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GB778014A - A process for alkylating benzene or a mono-alkyl benzene or a mixture thereof in the liquid phase - Google Patents

A process for alkylating benzene or a mono-alkyl benzene or a mixture thereof in the liquid phase

Info

Publication number
GB778014A
GB778014A GB18939/55A GB1893955A GB778014A GB 778014 A GB778014 A GB 778014A GB 18939/55 A GB18939/55 A GB 18939/55A GB 1893955 A GB1893955 A GB 1893955A GB 778014 A GB778014 A GB 778014A
Authority
GB
United Kingdom
Prior art keywords
benzene
catalyst
per cent
mono
liquid phase
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
GB18939/55A
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.)
Bataafsche Petroleum Maatschappij NV
Original Assignee
Bataafsche Petroleum Maatschappij NV
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 Bataafsche Petroleum Maatschappij NV filed Critical Bataafsche Petroleum Maatschappij NV
Publication of GB778014A publication Critical patent/GB778014A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C15/00Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
    • C07C15/02Monocyclic hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/54Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition of unsaturated hydrocarbons to saturated hydrocarbons or to hydrocarbons containing a six-membered aromatic ring with no unsaturation outside the aromatic ring
    • C07C2/64Addition to a carbon atom of a six-membered aromatic ring
    • C07C2/66Catalytic processes
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/06Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • C07C2521/08Silica
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/12Silica and alumina

Landscapes

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

Abstract

Benzene or a mono-alkyl benzene of which the alkyl group contains between one and four carbon atoms is alkylated in the liquid phase by means of an alkene containing between 2 and 4 carbon atoms at a temperature above 160 DEG C. in the presence of a cracking catalyst having a water content below 3.5 per cent by weight and an L.H.S.V. of at least 3. A cracking catalyst is defined as a catalyst which may be used in the cracking of petroleum. This may be a silicate of one or more of the metals aluminium, magnesium, and zirconium, optionally in the presence of smaller quantities of the oxides of calcium, sodium, potassium, and of traces of hydrogen, carbon and sulphur. Preferred catalysts are those of the aluminium silicate type produced according to the method described in Specification 504,614, [Group III], containing 85-90 per cent of SiO2 and 15-10 per cent of Al2O3. The catalyst may be surface treated by heating at 600 DEG C. for 1-24 hours in steam, or at 800 DEG C. for 1-24 hours in hot air, or in aqueous HF solution at air temperature. The moisture content of the catalyst is preferably between 0.1 and 0.2 per cent by weight. In examples, cumene is alkylated with propene according to the invention to give paradi-iso propyl benzene which may be converted to terephthalic acid by the processes of Specifications 737,439, 749,186 and 749,187.
GB18939/55A 1954-06-30 1955-06-30 A process for alkylating benzene or a mono-alkyl benzene or a mixture thereof in the liquid phase Expired GB778014A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL778014X 1954-06-30

Publications (1)

Publication Number Publication Date
GB778014A true GB778014A (en) 1957-07-03

Family

ID=19830036

Family Applications (1)

Application Number Title Priority Date Filing Date
GB18939/55A Expired GB778014A (en) 1954-06-30 1955-06-30 A process for alkylating benzene or a mono-alkyl benzene or a mixture thereof in the liquid phase

Country Status (1)

Country Link
GB (1) GB778014A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0064046A1 (en) * 1981-04-20 1982-11-03 Cosden Technology Inc. Alkylation of aromatic compounds with silicalite catalysts in the presence of steam
US4665256A (en) * 1983-04-29 1987-05-12 The Dow Chemical Company Alkylation of aromatic mixtures
US5030786A (en) * 1989-06-23 1991-07-09 Fina Technology, Inc. Liquid phase aromatic conversion process

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0064046A1 (en) * 1981-04-20 1982-11-03 Cosden Technology Inc. Alkylation of aromatic compounds with silicalite catalysts in the presence of steam
US4665256A (en) * 1983-04-29 1987-05-12 The Dow Chemical Company Alkylation of aromatic mixtures
US5030786A (en) * 1989-06-23 1991-07-09 Fina Technology, Inc. Liquid phase aromatic conversion process

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