GB1007423A - Pyrolysis of hydrocarbons - Google Patents

Pyrolysis of hydrocarbons

Info

Publication number
GB1007423A
GB1007423A GB4252961A GB4252961A GB1007423A GB 1007423 A GB1007423 A GB 1007423A GB 4252961 A GB4252961 A GB 4252961A GB 4252961 A GB4252961 A GB 4252961A GB 1007423 A GB1007423 A GB 1007423A
Authority
GB
United Kingdom
Prior art keywords
methane
hydrogen
acetylene
pyrolysed
mixture
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
GB4252961A
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.)
Individual
Original Assignee
Individual
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 US73435A external-priority patent/US3156733A/en
Priority claimed from US111646A external-priority patent/US3156734A/en
Application filed by Individual filed Critical Individual
Publication of GB1007423A publication Critical patent/GB1007423A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/76Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Acetylene and hydrogen are obtained by the pyrolysis of methane at subatmospheric pressure at a space velocity (volumes of gas at S.T.P. per volume of reactor space per second) of 0.05-20 sec.-1 in which the reaction zone is heated to maintain the inlet and exit temperatures at at least 1250 DEG C. and the maximum temperature at at least 1500 DEG C. but not more than 250 DEG C. above the minimum temperature and quenching immediately. In a modification a mixture of hydrogen and methane in a mole ratio of 1-39: 1 is pyrolysed at 1-5 atmospheres with a minimum temperature of at least 1200 DEG C. and a maximum temperature in the range 1450-2000 DEG C. but not more than 250 DEG C. above the minimum with an effective space velocity (the space velocity divided by the total pressure in atmospheres) of 0.5-100 sec.-1 atm.-1 Where methane is not mixed with hydrogen the pressure may be 50-115 mm./Hg. and where it is mixed with hydrogen other gases, e.g. nitrogen, may also be present. Heating is preferably effected electrically. The product is substantially a mixture of hydrogen acetylene and unchanged methane. Multistage operation may be used where methane alone is pyrolysed at a methane conversion to give maximum efficiency of conversion to acetylene and after removing the acetylene the hydrogen-methane mixture is again pyrolysed and the process repeated if necessary.ALSO:Acetylene and hydrogen are obtained by the pyrolysis of methane at subatmospheric pressure at a space velocity (volumes of gas at S.T.P. per volume of reactor space per second of 0.05-20 sec.-1 in which the reaction zone is heated to maintain the inlet and exit temperatures at at least 1250 DEG C. and the maximum temperature at at least 1500 DEG C. but not more than 250 DEG C. above the minimum temperature and quenching immediately. In a modification a mixture of hydrogen and methane in a mole ratio of 1-39 : 1 is pyrolysed at 1-5 atmospheres with a minimum temperature of at least 1200 DEG C. and a maximum temperature in the range 1450-2000 DEG C. but not more than 250 DEG C. above the minimum with an effective space velocity (the space velocity divided by the total pressure in atmospheres) of 0.5-100 sec.-1 atm.-1 Where methane is not mixed with hydrogen the pressure may be 50-115 mm. Hg. and where it is mixed with hydrogen other gases, e.g. nitrogen may also be present. Heating is preferably effected electrically. The product is substantially a mixture of hydrogen acetylene and unchanged methane. Multistage operation may be used where methane alone is pyrolysed at a methane conversion to give maximum efficiency of conversion to acetylene and after removing the acetylene the hydrogen-methane mixture is again pyrolysed and the process repeated if necessary.
GB4252961A 1960-12-02 1961-11-28 Pyrolysis of hydrocarbons Expired GB1007423A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US73435A US3156733A (en) 1960-12-02 1960-12-02 Selective pyrolysis of methane to acetylene and hydrogen
US111646A US3156734A (en) 1961-05-22 1961-05-22 Pyrolysis of methane-hydrogen mixtures

Publications (1)

Publication Number Publication Date
GB1007423A true GB1007423A (en) 1965-10-13

Family

ID=26754464

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4252961A Expired GB1007423A (en) 1960-12-02 1961-11-28 Pyrolysis of hydrocarbons

Country Status (3)

