US2014021094A1PendingUtilityA1
Method of removing heavy hydrocarbons
Est. expiryMar 31, 2031(~4.7 yrs left)· nominal 20-yr term from priority
C01B 2203/0233C01B 2203/0238C10G 5/04C10G 29/205C10G 7/02B01D 53/002C10G 21/14C01B 2203/0827C10G 25/003Y02P20/141B01D 2257/702B01D 53/1487C10G 2300/1022B01D 2256/24B01D 53/02C01B 3/384C01B 2203/062C10G 2/32
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Claims
Abstract
Heavy hydrocarbons contained in FT off gas of a GTL process are removed by bringing the FT off gas into contact with absorption oil, by introducing the FT off gas into a distillation tower, by cooling the FT off gas or by driving the FT off gas into an adsorbent. A burner tip for heating a reformer tube, using FT off gas as fuel, is prevented from being plugged by the deposition of heavy hydrocarbons contained in the FT off gas.
Claims
exact text as granted — not AI-modified1 . A method of producing various hydrocarbon oils from natural gas comprising:
a synthesis gas production step of producing synthesis gas containing hydrogen and carbon monoxide as main components by causing natural gas containing methane as main component to react with steam and/or carbon dioxide in a heated reformer tube filled with a reforming catalyst; a Fischer-Tropsch synthesis step of producing Fischer-Tropsch oil by subjecting the synthesis gas produced in the synthesis gas production step to a Fischer-Tropsch synthesis reaction and subsequently separating FT off gas containing gaseous products and unreacted synthesis gas; and an upgrading step of producing various hydrocarbon oils by subjecting the Fischer-Tropsch oil to a hydrotreating, hydroisomerization and hydrocracking process, wherein the FT off gas is recycled as a fuel for heating the reformer tube after heavy hydrocarbons contained in the FT off gas is removed.
2 . The method according to claim 1 , wherein the heavy hydrocarbons are hydrocarbons having five or more carbon atoms per molecule.
3 . The method according to claim 1 , wherein the heavy hydrocarbons are removed by bringing the FT off gas into contact with absorption oil directly.
4 . The method according to claim 3 , wherein the absorption oil is one of kerosene and gas oil.
5 . The method according to claim 1 , wherein the heavy hydrocarbons are removed by distilling the FT off gas.
6 . The method according to claim 1 , wherein the heavy hydrocarbons are removed by cooling the FT off gas.
7 . The method according to claim 1 , wherein the heavy hydrocarbons are removed from the FT off gas by adsorption.
8 . The method according to claim 7 , wherein an adsorbent used for the adsorption is active carbon.Join the waitlist — get patent alerts
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