Johann W. A. Sachtler - Des Plaines IL Randy J. Lawson - Palatine IL Susan L. Lambert - Rolling Meadows IL
Assignee:
UOP - Des Plaines IL
International Classification:
B01J 2928
US Classification:
502 61
Abstract:
This invention presents a novel catalyst formulation for the isomerization of alkylaromatic hydrocarbons. The catalyst comprises at least one Group VIII metal, a pentasil zeolite wherein a portion of the aluminum atom has been replaced with gallium atoms and a matrix material of zirconia-alumina. When utilized in a process for isomerizing a non-equilibrium mixture of xylenes containing ethylbenzene, a greater yield of para-xylene is obtained compared to prior art processes.
Hydrocarbon Conversion Processes Using Novel Crystalline Silicon Enhanced Aluminas
This invention relates to novel silicon enhanced aluminas (SEAL), processes to prepare them, and hydrocarbon conversion processes using the SEALs. The SEAL compositions have a bulk empirical formula of Al. sub. 2-x Si. sub. x O. sub. 3 F. sub. x where x varies from about 0. 01 to about 0. 5. This SEAL material has a three-dimensional pore structure with the pores having diameters in the range of about 20 to about 300. ANG. , a crystal structure characteristic of alumina, and where the surface of the SEAL has a higher silicon concentration than the interior of the SEAL. The SEAL is prepared by contacting an alumina with a fluorosilicate salt. This SEAL can be calcined to give a calcined seal with a formula Al. sub. 2-x Si. sub. x O. sub. 3 F. sub. y where x is as defined above and y varies from 0. 01 to x. The calcined SEAL contains both strong and weak acid sites.
This invention relates to novel silicon enhanced aluminas (SEAL) and processes to prepare them. The SEAL compositions have a bulk empirical formula of Al. sub. 2-x Si. sub. x O. sub. 3 F. sub. x where x varies from about 0. 01 to about 0. 5. This SEAL material has a three-dimensional pore structure with the pores having diameters in the range of about 20 to about 300. ANG. , a crystal structure characteristic of alumina, and where the surface of the SEAL has a higher silicon concentration than the interior of the SEAL. The SEAL is prepared by contacting an alumina with a fluorosilicate salt. This SEAL can be calcined to give a calcined seal with a formula Al. sub. 2-x Si. sub. x O. sub. 3 F. sub. y where x is as defined above and y varies from 0. 01 to x. The calcined SEAL contains both strong and weak acid sites.
Hydrocarbon Conversion Process Using Pillared Clay And A Silica-Substituted Alumina
Hydrocarbons are reduced in molecular weight in a conversion process wherein they are contacted with a solid catalyst comprising (i) a pillared clay and (ii) an alumina, such as gamma alumina, which has been isomorphously substituted with silicon. The treated alumina will have a silicon to fluorine mole ratio of about 1. 0:1. 0 to about 50. 0:1. The process may comprise the fluidized catalytic cracking of cycle oils. For use in hydrocracking, the catalyst contains a metal hydrogenation component and possibly one or more other inorganic oxides such as silica-alumina. Other non-zeolitic materials such as silica-alumina may also be composited into the catalysts.
Zirconium Silicate Composition, Method Of Preparation And Uses Thereof
This invention relates to a novel zirconium silicate compound which has the formula M. sub. x Si. sub. y Zr. sub. z O. sub. w where M is an ammonium ion, a hydronium ion, an alkali metal or mixtures thereof and x, y, z and w are the mole fractions of M, silicon, zirconium and oxygen respectively. The composition is characterized in that it has a unique x-ray powder diffraction pattern, has a surface area from about 80 to about 400 and has a layered structure. These compositions are prepared by hydrothermal crystallization of a reaction mixture containing reactive sources of the alkali metal, silicon, zirconium and water. Finally, these compositions may be used in various hydrocarbon conversion processes.
Hydrocarbon Conversion Process Using A Novel Silicon Enhanced Amorphous Silica-Alumina
Susan L. Lambert - Rolling Meadows IL Michael W. Schoonover - Arlington Heights IL
Assignee:
UOP - Des Plaines IL
International Classification:
C10G 1108 C10G 4708 C07C 270
US Classification:
208111
Abstract:
This invention relates to a hydrocarbon conversion processes, e. g. , hydrocracking, cracking, alkylation, etc. , using a silicon enhanced amorphous silica-alumina (SEASAL) composition. The composition is characterized in that from about 3 to about 22 mole percent of the aluminum atoms in a host amorphous silica-alumina have been replaced by silicon atoms. Additionally, the SEASAL contains from about 0. 5 to about 10 weight percent fluoride and has a cracking activity of at least 30%. The SEASAL is prepared by reacting a host amorphous silica-alumina with a fluorosilicate salt, thereby removing aluminum atoms and inserting silicon atoms.
Hydrocarbon Conversion Process Using Novel Silica-Substituted Aluminas
Hydrocarbons are reduced in molecular weight in a conversion process wherein they are contacted with a non-zeolitic solid catalyst comprising an alumina, such as gamma alumina, which has been isomorphously substituted with silicon. The treated alumina will have a fluorine to silicon mole ratio of about 0. 8:1 to about 1. 3:1. For use in hydrocracking, the catalyst contains a metal hydrogenation component and possibly one or more other inorganic oxides such as silica-alumina. Other non-zeolitic materials such as delaminated clay or silica-alumina may also be composited into the catalysts.
J. W. Adriaan Sachtler - Des Plaines IL R. Joe Lawson - Palatine IL Susan L. Lambert - Rolling Meadows IL
Assignee:
UOP - Des Plaines IL
International Classification:
C07C 522
US Classification:
585 481
Abstract:
This invention presents a process for isomerizing a non-equilibrium mixture of xylenes containing ethylbenzene, using a novel catalyst formulation comprising at least one Group VIII metal, a gallium-substituted pentasil zeolite and a matrix material of zirconia-alumina.
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