US2014230318A1PendingUtilityA1

In-Situ Upgrading Of Biomass Pyrolysis Vapor By Cracking And Hydroprocessing

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Assignee: LIU YUNQUANPriority: Feb 21, 2013Filed: Feb 21, 2013Published: Aug 21, 2014
Est. expiryFeb 21, 2033(~6.6 yrs left)· nominal 20-yr term from priority
C10L 1/06C10G 2400/02C10G 3/42C10G 3/50C10G 3/46C10G 67/02C10G 3/48Y02P30/20C10G 2400/04C10L 1/1802
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Claims

Abstract

Processes for thermal conversion of biomass are provided. The processes involve upgrading the pyrolysis vapor from a pyrolysis reactor. The steps include thermally converting a biomass feedstock in a pyrolysis reactor, recovering a pyrolysis vapor from the reactor, passing the pyrolysis vapor in contact with a cracking catalyst, a water-gas shift reaction catalyst, and a hydrotreating catalyst, and converting the resulting upgraded pyrolysis vapor into a liquid product. The resulting biooil liquid product is more refined, and the overall processes offer economic and energy efficiency.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A process for the thermal conversion of biomass comprising the steps of:
 a) thermal conversion of a biomass feedstock in a pyrolysis reactor;   b) recovering a pyrolysis vapor from the reactor;   c) passing the pyrolysis vapor in contact with a cracking catalyst, a water-gas shift reaction catalyst, and a hydrotreating catalyst to produce an upgraded pyrolysis vapor; and   d) converting the upgraded pyrolysis vapor from step c) into a liquid product.   
     
     
         2 . The process of  claim 1 , wherein the catalysts in step c) are layered in a single reactor. 
     
     
         3 . The process of  claim 2 , wherein the catalysts are layered so that the pyrolysis vapor contacts the cracking catalyst first, the water-gas shift reaction catalyst second, and the hydrotreating catalyst third. 
     
     
         4 . The process of  claim 2 , wherein the catalysts are layered so that the pyrolysis vapor contacts the water-gas shift reaction catalyst first, the hydrotreating catalyst second, and the cracking catalyst last. 
     
     
         5 . The process of  claim 2 , wherein the reaction temperature is controlled for each catalyst layer in order to promote the corresponding reaction. 
     
     
         6 . The process of  claim 5 , wherein the temperature is changed for each catalyst layer. 
     
     
         7 . The process of  claim 1 , wherein the cracking catalyst comprises a zeolite, the water-gas shift reaction catalyst comprises a transaction metal or transaction metal oxide, and the hydrotreating catalyst comprises a noble metal catalyst, nickel molybdenum catalyst, or cobalt molybdenum catalyst. 
     
     
         8 . The process of  claim 2 , wherein hydrogen produced in the water-gas shift reaction is used in the hydrotreating catalyst. 
     
     
         9 . The process of  claim 1 , wherein the catalysts in step c) are contacted with the pyrolysis vapor in separate reactors connected in series. 
     
     
         10 . The process of  claim 9 , wherein the pyrolysis vapor contacts a guard bed before at least one of the reactors. 
     
     
         11 . The process of  claim 9 , wherein the temperature and pressure is controlled for each of the reactors. 
     
     
         12 . The process of  claim 11 , wherein at least the temperature is different for each reactor. 
     
     
         13 . The process of  claim 9 , wherein hydrogen produced in the water-gas shift reactor is used in the reactor with the hydrotreating catalyst. 
     
     
         14 . The process of  claim 9 , wherein the pyrolysis vapor contacts the cracking catalyst first, the water-gas shift reaction catalyst second, and the hydrotreating catalyst third. 
     
     
         15 . The process of  claim 9 , wherein the pyrolysis vapor contacts the water-gas shift reaction catalyst first, the hydrotreating catalyst second, and the cracking catalyst last. 
     
     
         16 . The process of  claim 1 , further comprising combining the liquid product directly with crude oil to make a gasoline product. 
     
     
         17 . The process of  claim 2 , further comprising combining the liquid product directly with crude oil to make a gasoline product. 
     
     
         18 . The process of  claim 9 , further comprising combining the liquid product directly with crude oil to make a gasoline product.

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