Collection enhanced materials, down stream additives, and methods of making the enhanced materials and down stream additives are provided. In one embodiment, a down stream additive is provided that includes an active phase component and at least one of a collection enhancing component. In other embodiments, the down stream additive may have attrition index from about two (2) to about ten (10) and/or an average diameter from about 20 µm to about 60 µm. In other embodiments, the down stream additive may have an active phase component which is incompatible with a process performed in an FCC unit. In yet another embodiment, a collection enhanced material having an average diameter from about 60 µm to about 300 µm is provided that includes an active component and a collection enhancing component.
B03C 3/00 - Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
2.
CRACKING CATALYST, ADDITIVES, METHODS OF MAKING THEM AND USING THEM
Collection enhanced materials, down stream additives, and methods of making the enhanced materials and down stream additives are provided. In one embodiment, a down stream additive is provided that includes an active phase component and at least one of a collection enhancing component. In other embodiments, the down stream additive may have attrition index from about two (2) to about ten (10) and/or an average diameter from about 20 µm to about 60 µm. In other embodiments, the down stream additive may have an active phase component which is incompatible with a process performed in an FCC unit. In yet another embodiment, a collection enhanced material having an average diameter from about 60 µm to about 300 µm is provided that includes an active component and a collection enhancing component.
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
3.
CRACKING CATALYST, ADDITIVES, METHODS OF MAKING THEM AND USING THEM
Collection enhanced materials, down stream additives, and methods of making the enhanced materials and down stream additives are provided. In one embodiment, a down stream additive is provided that includes an active phase component and at least one of a collection enhancing component. In other embodiments, the down stream additive may have attrition index from about two (2) to about ten (10) and/or an average diameter from about 20 µm to about 60 µm. In other embodiments, the down stream additive may have an active phase component which is incompatible with a process performed in an FCC unit. In yet another embodiment, a collection enhanced material having an average diameter from about 60 µm to about 300 µm is provided that includes an active component and a collection enhancing component.
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
4.
COMPOSITION AND METHODS FOR PREFERENTIALLY INCREASING YIELDS OF ONE OR MORE SELECTED HYDROCARBON PRODUCTS
Methods and compositions to preferentially increase or decrease the yield of at least a selected hydrocarbon product in one or more fluidized units are provided. An embodiment includes: providing a high activity component to a fluidized unit as physically separate and distinct particles in an amount sufficient to preferentially increase the yield of at least a selected hydrocarbon product compared to another hydrocarbon product. Another embodiment includes: providing a high activity component to a fluidized unit as physically separate and distinct particles to preferentially decrease the yield of at least a selected hydrocarbon product compared to another hydrocarbon product. Another method includes: providing at least a high activity component comprising a contaminant inhibitor component to a fluidized unit as physically separate and distinct particles to inhibit the adverse effects of at least a contaminant in a feed stock.
C10G 11/18 - Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised bed" technique
5.
SULFUR OXIDE REMOVING ADDITIVES AND METHODS FOR PARTIAL OXIDATION CONDITIONS
The sulfur oxide removing additive suitable for a FCC unit at low oxygen environment condition is described. The SOx removing additive includes one or more sorbents and one or more oxidation catalysts. The sorbent includes a source of Al and a divalent component. The divalent component is selected from a group consisting of magnesium, calcium, and combinations of two or more. The oxidation catalyst includes a source of cerium. The SOx removing additive is substantially free of vanadium. Also described is a method of removing the sulfur oxide content of a sulfur oxide-containing gas from an FCC unit. The method includes contacting the gas with a SOx removing additive at a low oxygen environment condition.
The sulfur oxide removing additive suitable for a FCC unit at low oxygen environment condition is described. The SOx removing additive includes one or more sorbents and one or more oxidation catalysts. The sorbent includes a source of Al and a divalent component. The divalent component is selected from a group consisting of magnesium, calcium, and combinations of two or more. The oxidation catalyst includes a source of cerium. The SOx removing additive is substantially free of vanadium. Also described is a method of removing the sulfur oxide content of a sulfur oxide-containing gas from an FCC unit. The method includes contacting the gas with a SOx removing additive at a low oxygen environment condition.
The present invention is directed to methods for reducing SOx, NOx, and CO emissions from a fluid stream comprising contacting said fluid stream with a compound comprising magnesium and aluminum and having an X-ray diffraction pattern displaying at least a reflection at a two theta peak position at about 43 degrees and about 62 degrees, wherein the ratio of magnesium to aluminum in the compound is from about 1:1 to about 10:1. In one embodiment, the ratio of magnesium to aluminum in the compound is from about 1:1 to about 6:1. In one embodiment, the ratio of magnesium to aluminum in the compound is from about 1.5:1 to about 10:1. In another embodiment, the invention is directed to methods wherein the ratio of magnesium to aluminum in the compound is from about 1.5:1 to about 6:1.
B01J 8/18 - Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
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