Edward J. Demmel - Newport Beach CA Albert A. Vierheilig - Richmond Hill GA
Assignee:
Bulldog Technologies U.S.A., Inc. - Wilmington DE
International Classification:
C07C 258
US Classification:
585722
Abstract:
Zeolite/clay/phosphate catalysts can be prepared by a process wherein a composition of zeolite-clay-phosphate is brought to a pH level of about 7. 0 to about 14. The resulting slurry is then age reacted for about 0. 5 to about 24 hours. Thereafter the slurry is dried to produce a zeolite/clay/phosphate catalyst particles that are particularly characterized by their high levels of zeolite stability.
Louis M. Magnabosco - El Torro CA Edward J. Demmel - Newport Beach CA
Assignee:
Intercat, Inc. - Sea Girt NJ
International Classification:
B01J 2104 B01J 2110 B01J 2310 B01J 2322
US Classification:
502304
Abstract:
Spinels can be synthesized by uniformly dispersing predetermined quantities of ingredient compounds whose particles have sizes no greater than about 5 nanometers in a liquid medium, arresting the ingredient compounds in a solid matrix by spray drying said liquid medium and then calcining the resulting particles to form a solid solution of oxides of said compounds in a crystalline lattice which is substantially free of undesired complex compounds of the ingredient compounds.
Processes For Reacting Bastnaesite With Metal Oxides
Bastnaesite materials and Mg[A] (and/or Al[B]) materials can be chemically reacted by use of reactions wherein a Al[B] ingredient such as alumina is made into a sol by use of a mono-protonic acid before Mg[A] (and/or Al[B]) materials is (are) reacted with the bastnaesite material.
Processes For Using Bastnaesite/Metal Oxide Compounds
Bastnaesite materials and Mg A! (and/or Al B!) materials can be chemically reacted by use of reactions wherein a Al B! ingredient such as alumina is made into a sol by use of a mono-protonic acid before Mg A! (and/or Al B!) materials is (are) reacted with the bastnaesite material. The resulting compounds are then used as SO. sub. x catalyst/absorbent materials in fluid catalytic cracking units and/or in fixed bed units.
Processes For Reacting Bastnaesite With Alkaline-Earth Metals
Bastnaesite and magnesium-containing materials can be chemically reacted by use of reactions wherein alumina is made into a sol by use of a mono-protonic acid and then reacted with a magnesium-containing ingredient (e. g. , magnesium acetate) and a bastnaesite ingredient such that, upon spray drying and calcination of the resulting composition, the bastnaesite is chemically reacted with magnesia to form a bastnaesite/magnesia/alumina compound having SO. sub. x activity.
Edward J. Demmel - Newport Beach CA Albert A. Vierheilig - Richmond Hill GA
Assignee:
Bulldog Technologies U.S.A., Inc. - Wilmington DE
International Classification:
B01J 2906 B01J 2116 B01J 2904 B01J 2714
US Classification:
502 68
Abstract:
Zeolite/clay/phosphate catalysts can be prepared by a process wherein a composition of zeolite-clay-phosphate is brought to a pH level of about 7. 0 to about 14. The resulting slurry is then age reacted for about 0. 5 to about 24 hours. Thereafter the slurry is dried to produce a zeolite/clay/phosphate catalyst particles that are particularly characterized by their high levels of zeolite stability.
Method For Producing Attrition-Resistant Catalyst Binders
Attrition-resistant binders can be prepared by a process wherein a slurry of clay particles is brought to either a low pH level (e. g. , 1. 0 to 3. 0) or to a high pH level (e. g. , 14. 0 to 10. 0) and mixed with a phosphate-containing compound in a concentration of from about 2. 0 to about 20. 0 weight percent. Preferably, the resulting slurry is spray dried and the particulate products of the spray drying are then calcined to produce attrition-resistant binder particles.
Production Of Attrition-Resistant Catalyst Binders Through Use Of Delaminated Clay
Attrition-resistant binders can be prepared by a process wherein a slurry of delaminated and calcined clay particles is brought to either a low pH level (e. g. , 1. 0 to 3. 0) or to a high pH level (e. g. , 14. 0 to 10. 0) and mixed with a phosphate-containing compound in a concentration of from about 2. 0 to about 20. 0 weight percent. Preferably, the resulting slurry is spray dried and the particulate products of the spray drying are then calcined to produce attrition-resistant binder particles.
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