US2014230318A1PendingUtilityA1
In-Situ Upgrading Of Biomass Pyrolysis Vapor By Cracking And Hydroprocessing
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
47
PatentIndex Score
0
Cited by
0
References
0
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-modifiedWhat 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.Cited by (0)
No later patents cite this yet.
References (0)
No backward citations on record.