GB191024256A - An Improved Process and Apparatus for the Continuous Manufacture of Hydrogen and Finely Divided Carbon (Soot) from Acetylene or a Mixture of Acetylene with other Hydrocarbons. - Google Patents

An Improved Process and Apparatus for the Continuous Manufacture of Hydrogen and Finely Divided Carbon (Soot) from Acetylene or a Mixture of Acetylene with other Hydrocarbons.

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Publication number
GB191024256A
GB191024256A GB191024256DA GB191024256A GB 191024256 A GB191024256 A GB 191024256A GB 191024256D A GB191024256D A GB 191024256DA GB 191024256 A GB191024256 A GB 191024256A
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GB
United Kingdom
Prior art keywords
acetylene
soot
hydrogen
mixture
conduit
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
Inventor
Raoul Pierre Pictet
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Application granted granted Critical
Publication of GB191024256A publication Critical patent/GB191024256A/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/22Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
    • C01B3/24Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons

Abstract

24,256. Pictet, R. P. Oct. 2], 1909, [Convention date]. Carbon and hydrogen are obtained from acetylene, or a mixture of acetylene with hydrocarbons, such as benzine, petroleum, masut, &c., in the form of gas or vapour, by passing the gas or gases through a conduit heated to about 500‹ C., under a pressure slightly higher than atmospheric, the mixture being cooled in a further portion of the conduit, and its constituents being then separated. The vertical conduit a consists of a tubular body, and may be subdivided internally by a partition f of cruciform horizontal section. Pure acetylene, for example, passes in at the top e under constant pressure, and is preheated by means of a jacket c, through which are passed hot furnace gases &c., or combustible gases consumed in situ. With the commencement of the acetylene flow the external heating is stopped, the exothermic decomposition of the gas giving sufficient heat. Travelling down through the conduit a, the mixture of hydrogen and soot formed is cooled by means of a jacket d, through which is passed a regulated current of, preferably, water, or oils, the vapours of which may be mixed with the acetylene. Preferably, scraping-device is furnished to clear the walls of soot deposited thereon. The still hot mixture flows into a reservoir b on which the conduit a is mounted, for further cooling and for separation, suitable cooling-devices being preferably provided. The reservoir b is subdivided by perforated partitions h of graduated mesh, the last partition advantageously consisting of close-meshed fabric. Hydrogen is thus discharged pure at the exit i. A shaking-device k continuously clears the soot from the partitions h. In a modification, Fig. 3, the mixture of hydrogen and soot flows from the conduit a into a reservoir l, into which also water, or an oil such as petroleum, benzine, masut, or an oil suitable for mixing with the soot to form a product for subsequent utilization, say, printing- ink, is simultaneously sprayed, in excess, from a pipe s. The soot and liquid may be subsequently separated or further treated. A curved overflow pipe m is so arranged at the bottom of the reservoir l that air cannot enter, while both the hydrogen and oil continually escape.
GB191024256D 1909-10-21 1910-10-19 An Improved Process and Apparatus for the Continuous Manufacture of Hydrogen and Finely Divided Carbon (Soot) from Acetylene or a Mixture of Acetylene with other Hydrocarbons. Expired GB191024256A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE191024256X 1909-10-21

Publications (1)

Publication Number Publication Date
GB191024256A true GB191024256A (en) 1911-07-20

Family

ID=34353913

Family Applications (1)

Application Number Title Priority Date Filing Date
GB191024256D Expired GB191024256A (en) 1909-10-21 1910-10-19 An Improved Process and Apparatus for the Continuous Manufacture of Hydrogen and Finely Divided Carbon (Soot) from Acetylene or a Mixture of Acetylene with other Hydrocarbons.

Country Status (1)

Country Link
GB (1) GB191024256A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2440424A (en) * 1944-05-04 1948-04-27 Columbian Carbon Manufacture of carbon black
US2453440A (en) * 1943-05-11 1948-11-09 Shawinigan Chem Ltd Carbon black
US8771636B2 (en) 2008-01-07 2014-07-08 Mcalister Technologies, Llc Chemical processes and reactors for efficiently producing hydrogen fuels and structural materials, and associated systems and methods
US9617983B2 (en) 2011-08-12 2017-04-11 Mcalister Technologies, Llc Systems and methods for providing supplemental aqueous thermal energy
FR3121937A1 (en) * 2021-04-16 2022-10-21 Abderrezak DJENANI Variable electricity storage method

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2453440A (en) * 1943-05-11 1948-11-09 Shawinigan Chem Ltd Carbon black
US2440424A (en) * 1944-05-04 1948-04-27 Columbian Carbon Manufacture of carbon black
US8771636B2 (en) 2008-01-07 2014-07-08 Mcalister Technologies, Llc Chemical processes and reactors for efficiently producing hydrogen fuels and structural materials, and associated systems and methods
US9617983B2 (en) 2011-08-12 2017-04-11 Mcalister Technologies, Llc Systems and methods for providing supplemental aqueous thermal energy
FR3121937A1 (en) * 2021-04-16 2022-10-21 Abderrezak DJENANI Variable electricity storage method

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