US2012323056A1PendingUtilityA1
Catalyst for producing hydrogenated biodiesel and method of producing the same
Est. expiryFeb 11, 2030(~3.6 yrs left)· nominal 20-yr term from priority
B01J 23/883B01J 37/0201Y02P30/20B01J 23/30B01J 23/34B01J 23/44C10L 2290/06B01J 23/885C10L 1/08B01J 23/882B01J 23/745B01J 23/462B01J 23/28B01J 23/755B01J 23/468B01J 38/18B01J 23/888C10G 3/46C11C 3/126B01J 21/066B01J 23/8877B01J 21/063B01J 23/42C10G 3/44C10L 2200/0469B01J 23/75C10G 3/50C10L 1/026Y02E50/10
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Claims
Abstract
Disclosed herein is a catalyst for producing biodiesel, including a carrier having water resistance and an active component supported on the carrier and used in a hydrotreating reaction or a decarboxylation reaction. Since the catalyst for producing biodiesel includes a carrier having strong water resistance, the deactivation of the catalyst due to the water produced through a process of producing HBD can be prevented, thus remarkably improving the long term stability of a catalyst.
Claims
exact text as granted — not AI-modified1 . A catalyst for producing biodiesel, comprising a carrier having water resistance and an active component supported on the carrier and used in a hydrotreating reaction or a decarboxylation reaction.
2 . The catalyst for producing biodiesel according to claim 1 , wherein the catalyst comprises a group VIB metal as the active component supported on the carrier.
3 . The catalyst for producing biodiesel according to claim 2 , wherein the catalyst further comprises a group VIIB metal or a group VIII metal as the active component supported on the carrier.
4 . The catalyst for producing biodiesel according to claim 1 , wherein the carrier is selected from among zirconia, titania, aluminum phosphate, niobia, zirconium phosphate, titanium phosphate, silicon carbide, carbon and mixtures thereof.
5 . The catalyst for producing biodiesel according to claim 2 , wherein the group VIB metal is Mo or W, and the amount thereof is 0.1˜70 wt % among total active agent.
6 . The catalyst for producing biodiesel according to claim 3 , wherein the group VIII metal is Ni, Pd or Pt, and the amount thereof is 0˜60 wt % among total active agent.
7 . The catalyst for producing biodiesel according to claim 3 , wherein the group VIIB metal is Co, Ru, Fe, Mn or Ir, and the amount thereof is 0˜60 wt % among total active agent.
8 . The catalyst for producing biodiesel according to claim 2 , wherein the group VIB metal is present in an amount of 1˜40 wt % based on the carrier.
9 . The catalyst for producing biodiesel according to claim 3 , wherein the group VIII metal or group VIIB metal is present in an amount of 0˜20 wt % based on the carrier.
10 . A method of producing biodiesel through a hydrotreating reaction or a decarboxylation reaction in the presence of the catalyst of claim 1 .
11 . The method of producing biodiesel according to claim 10 , wherein biomass, such as plant oil, plant fat, animal fat, fish oil, recycled fat, plant fatty acids, animal fatty acids or mixtures thereof, is used as a feed.
12 . The method of producing biodiesel according to claim 11 , wherein the plant fat, animal fat or recycled fat includes triglycerides, each chain of which is composed of 1˜28 carbon atoms, and each of the plant fatty acids or animal fatty acids has 1˜28 carbon atoms.
13 . The method of producing biodiesel according to claim 11 , wherein, in addition to the biomass, one or more hydrocarbon mixtures (0-99%) are used as the feed.
14 . The method of producing biodiesel according to claim 13 , wherein the hydrocarbon includes kerosene, diesel, light gas oil (LGO), and recycled HBD.
15 . The method of producing biodiesel according to claim 10 , the method comprises the steps of: pretreating a feed through hydrotreatment; separating unreacted hydrogen after a hydrodeoxygenation reaction to form hydrocarbons; and cooling, separating and isomerizing the formed hydrocarbons.
16 . Biodiesel produced by the method of claim 10 .Cited by (0)
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