GB592867A - Production of styrenes and other products - Google Patents

Production of styrenes and other products

Info

Publication number
GB592867A
GB592867A GB6592/45A GB659245A GB592867A GB 592867 A GB592867 A GB 592867A GB 6592/45 A GB6592/45 A GB 6592/45A GB 659245 A GB659245 A GB 659245A GB 592867 A GB592867 A GB 592867A
Authority
GB
United Kingdom
Prior art keywords
xylyl
ethane
catalyst
tolyl
phenyl
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
GB6592/45A
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.)
Domtar Inc
Original Assignee
Dominion Tar and Chemical Co Ltd
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 Dominion Tar and Chemical Co Ltd filed Critical Dominion Tar and Chemical Co Ltd
Publication of GB592867A publication Critical patent/GB592867A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • 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
    • 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
    • Y02P20/584Recycling of catalysts

Landscapes

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

Abstract

Styrenes and their nuclear substituted derivatives are produced by heating asym. diaryl paraffins, and their nuclear substituted derivatives having at least 2 carbon atoms in the paraffin chain, to at least 350 DEG C., and passing them through a finely-divided siliceous catalyst, preferably a hydrated aluminium silicate, with a contact time of .004-.4 sec. Inert diluents such as water vapour, hydrocarbons, e.g. benzene or toluene or fixed gases, e.g. nitrogen or carbon dioxide, are preferably present in a molar ratio to the diaryl paraffin of 1 : 2 to 25 : 1. Initial materials include asym. diphenyl, phenyl tolyl, ditolyl, phenyl xylyl, tolyl xylyl, and dixylyl ethanes, a ,a -diphenyl, phenyl tolyl, phenyl xylyl, ditolyl, and tolyl xylyl propanes, and their nuclear halogen or hydroxy substituted derivatives, and hydrocarbon oils containing the same as obtained by distilling benzol still residues. These may be preheated and passed through a steel, silica or other converter containing the catalyst at the desired temperature of 350 DEG to about 600 DEG C. or even higher. Those catalysts with higher ratios of silica to alumina are most active. They may be formed into pellets, preferably of not more than 5 mm. greatest diameter. The contact time is computed on the assumption that the catalyst is 50 per cent voids and neglecting pressure drop and volume increase. Unconverted materials may be recirculated. Pressure may be atmospheric, reduced or elevated. The catalyst is reactivated with air, preferably mixed with steam, at about 590-650 DEG C. In examples: ditolyl ethane with benzene, water, nitrogen or carbon dioxide in molar ratios of 1 : 12.2, 16, 11.85 or 12.1 respectively is treated at between 440 DEG and 475 DEG C. using contact times of .08, .033 and .10, p-methyl styrene and toluene being recovered; di-(m-xylyl) ethane with 23.7 molar proportions of water is treated at 390 DEG C. with a contact time of .065 sec. giving dimethyl styrenes and m-xylene; while di-(chlorphenyl) ethane and di-(dichlorphenyl) ethane with water at between 630 DEG and 650 DEG C. and contact times of .1-.4 sec. give chlor- and dichlorstyrene respectively and chlorbenzene or o-dichlor-benzene. Specification 569,465 is referred to.
GB6592/45A 1944-09-29 1945-03-15 Production of styrenes and other products Expired GB592867A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CA592867X 1944-09-29

Publications (1)

Publication Number Publication Date
GB592867A true GB592867A (en) 1947-10-01

Family

ID=4171886

Family Applications (1)

Application Number Title Priority Date Filing Date
GB6592/45A Expired GB592867A (en) 1944-09-29 1945-03-15 Production of styrenes and other products

Country Status (1)

Country Link
GB (1) GB592867A (en)

Similar Documents

Publication Publication Date Title
GB950976A (en) Improvements in and relating to the production of olefines
GB402928A (en) A process for the halogenation of unsaturated hydrocarbons
GB586483A (en) Process for the conversion of normally gaseous olefins to liquid hydrocarbons
US2399678A (en) Catalysis
US2369377A (en) Method of preparing sulphur compounds
US2002394A (en) Process for converting hydrocarbons
US2030070A (en) Manufacture of acetylene
US2315499A (en) Production of paraffin-olefin mixtures
GB592867A (en) Production of styrenes and other products
US3126422A (en) Temperature
GB1107432A (en) Dehydrogenation process
US3446868A (en) Disproportionation of propane
GB753770A (en) Process for preparing olefins by cracking high boiling hydrocarbons
US2204673A (en) Method of treating hydrocarbons
US2302721A (en) Alkylation of aromatic compounds
US3417148A (en) Alkylation process
US3054835A (en) Alkylation of aromatic hydrocarbons
US2326586A (en) High pressure alkylation reaction
US2002534A (en) Method for the production of normally liquid hydrocarbons from gaseous or lower boiling hydrocarbon materials
US3336410A (en) Alkylation process and catalyst therefor
GB945448A (en) Improvements in and relating to the production of lower olefines
US3393246A (en) Isomerization process
GB737026A (en) Polymerisation of olefins
GB1393904A (en) Hydroalkylation
US3529032A (en) Cracking of olefins