrophilic micron-sized particles in a water-immiscible liquid thereby forming a dispersion; (b) gradually adding to the dispersion an aqueous phase while continuing the high speed mixing until substantially spherical microagglomerates form within the water-immiscible liquid; (c) subjecting the microagglomerates to agitation in a vessel having a hydrophobic inner surface at a speed low enough to achieve substantially uniformly sized spherical agglomerates; (d) drying the agglomerates to produce hardened substantially spherical uniformly sized agglomerates; and (e) optionally further separating the agglomerates by size. Optionally, the aqueous phase in step (b) may include the soluble salts of catalytic metals, acids and bases and/or colloidal-sized inorganic particles. These spherical particles have diameters generally between 1 to 5 millimeters and are useful as catalysts, or catalyst supports, where the catalytic components are subsequently deposited on the support.

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