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GB1063378A - Process for the removal of methylacetylene and propadiene from hydrocarbon mixtures - Google Patents

Process for the removal of methylacetylene and propadiene from hydrocarbon mixtures

Info

Publication number
GB1063378A
GB1063378A GB2829264A GB2829264A GB1063378A GB 1063378 A GB1063378 A GB 1063378A GB 2829264 A GB2829264 A GB 2829264A GB 2829264 A GB2829264 A GB 2829264A GB 1063378 A GB1063378 A GB 1063378A
Authority
GB
United Kingdom
Prior art keywords
liquid
hydrogen
propadiene
catalyst
methylacetylene
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
GB2829264A
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.)
Huels AG
Original Assignee
Chemische Werke Huels 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
Application filed by Chemische Werke Huels AG filed Critical Chemische Werke Huels AG
Publication of GB1063378A publication Critical patent/GB1063378A/en
Expired legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00—Purification; Separation; Use of additives
    • C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
    • C07C7/163—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation
    • C07C7/167—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation for removal of compounds containing a triple carbon-to-carbon bond
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/06—Halogens; Compounds thereof
    • B01J27/128—Halogens; Compounds thereof with iron group metals or platinum group metals
    • B01J27/13—Platinum group metals
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00—Purification; Separation; Use of additives
    • C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
    • C07C7/163—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Water Supply & Treatment (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Liquid C3 hydrocarbon mixtures are purified to remove methylacetylene and propadiene by passing a solution of hydrogen in the liquid through a reactor containing a hydrogenation catalyst so that the reactor remains filledwith liquid. Hydrogen is dissolved by bubbling into the liquid or spraying the liquid or trickling it through a hydrogen atmosphere, the amount of hydrogen dissolved being regulated by the pressure or partial pressure of the hydrogen which may be, for example 0-50 atmospheres. The percentage of impurities may be reduced to reduce the hydrogen concentration necessary by recycling purified product. Reaction is effected at 0-80 DEG C. and up to 100 atmospheres to maintain the liquid phase with throughputs of 10-100 kg. of mixture per hour per litre of catalyst. The catalyst may be nickel or palladium on a support.
GB2829264A 1963-07-10 1964-07-09 Process for the removal of methylacetylene and propadiene from hydrocarbon mixtures Expired GB1063378A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEC30406A DE1184336B (en) 1963-07-10 1963-07-10 Process for removing methylacetylene and propadiene from a predominantly propene-containing C-hydrocarbon mixture

Publications (1)

Publication Number Publication Date
GB1063378A true GB1063378A (en) 1967-03-30

Family

ID=7019329

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2829264A Expired GB1063378A (en) 1963-07-10 1964-07-09 Process for the removal of methylacetylene and propadiene from hydrocarbon mixtures

Country Status (3)

Country Link
DE (1) DE1184336B (en)
GB (1) GB1063378A (en)
NL (1) NL6400176A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4128595A (en) * 1977-05-02 1978-12-05 Phillips Petroleum Company Acetylene hydrogenation in liquid phase with a liquid hydrocarbon reaction medium
GB2199588A (en) * 1986-12-30 1988-07-13 Labofina Sa Process for the selective hydrogenation of acetylenes
US4831200A (en) * 1986-12-30 1989-05-16 Labofina, S.A. Process for the selective hydrogenation of alkynes
EP0541871A1 (en) * 1989-11-02 1993-05-19 Uop Hydroconversion of a waste feedstock comprising highly reactive organic compounds

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3143647A1 (en) * 1981-11-04 1983-05-11 Chemische Werke Hüls AG, 4370 Marl METHOD FOR SELECTIVELY HYDROGENATING MULTIPLE UNSATURATED HYDROCARBONS IN HYDROCARBON MIXTURES

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4128595A (en) * 1977-05-02 1978-12-05 Phillips Petroleum Company Acetylene hydrogenation in liquid phase with a liquid hydrocarbon reaction medium
GB2199588A (en) * 1986-12-30 1988-07-13 Labofina Sa Process for the selective hydrogenation of acetylenes
US4831200A (en) * 1986-12-30 1989-05-16 Labofina, S.A. Process for the selective hydrogenation of alkynes
GB2199588B (en) * 1986-12-30 1990-12-05 Labofina Sa Process for the selective hydrogenation of acetylenes
EP0541871A1 (en) * 1989-11-02 1993-05-19 Uop Hydroconversion of a waste feedstock comprising highly reactive organic compounds

Also Published As

Publication number Publication date
DE1184336B (en) 1964-12-31
NL6400176A (en) 1965-01-11

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