High Nanopore Volume Catalyst And Process Using SSZ-91
US-2024058802-A1 · Feb 22, 2024 · US
US9758734B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9758734-B2 |
| Application number | US-201414202127-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 10, 2014 |
| Priority date | Mar 13, 2013 |
| Publication date | Sep 12, 2017 |
| Grant date | Sep 12, 2017 |
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The hydroisomerization of a paraffinic hydrocarbon feedstock obtained from renewable sources is effectively achieved by passing the feedstock in the presence of hydrogen over a hydroisomerization catalyst comprising a crystalline metal silicate molecular sieve, in which a portion of the crystalline framework contains iron.
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The invention claimed is: 1. A process for hydroisomerization of a paraffinic hydrocarbon feedstream, the process comprising: contacting said hydrocarbon feedstream with hydrogen and a catalyst comprising a crystalline metal silicate molecular sieve having a crystalline framework, wherein the crystalline framework comprises aluminum located at aluminum sites, wherein at least a portion of the aluminum sites are isomorphously-substituted with iron, and yielding a product having an increase in branched hydrocarbons relative to said hydrocarbon feedstream, wherein the metal silicate molecular sieve is ZSM-12, ZSM-22, ZSM-23, ZSM-48, ZSM-57, or MCM-22, wherein the catalyst further contains from 0.01 to 10 wt. % of a platinum group metal and wherein said metal silicate molecular sieve has a molar framework formula [X a X 1 1-a ] 2 O 3 :(y)YO 2 wherein X is iron, X 1 is aluminum, a is at least 0.90; Y is silicon; and y is from about 20 to about 300. 2. The process of claim 1 , wherein said molecular sieve has a pore size of about 3 to 10 angstroms. 3. The process of claim 1 , wherein said platinum group metal is platinum. 4. The process of claim 1 , wherein said paraffinic hydrocarbon feedstream comprises nC 8+ hydrocarbons. 5. The process of claim 4 , wherein said paraffinic hydrocarbon feedstream is obtained from the deoxygenation of a non-petroleum feedstock originating from one of plants or animals. 6. The process of claim 5 , wherein said non-petroleum feedstock comprises glycerides and free fatty acids. 7. The process of claim 6 , wherein said non-petroleum feedstock comprises palm oil. 8. The process of claim 1 , wherein said molecular sieve in as synthesized form has a formula on an anhydrous basis of (0.05 to 1.0)M 2 O:(0 to 75)R:Z 2 O 3 :( y )YO 2 wherein M is an alkali metal cation, R is a specific organic directing agent and Z is a mixture of X and X′. 9. The process of claim 1 , wherein said product has a cloud point ranging from 0 to −65° C. 10. The process of claim 9 , wherein said product is a diesel fuel having a cloud point ranging from −10 to −50° C. 11. The process of claim 9 , wherein said product is a biojet fuel having a cloud point ranging from −25 to −65° C. 12. The process of claim 1 , wherein said catalyst is not treated with a passivator. 13. The process of claim 1 , wherein said catalyst further contains a base metal promoter. 14. The process of claim 13 , wherein said base metal promoter is nickel. 15. The process of claim 1 , wherein a majority of said platinum group metal is contained on said molecular sieve and said catalyst is mixed with a matrix material.
using bio-feedstock · CPC title
Jet fuel · CPC title
containing crystalline alumino-silicates, e.g. molecular sieves · CPC title
Iron group metals or copper · CPC title
TON-type, e.g. Theta-1, ISI-1, KZ-2, NU-10 or ZSM-22 · CPC title
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