Renewable olefins from a mixture of acetic acid and propionic acid
US-9212106-B2 · Dec 15, 2015 · US
US9211525B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9211525-B2 |
| Application number | US-200913055639-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 30, 2009 |
| Priority date | Jul 30, 2008 |
| Publication date | Dec 15, 2015 |
| Grant date | Dec 15, 2015 |
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Compositions and processed for their use as additives for reducing the sulfur content of FCC gasoline employ a support material having deposited on its surface (a) a first metal component from Group IIB of the Periodic Table and (b) a second metal component from Group III or Group IV of the Periodic Table. The additive composition is preferably made of a montmorillonite clay support containing zinc and gallium, zinc and zirconium. Alternatively, the additive composition includes support material having deposited on its surface a metal component from Group III of the Periodic Table, preferably a montmorillonite clay support containing gallium. The clay is impregnated with the metal(s) using the known incipient wetness method and the dried powdered additive composition is preferably formed into shapes suitable for use in the FCC unit.
Opening claim text (preview).
We claim: 1. A sulfur reduction additive composition for use a hydrocarbon cracking process, the additive composition comprising a montmorillonite clay support material having deposited on its surface a metal component from Group IIIA of the Periodic Table and a hydrocarbon cracking catalyst. 2. The additive composition according to claim 1 , wherein the metal component is impregnated on the surface of the support material by the incipient wetness method. 3. The additive composition according to claim 1 , wherein said metal component from Group IIIA of the Periodic Table is Ga. 4. The additive according to claim 3 , wherein the sulfur reduction additive contains from about 1 to about 5 weight percent of gallium based on the total weight of the additive. 5. The additive according to claim 1 , wherein the concentration of the sulfur reduction additive is from about 5 to about 20 weight percent of the hydrocarbon cracking catalyst. 6. The additive according to claim 1 , wherein the concentration of the sulfur reduction additive is from about 8 to about 15 weight percent of the hydrocarbon cracking catalyst. 7. A process for reducing the sulfur content of a gasoline fraction obtained from a fluid catalytic cracking process which comprises contacting a hydrocarbon feedstock with a hydrocarbon cracking catalyst in combination with a sulfur reduction additive composition, said additive composition comprising a montmorillonite clay support material having deposited on its surface a metal component from Group IIIA of the Periodic Table. 8. The process according to claim 7 , wherein the Ga is impregnated on the surface of the support material by the incipient wetness method. 9. The processing according to claim 7 , wherein the metal component from Group IIIA of the Periodic Table is Ga. 10. The process according to claim 9 , wherein the sulfur reduction additive composition contains from about 1 to about 5 weight percent of gallium based on the total weight of the additive composition. 11. The process according to claim 7 , wherein the concentration of the sulfur reduction additive composition is from about 5 to about 20 weight percent of the cracking catalyst. 12. The process according to claim 7 , wherein the concentration of the sulfur reduction additive composition is from about 8 to about 15 weight percent of the cracking catalyst.
of zinc, cadmium or mercury · CPC title
Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C · CPC title
Impregnation · CPC title
characterised by the catalyst used · CPC title
Clays or other mineral silicates · CPC title
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