Method for producing liquid hydrocarbon fuels directly from lignocellulosic biomass
US-9487712-B2 · Nov 8, 2016 · US
US10335778B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10335778-B2 |
| Application number | US-201816043161-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 24, 2018 |
| Priority date | Nov 6, 2017 |
| Publication date | Jul 2, 2019 |
| Grant date | Jul 2, 2019 |
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Disclosed are a heteropolyacid catalyst for producing gamma-valerolactone, which is supported on M-Beta zeolite (M=Sn, Ti, Zr or Hf), and a method for preparing the same and a method for manufacturing gamma-valerolactone using the catalyst. The catalyst has an effect of producing gamma-valerolactone from biomass-derived furfural at a high yield through a one-pot process.
Opening claim text (preview).
What is claimed is: 1. A catalyst for producing gamma-valerolactone, comprising Beta zeolite substituted with a metal; and a heteropolyacid supported on the zeolite. 2. The catalyst for producing gamma-valerolactone according to claim 1 , wherein the metal is one or more selected from Group 4 consisting of titanium (Ti), zirconium (Zr), and hafnium (Hf). 3. The catalyst for producing gamma-valerolactone according to claim 1 , wherein the metal is tin (Sn). 4. The catalyst for producing gamma-valerolactone according to claim 1 , wherein the zeolite substituted with a metal is prepared by a method including removing aluminum from Al-Beta zeolite and mixing the dealuminated Si-Beta zeolite with a metal precursor and then performing a heat treatment to substitute the zeolite skeleton with a metal. 5. The catalyst for producing gamma-valerolactone according to claim 1 , wherein the catalyst is for producing gamma-valerolactone from furfural. 6. The catalyst for producing gamma-valerolactone according to claim 1 , wherein a content of the metal is 1 to 10 wt % based on a total weight of the catalyst. 7. The catalyst for producing gamma-valerolactone according to claim 1 , wherein the heteropolyacid has a formula H n XM 12 O 40 where X is a center element of phosphorus (P), silicon (Si), germanium (Ge) or arsenic (As), M is a coordinating element including tungsten (W) or molybdenum (Mo), and n is an integer more than 0. 8. The catalyst for producing gamma-valerolactone according to claim 7 , wherein the heteropolyacid is one or more selected from the group consisting of 12-tungstophosphoric acid (H 3 PW 12 O 40 ), 12-tungstosilicic acid (H 4 SiW 12 O 40 ), 12-molybdophosphoric acid (H 3 PMo 12 O 40 ), and 12-molybdosilicic acid (H 4 SiMo 12 O 40 ). 9. The catalyst for producing gamma-valerolactone according to claim 1 , wherein the heteropolyacid is supported in an amount of 1 to 10 parts by weight based on 100 parts by weight of a total weight of zeolite. 10. A method for preparing the catalyst for producing gamma-valerolactone according to claim 1 , the method comprising: impregnating Beta zeolite substituted with a metal with a heteropolyacid solution; and calcining the impregnated catalyst. 11. The method for preparing the catalyst for producing gamma-valerolactone according to claim 10 , wherein a solvent of the heteropolyacid solution is an alcohol solvent having 1 to 6 carbon atoms. 12. The method for preparing the catalyst for producing gamma-valerolactone according to claim 10 , wherein the impregnating method is an incipient wetness impregnation in which a heteropolyacid solution in an amount corresponding to a pore volume of zeolite is gradually added to and supported on the zeolite. 13. The method for preparing the catalyst for producing gamma-valerolactone according to claim 10 , wherein a calcination temperature is 100° C. to 400° C. 14. A method for manufacturing gamma-valerolactone, the method comprising: conducting a reaction for producing gamma-valerolactone using the catalyst for producing gamma-valerolactone according to claim 1 . 15. The method for manufacturing gamma-valerolactone according to claim 14 , wherein the reaction for producing gamma-valerolactone is conducted by mixing furfural and an alcohol solvent with the catalyst. 16. The method for manufacturing gamma-valerolactone according to claim 14 , wherein the reaction for producing gamma-valerolactone is conducted at 120° C. to 180° C. 17. The method for manufacturing gamma-valerolactone according to claim 14 , wherein the reaction for producing gamma-valerolactone is conducted for 6 to 48 hours.
with chromium, molybdenum, tungsten or polonium · CPC title
in framework positions · CPC title
in position 2, the oxygen atom being in its keto or unsubstituted enol form · CPC title
Zeolite Beta · CPC title
Impregnation · CPC title
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