Country Link
DE (1) DE1297593B (en)
GB (1) GB1007423A (en)
NL (1) NL272069A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012099677A3 (en) * 2011-01-19 2013-01-17 Exxonmobil Chemical Patents Inc. Method and apparatus for converting hydrocarbons into olefins
US9346728B2 (en) 2011-01-19 2016-05-24 Exxonmobil Chemical Patents Inc. Hydrocarbon conversion process
US9505680B2 (en) 2011-01-19 2016-11-29 Exxonmobil Chemical Patents Inc. Method and apparatus for managing the conversion of hydrocarbons into olefins
US9663419B2 (en) 2011-01-19 2017-05-30 Exxonmobil Chemical Patents Inc. Hydrocarbon conversion process
US9676681B2 (en) 2011-01-19 2017-06-13 Exxonmobil Chemical Patents Inc. Method and apparatus for managing hydrogen content through the conversion of hydrocarbons into olefins
US9677014B2 (en) 2011-01-19 2017-06-13 Exxonmobil Chemical Patents Inc. Process and apparatus for converting hydrocarbons
US9708232B2 (en) 2011-01-19 2017-07-18 Exxonmobil Chemical Patents Inc. Method and apparatus for converting hydrocarbons into olefins
US9708231B2 (en) 2011-01-19 2017-07-18 Exxonmobil Chemical Patents Inc. Method and apparatus for converting hydrocarbons into olefins using hydroprocessing and thermal pyrolysis
US9809508B2 (en) 2011-01-19 2017-11-07 Exxonmobil Chemical Patents Inc. Method and apparatus for converting hydrocarbons into olefins
US9815751B2 (en) 2011-01-19 2017-11-14 Exxonmobil Chemical Patents Inc. Hydrocarbon and oxygenate conversion by high severity pyrolysis to make acetylene and ethylene
US9868680B2 (en) 2011-01-19 2018-01-16 Exxonmobil Chemical Patents Inc. Method and apparatus for converting hydrocarbons into olefins
US11617997B2 (en) 2018-06-05 2023-04-04 Ihi Corporation Hydrogen production apparatus and hydrogen production method

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1773611A (en) * 1926-03-15 1930-08-19 Banck Martin Preparation of acetylene and hydrogen
DE594125C (en) * 1926-03-16 1934-03-13 Ruhrchemie Akt Ges Process for the production of acetylene from methane or other gaseous hydrocarbons
GB416921A (en) * 1932-12-23 1934-09-24 Fischer Franz Process for the production of unsaturated hydrocarbons from hydrocarbons proportionately richer in hydrogen

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012099677A3 (en) * 2011-01-19 2013-01-17 Exxonmobil Chemical Patents Inc. Method and apparatus for converting hydrocarbons into olefins
US9346728B2 (en) 2011-01-19 2016-05-24 Exxonmobil Chemical Patents Inc. Hydrocarbon conversion process
US9505680B2 (en) 2011-01-19 2016-11-29 Exxonmobil Chemical Patents Inc. Method and apparatus for managing the conversion of hydrocarbons into olefins
US9663419B2 (en) 2011-01-19 2017-05-30 Exxonmobil Chemical Patents Inc. Hydrocarbon conversion process
US9676681B2 (en) 2011-01-19 2017-06-13 Exxonmobil Chemical Patents Inc. Method and apparatus for managing hydrogen content through the conversion of hydrocarbons into olefins
US9677014B2 (en) 2011-01-19 2017-06-13 Exxonmobil Chemical Patents Inc. Process and apparatus for converting hydrocarbons
US9708232B2 (en) 2011-01-19 2017-07-18 Exxonmobil Chemical Patents Inc. Method and apparatus for converting hydrocarbons into olefins
US9708231B2 (en) 2011-01-19 2017-07-18 Exxonmobil Chemical Patents Inc. Method and apparatus for converting hydrocarbons into olefins using hydroprocessing and thermal pyrolysis
US9809508B2 (en) 2011-01-19 2017-11-07 Exxonmobil Chemical Patents Inc. Method and apparatus for converting hydrocarbons into olefins
US9815919B2 (en) 2011-01-19 2017-11-14 Exxonmobil Chemical Patents Inc. Hydrocarbon conversion process
US9815751B2 (en) 2011-01-19 2017-11-14 Exxonmobil Chemical Patents Inc. Hydrocarbon and oxygenate conversion by high severity pyrolysis to make acetylene and ethylene
US9868680B2 (en) 2011-01-19 2018-01-16 Exxonmobil Chemical Patents Inc. Method and apparatus for converting hydrocarbons into olefins
US11617997B2 (en) 2018-06-05 2023-04-04 Ihi Corporation Hydrogen production apparatus and hydrogen production method

Also Published As

Publication number Publication date
DE1297593B (en) 1969-06-19
NL272069A (en)

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