UA98660C2 - Hydrocarbon synthesis process - Google Patents

Hydrocarbon synthesis process

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Publication number
UA98660C2
UA98660C2 UAA201002000A UAA201002000A UA98660C2 UA 98660 C2 UA98660 C2 UA 98660C2 UA A201002000 A UAA201002000 A UA A201002000A UA A201002000 A UAA201002000 A UA A201002000A UA 98660 C2 UA98660 C2 UA 98660C2
Authority
UA
Ukraine
Prior art keywords
iron
catalyst
fischer tropsch
hand
reducing gas
Prior art date
Application number
UAA201002000A
Other languages
Russian (ru)
Ukrainian (uk)
Inventor
Йоганнес Якобус Хайзер
ван Вюрен Маттис Джозефус Янсе
Original Assignee
Сейсол Текнолоджи (Пти) Лимитед
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Сейсол Текнолоджи (Пти) Лимитед filed Critical Сейсол Текнолоджи (Пти) Лимитед
Publication of UA98660C2 publication Critical patent/UA98660C2/en

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Abstract

This invention relates to a hydrocarbon synthesis process. More particularly, but not exclusively, this invention relates to a Fischer Tropsch Process employing an activated catalyst and to the use of such an activated catalyst, wherein the Fischer Tropsch Process conditions favour the attainment of a low acid selectivity. More particularly the invention relates to a three-phase low temperature Fischer Tropsch (LTFT) process wherein a feed of Hand CO are converted to hydrocarbons and possible oxygenates thereof by contacting the Hand CO in the presence of an iron-based Fischer Tropsch catalyst in a reaction zone, wherein (lie molar ratio of H: CO in the feed is from 0.5 and less than 1.0 and wherein the iron-based Fischer Tropsch catalyst is activated according to the steps of: (a) providing an iron-based catalyst including iron in a positive oxidation state; and (b) contacting the iron- based catalyst in a reactor with a reducing gas selected from CO and a combination of Hand CO; at a reduction temperature of at least and below ; at a reducing gas pressure of above 0.5 MPa and not more than 2.2 MPa; and at a GMSV of total reducing gas fed to the reactor of at least 6000 ml(N)/g cat/h, thereby reducing the iron that is in a positive oxidation step in the catalyst.
UAA201002000A 2007-08-10 2008-08-05 Hydrocarbon synthesis process UA98660C2 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
ZA200706948 2007-08-10

Publications (1)

Publication Number Publication Date
UA98660C2 true UA98660C2 (en) 2012-06-11

Family

ID=43618593

Family Applications (1)

Application Number Title Priority Date Filing Date
UAA201002000A UA98660C2 (en) 2007-08-10 2008-08-05 Hydrocarbon synthesis process

Country Status (2)

Country Link
UA (1) UA98660C2 (en)
ZA (1) ZA201000618B (en)

Also Published As

Publication number Publication date
ZA201000618B (en) 2010-09-29

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