GB366107A - Improvements in the thermal treatment of organic substances - Google Patents

Improvements in the thermal treatment of organic substances

Info

Publication number
GB366107A
GB366107A GB2885230A GB2885230A GB366107A GB 366107 A GB366107 A GB 366107A GB 2885230 A GB2885230 A GB 2885230A GB 2885230 A GB2885230 A GB 2885230A GB 366107 A GB366107 A GB 366107A
Authority
GB
United Kingdom
Prior art keywords
per cent
hydrogen
methane
passed
chromic acid
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
GB2885230A
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.)
IG Farbenindustrie AG
Original Assignee
IG Farbenindustrie 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 IG Farbenindustrie AG filed Critical IG Farbenindustrie AG
Priority to GB2885230A priority Critical patent/GB366107A/en
Publication of GB366107A publication Critical patent/GB366107A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/02Apparatus characterised by being constructed of material selected for its chemically-resistant properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/02Apparatus characterised by their chemically-resistant properties
    • B01J2219/0204Apparatus characterised by their chemically-resistant properties comprising coatings on the surfaces in direct contact with the reactive components
    • B01J2219/0236Metal based
    • B01J2219/024Metal oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/02Apparatus characterised by their chemically-resistant properties
    • B01J2219/025Apparatus characterised by their chemically-resistant properties characterised by the construction materials of the reactor vessel proper
    • B01J2219/0263Ceramic
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/02Apparatus characterised by their chemically-resistant properties
    • B01J2219/025Apparatus characterised by their chemically-resistant properties characterised by the construction materials of the reactor vessel proper
    • B01J2219/0263Ceramic
    • B01J2219/0268Porcelain

Landscapes

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

Abstract

In thermal treatments of organic products, such as the cracking of oils, the conversion of methane and its homologues with steam or carbon dioxide into carbon monoxide and hydrogen, or in the reduction of phenol, cresol, and the like with hydrogen, the deposition of carbon is avoided by providing the surfaces of ceramic apparatus which come into contact with the hot organic materials, with a complete or partial covering of oxides of chromium, tungsten, vanadium, or uranium. For example, chamotte tubes or bricks or unglazed porcelain tubes are impregnated with aqueous chromic acid or chromium salts (or chromates which form chromium oxide on heating) and then heating, for instance to 1600 DEG C.; or the metal compounds may be incorporated in the materials from which the ceramic material is made. Catalysts may also be employed, incorporated in the surfaces in a similar manner. In examples (1) an internally unglazed porcelain tube is soaked with a 50 per cent aqueous chromic acid and dried at 400 DEG C., this being repeated three times; methane is passed through this tube at 1075-1100 DEG C. to produce benzene hydrocarbons and hydrogen; (2) methane is passed through a fireclay tube impregnated with chromic acid and is converted into benzene hydrocarbons and hydrogen at 1100-1200 DEG C.; (3) vapour of paraffin oil (boiling point 330-380 DEG C.) is passed at 650-700 DEG C. through a porcelain tube impregnated with chromic acid, 41 per cent of oils and 61 per cent of gases being produced; of the oils 60 per cent are of boiling point up to 200 DEG C. and 16 per cent of boiling point 200-300 DEG C., while the gas contains 40 per cent of olefines, 48 per cent of methane and its homologues and 10 per cent of hydrogen; (4) ethylene is passed at 700-750 DEG C. through a similar tube, 15 per cent of the ethylene being converted into a liquid containing 50 per cent of benzene and 50 per cent higher aromatic hydrocarbons; the gas contains 39 per cent of ethylene, 38 per cent of methane, and 21 per cent of hydrogen. Specification 317,359, [Class 32, Distilling &c.], is referred to.ALSO:In thermal treatments of organic products, such as the cracking of oils, the polymerization of olefines or cracking gases into benzene, the conversion of methane into benzene or olefines, the conversion of methane and its homologues with steam or carbon dioxide into carbon monoxide and hydrogen, or in the reduction of phenol, cresol, and the like with hydrogen, the deposition of carbon is avoided by providing the surfaces of ceramic apparatus which come into contact with the hot organic materials, with a complete or partial covering of oxides of chromium, tungsten, vanadium, or uranium. For example, chamotte tubes or bricks or unglazed porcelain tubes are impregnated with aqueous chromic acid or chromium salts (or chromates which form chromium oxide on heating) and then heating for instance to 1600 DEG C.; or the metal compounds may be incorporated in the materials from which the ceramic material is made. Catalysts may also be employed, incorporated in the surfaces in a similar manner. In examples (1) an internally unglazed porcelain tube is soaked with a 50 per cent aqueous chromic acid and dried at 400 DEG C., this being repeated three times; methane is passed through this tube at 1075-1100 DEG C. to produce benzene hydrocarbons and hydrogen; (2) methane is passed through a fireclay tube impregnated with chromic acid and is converted into benzene hydrocarbons and hydrogen at 1100-1200 DEG C.; (3) vapour of paraffin oil (b.p. 330-380 DEG C.) is passed at 650-700 DEG C. through a porcelain tube impregnated with chromic acid, 41 per cent of oils and 61 per cent of gases being produced; of the oils 60 per cent are of b.p. up to 200 DEG C. and 16 per cent of b.p. 200-300 DEG C., while the gas contains 40 per cent of olefines, 48 per cent of methane and its homologues and 10 per cent of hydrogen; (4) ethylene is passed at 700-750 DEG C. through a similar tube, 15 per cent of the ethylene being converted into a liquid containing 50 per cent of benzene and 50 per cent higher aromatic hydrocarbons; the gas contains 39 per cent of ethylene, 38 per cent of methane and 21 per cent of hydrogen. Specification 317,359 [Class 2 (iii), Dyes &c.], is referred to.
GB2885230A 1930-09-26 1930-09-26 Improvements in the thermal treatment of organic substances Expired GB366107A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2885230A GB366107A (en) 1930-09-26 1930-09-26 Improvements in the thermal treatment of organic substances

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2885230A GB366107A (en) 1930-09-26 1930-09-26 Improvements in the thermal treatment of organic substances

Publications (1)

Publication Number Publication Date
GB366107A true GB366107A (en) 1932-01-26

Family

ID=10282191

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2885230A Expired GB366107A (en) 1930-09-26 1930-09-26 Improvements in the thermal treatment of organic substances

Country Status (1)

Country Link
GB (1) GB366107A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE865504C (en) * 1950-02-25 1953-02-02 Didier Kogag Hinselmann Koksof Method and device for the thermal cracking of gases containing methane and similar hydrocarbons

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE865504C (en) * 1950-02-25 1953-02-02 Didier Kogag Hinselmann Koksof Method and device for the thermal cracking of gases containing methane and similar hydrocarbons

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