GB1490494A - Process for the production of low molecular weight hydrocarbons - Google Patents

Process for the production of low molecular weight hydrocarbons

Info

Publication number
GB1490494A
GB1490494A GB15992/76A GB1599276A GB1490494A GB 1490494 A GB1490494 A GB 1490494A GB 15992/76 A GB15992/76 A GB 15992/76A GB 1599276 A GB1599276 A GB 1599276A GB 1490494 A GB1490494 A GB 1490494A
Authority
GB
United Kingdom
Prior art keywords
reactor
catalyst
gas
per
catalytic hydrogenation
Prior art date
Legal status (The legal status 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 status listed.)
Expired
Application number
GB15992/76A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ruhrchemie AG
Original Assignee
Ruhrchemie AG
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
Priority claimed from DE19752518982 external-priority patent/DE2518982C3/en
Application filed by Ruhrchemie AG filed Critical Ruhrchemie AG
Publication of GB1490494A publication Critical patent/GB1490494A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/78Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with alkali- or alkaline earth metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/80Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with zinc, cadmium or mercury
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61Surface area
    • B01J35/612Surface area less than 10 m2/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/61Surface area
    • B01J35/615100-500 m2/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/60Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/64Pore diameter
    • B01J35/657Pore diameter larger than 1000 nm
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/06Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74Iron group metals
    • C07C2523/745Iron

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

1490494 C 2 -C 4 olefins by hydrogenation of carbon monoxide RUHRCHEMIE AG 20 April 1976 [29 April 1975] 15992/76 Heading C5E A process for the production of a hydrocarbon mixture containing at least 50% by weight of one or more C 2 to C 4 hydrocarbons and at least 50% by weight of one or more olefins the percentage being used on the total content of hydrocarbons having at least 2 carbon atoms, comprises catalytic hydrogenation of carbon monoxide in a fixed-bed reactor under superatmospheric total pressure and at elevated temperatures, as follows: the catalytic hydrogenation is carried out using one or more catalysts arranged in at least 2 and not more than 10 layers: the catalytic hydrogenation is carried out in a reactor having a length of from 0À5 to 4À5 meters: the pressure in the reactor is from 5 to 30 bars: the temperature measured on the catalyst is from 250‹ to 370‹ C: the space velocity of fresh gas through the reactor is adjusted to from 1,000 to 10,000 std. cu.m.per cu.m. of catalyst per hour and: the rate of supply of recycle gas to the reactor is adjusted to from 5 times to 25 times the rate of supply of fresh gas to the reactor: the total gas loading to the reactor is from 7,500 to 50,000std.cu.m.per cu.m. of catalyst per hour and the catalyst is arranged in such a manner that the linear gas flow velocity through the reactor ranges between 1 and 10 m./second, based on normal conditions, and the residence time of the gas in the reactor ranges between 0À05 and 1 second, based of normal conditions, and the or each catalyst has an internal surface area of 5 to 150 sq.m. per gram of catalyst. A preferred catalyst comprises iron oxide, copper oxide, zinc oxide and K 2 CO 3 .
GB15992/76A 1975-04-29 1976-04-20 Process for the production of low molecular weight hydrocarbons Expired GB1490494A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19752518982 DE2518982C3 (en) 1975-04-29 Process for the production of hydrocarbon mixtures

Publications (1)

Publication Number Publication Date
GB1490494A true GB1490494A (en) 1977-11-02

Family

ID=5945273

Family Applications (1)

Application Number Title Priority Date Filing Date
GB15992/76A Expired GB1490494A (en) 1975-04-29 1976-04-20 Process for the production of low molecular weight hydrocarbons

Country Status (9)

Country Link
JP (1) JPS51131808A (en)
AU (1) AU498400B2 (en)
BE (1) BE840969A (en)
CA (1) CA1053265A (en)
DD (1) DD123881A5 (en)
FR (1) FR2309497A1 (en)
GB (1) GB1490494A (en)
NL (1) NL162622C (en)
ZA (1) ZA762412B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7012103B2 (en) 2003-03-24 2006-03-14 Conocophillips Company Commercial fischer-tropsch reactor

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4206134A (en) * 1979-03-12 1980-06-03 Exxon Research & Engineering Co. Ruthenium supported on manganese oxide as hydrocarbon synthesis catalysts in CO/H2 reactions
US4402869A (en) 1979-03-12 1983-09-06 Exxon Research And Engineering Co. Group VIII metals on manganese-containing oxide supports which exhibit strong metal support interactions
EP0101913A3 (en) * 1982-08-03 1986-07-30 BASF Aktiengesellschaft Dehydrogenation catalyst
GB0501731D0 (en) * 2005-01-31 2005-03-02 Accentus Plc Catalytic reactor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7012103B2 (en) 2003-03-24 2006-03-14 Conocophillips Company Commercial fischer-tropsch reactor

Also Published As

Publication number Publication date
AU1322476A (en) 1977-10-27
JPS51131808A (en) 1976-11-16
JPS5443481B2 (en) 1979-12-20
FR2309497B1 (en) 1981-02-13
BE840969A (en) 1976-10-21
CA1053265A (en) 1979-04-24
DE2518982B2 (en) 1977-03-03
NL162622B (en) 1980-01-15
NL162622C (en) 1980-06-16
DE2518982A1 (en) 1976-11-11
FR2309497A1 (en) 1976-11-26
NL7509662A (en) 1976-11-02
ZA762412B (en) 1977-04-27
AU498400B2 (en) 1979-03-08
DD123881A5 (en) 1977-01-19

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PCNP Patent ceased through non-payment of renewal fee