GB613926A - Improvements in or relating to alkylation process and products thereof - Google Patents

Improvements in or relating to alkylation process and products thereof

Info

Publication number
GB613926A
GB613926A GB25055/45A GB2505545A GB613926A GB 613926 A GB613926 A GB 613926A GB 25055/45 A GB25055/45 A GB 25055/45A GB 2505545 A GB2505545 A GB 2505545A GB 613926 A GB613926 A GB 613926A
Authority
GB
United Kingdom
Prior art keywords
benzene
silica
alumina
catalyst
gel
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
GB25055/45A
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.)
Phillips Petroleum Co
Original Assignee
Phillips Petroleum Co
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 Phillips Petroleum Co filed Critical Phillips Petroleum Co
Priority to GB25055/45A priority Critical patent/GB613926A/en
Publication of GB613926A publication Critical patent/GB613926A/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
    • C07C2/54Preparation 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
    • C07C2521/02Boron or aluminium; Oxides or hydroxides thereof
    • 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
    • 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
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/08Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of gallium, indium or thallium
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2527/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • C07C2527/02Sulfur, selenium or tellurium; Compounds thereof
    • C07C2527/053Sulfates or other compounds comprising the anion (SnO3n+1)2-
    • C07C2527/054Sulfuric acid or other acids with the formula H2Sn03n+1
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2527/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • C07C2527/14Phosphorus; Compounds thereof
    • C07C2527/16Phosphorus; Compounds thereof containing oxygen
    • C07C2527/167Phosphates or other compounds comprising the anion (PnO3n+1)(n+2)-
    • C07C2527/173Phosphoric acid or other acids with the formula Hn+2PnO3n+1
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

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

Abstract

Benzene compounds are alkylated with olefins of not more than 6 carbon atoms by reacting a mixture thereof with the benzene compound in molar excess, and free from other unsaturated hydrocarbons, in the presence of an absorbant gel comprising silica and not more than 10 per cent by weight of an oxide of a metal of Group 3B, including boron, or Group 4A. Suitable silica-alumina catalysts may be prepared as disclosed in U.S.A. Specifications 2,142,324 and 2,147,985. A hydrous silica gel is first made from alkali silicate and acid, washed, activated with a solution of a metal salt which is hydrolysable, and washed and dried to give hard granules. Alternatively, the metal salt may be added before gelation. Instead of alumina, oxides of boron, indium, thallium, titanium, zirconium and thorium may similarly be incorporated. The amount of metal oxide is preferably about 0.1-2 per cent by weight. Catalytic activity is increased by dehydration at about 200-300 DEG F. in a steam of inert gas prior to use. A benzene to olefin molar ratio between 1 : 1 and 1 : 10 is suitable. Multi-point injection of olefin and recirculation of the effluent may be used. Temperatures are generally about 200-700 DEG F. With propylene 250-450 DEG and with ethylene 450-550 DEG F. are preferred. Pressures to maintain a substantial amount of liquid phase, generally 50-2000 p.s.i., may be used. Temperature may be increased gradually as activity decreases. Flow rates are normally 0.1-10 liquid vols. per vol. per hr. Pure olefins or mixtures thereof or with paraffins may be treated. In addition to benzene and its homologues such as toluene, xylene and ethylbenzene compounds such as phenols and halogen derivatives may be used. In examples: (1) a silica-alumina gel containing 1.3 per cent alumina, made by adding sodium silicate to sulphuric acid, boiling the partially dried gel with aluminium sulphate solution, washing and drying is used to alkylate a 5 : 1 molar benzene-ethylene solution at 500 DEG F., 400 p.s.i., and reaction time of 46 mins.; (2) using aluminium and zirconium chlorides, a catalyst containing silica, alumina and zirconia in a weight ratio of 95 : 4 : 1 is obtained and used to produce ethylbenzene; (3) isopropylbenzene is prepared from propylene and benzene using the catalyst of (1) at 350-400 DEG F., reaction time 30 mins.; (4) the catalyst is first dehydrated in propane at 250 DEG F.; (5) benzene and propylene in molar ratio 8 : 1 are reacted at 300-330 DEG F. and 250 p.s.i.; (6) silica-zirconia made by mixed precipitation is used for a similar reaction; (7) a butane-butene fraction with benzene in 6 : 1 molar excess yields butyl benzenes; (8) a 3 : 1 benzene, ethylene mixture with the catalyst of (1) yields ethylbenzene; (9) a silica-zirconia catalyst is used for ethylating benzene.
GB25055/45A 1945-09-27 1945-09-27 Improvements in or relating to alkylation process and products thereof Expired GB613926A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB25055/45A GB613926A (en) 1945-09-27 1945-09-27 Improvements in or relating to alkylation process and products thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB25055/45A GB613926A (en) 1945-09-27 1945-09-27 Improvements in or relating to alkylation process and products thereof

Publications (1)

Publication Number Publication Date
GB613926A true GB613926A (en) 1948-12-07

Family

ID=10221491

Family Applications (1)

Application Number Title Priority Date Filing Date
GB25055/45A Expired GB613926A (en) 1945-09-27 1945-09-27 Improvements in or relating to alkylation process and products thereof

Country Status (1)

Country Link
GB (1) GB613926A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2852576A (en) * 1955-04-06 1958-09-16 Standard Oil Co Mixture of certain metal hydrides with solid acidic promoters as catalysts for aromatic alkylation

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2852576A (en) * 1955-04-06 1958-09-16 Standard Oil Co Mixture of certain metal hydrides with solid acidic promoters as catalysts for aromatic alkylation

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