GB455567A - Improvements relating to the manufacture of acetylene - Google Patents

Improvements relating to the manufacture of acetylene

Info

Publication number
GB455567A
GB455567A GB30056/35A GB3005635A GB455567A GB 455567 A GB455567 A GB 455567A GB 30056/35 A GB30056/35 A GB 30056/35A GB 3005635 A GB3005635 A GB 3005635A GB 455567 A GB455567 A GB 455567A
Authority
GB
United Kingdom
Prior art keywords
arc
fed
carbonaceous material
solid carbonaceous
water
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
GB30056/35A
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.)
Standard Oil Development Co
Original Assignee
Standard Oil Development 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 Standard Oil Development Co filed Critical Standard Oil Development Co
Publication of GB455567A publication Critical patent/GB455567A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Working-Up Tar And Pitch (AREA)

Abstract

<PICT:0455567/IV/1> <PICT:0455567/IV/2> <PICT:0455567/IV/3> Acetylene is obtained by feeding a finely comminuted, normally solid carbonaceous material and a normally fluid hydrocarbon material simultaneously to an electric arc. The normally solid carbonaceous material must have an atomic H : C ratio below 0,75, and may be soft or hard coal, coke, charcoal or lamp black. The normally fluid hydrocarbon material may be methane, natural gas, petroleum refinery gases, ethane, butane, ethylene, butylene, naphtha, gas oil, or tar. The materials are preferably preheated, and may also be mixed before they are fed to the arc. The period during which the materials are subjected to the reaction temperature should lie between 1 and 0,0005 second. The process may be effected at atmospheric or somewhat raised or reduced pressure, and the reaction products should be rapidly cooled, e.g. by injection of water; the cooling water may be recirculated directly, or the solids which it contains may be separated and optionally returned to the arc. As shown in Fig. 1, coke or coal fed to a crusher 1 is passed by a blower 2 to a hopper 6, from which it is fed to a pipe 8 through which hydrocarbon gas is supplied. The mixture passes through a preheater 9 to an arc 10, the products from which pass through a water spray 14, cooler 15, dust separator 16 and blower 17 to a scrubber 18, from which the gases containing acetylene are withdrawn. The liquid used in scrubber 18 may be gas oil or other solvent for diacetylene and like impurities. The solids washed from the gases by the spray 14 are collected in a tank 20 and may be discharged through outlet 24 or fed by a conveyer 25 through a drier 26 and thence to blower 2. Clarified water from the tank 20 is returned to the spray 14 by a pump 28. In a modification, Fig. 2, the hydrocarbon gas is fed to the arc 10 through a hollow positive electrode 11a, and the solid carbonaceous material is supplied as a preferably preheated solid rod 30 fed against an abrading device such as a rotary toothed wheel or drum 31, preferably water-cooled; the products are withdrawn through the hollow annular negative electrode 12a. In a further modification, Fig. 3 (not shown), the positive electrode is solid, and a hydrocarbon liquid, e.g. gas oil, containing solid carbonaceous material in suspension, is fed through nozzles directly into the arc. In a further modification, Fig. 4 (not shown), a mixture of hydrocarbon gas and solid carbonaceous material is fed downwardly through a vertical hollow positive electrode and the products are cooled by a water spray immediately after they have passed through the negative electrode; alternatively, the materials may be fed tangentially into the arc chamber so as to produce a swirling arc. As a further modification, Fig. 5 (not shown), the arc may be struck between electrodes composed of finely divided carbonaceous material loosely packed in stick form, a hydrocarbon gas or vapour being fed to the arc through a preheater; the electrodes for use in this modification may be prepared by mixing coke dust with such a restricted amount of a binder that a shower of dust particles is produced in the arc; the binder may be water, preferably containing a little glue or like material, or a water-insoluble p binder such as tar; loosely packed rods prepared as described may alternatively be used merely as the source of solid carbonaceous material in association with ordinary carbon electrodes. Fig. 6 shows a further modification in which hydrocarbon gas is fed to an arc 10 through a pipe 8, and solid carbonaceous material is supplied as a rod 30 fed against a toothed wheel or drum 31. The Specification as open to inspection under Sect. 91 defines the solid carbonaceous material as having, preferably, a H : C ratio below 1, and specifies, as suitable materials, asphaltenes, polynuclear aromatic materials such as anthracene and fluorescein, or derivatives thereof or products containing them, such as suitable fractions obtained by the distillation of coal or oil shale. This subject-matter does not appear in the Specification as accepted.
GB30056/35A 1934-12-29 1935-10-31 Improvements relating to the manufacture of acetylene Expired GB455567A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US455567XA 1934-12-29 1934-12-29

Publications (1)

Publication Number Publication Date
GB455567A true GB455567A (en) 1936-10-23

Family

ID=21938593

Family Applications (1)

Application Number Title Priority Date Filing Date
GB30056/35A Expired GB455567A (en) 1934-12-29 1935-10-31 Improvements relating to the manufacture of acetylene

Country Status (1)

Country Link
GB (1) GB455567A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3148227A (en) * 1961-05-04 1964-09-08 Crown Zellerbach Corp Preparation of unsaturated hydrocarbons from oxygen-containing organic materials
US4358629A (en) * 1980-08-18 1982-11-09 Avco Corporation Method of producing acetylene from coal

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3148227A (en) * 1961-05-04 1964-09-08 Crown Zellerbach Corp Preparation of unsaturated hydrocarbons from oxygen-containing organic materials
US4358629A (en) * 1980-08-18 1982-11-09 Avco Corporation Method of producing acetylene from coal

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