GB360943A - Improvements in and apparatus for introducing and withdrawing solid substances into and out of vessels containing a medium under high pressure - Google Patents

Improvements in and apparatus for introducing and withdrawing solid substances into and out of vessels containing a medium under high pressure

Info

Publication number
GB360943A
GB360943A GB2368230A GB2368230A GB360943A GB 360943 A GB360943 A GB 360943A GB 2368230 A GB2368230 A GB 2368230A GB 2368230 A GB2368230 A GB 2368230A GB 360943 A GB360943 A GB 360943A
Authority
GB
United Kingdom
Prior art keywords
pressure
chamber
chambers
elastic
valves
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
GB2368230A
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 GB2368230A priority Critical patent/GB360943A/en
Publication of GB360943A publication Critical patent/GB360943A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/06Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by destructive hydrogenation

Landscapes

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

Abstract

Solid substances are fed to or withdrawn from a vessel A, Fig 1, containing a medium under high pressure by means of a plurality of chambers B arranged in series and in which the pressure increases or decreases in successive chambers. The stage vessels or chambers B are separated from one another by valves C, C<1> respectively connected to operating means D, D<1> and are connected to each other by pressure equalizing valves E, E<1>. These valves are opened so that the pressure between two adjacent stage vessels is equalized and then the valve C or C<1> separating the chambers is opened for the solid material to pass from one chamber into the other on its way to the vessel A. If the vessel A is subjected to a pressure 5p then the pressure in the chambers B may be indicated by Op, 1p, 2p, &c. Each chamber B is connected by a pipe to a pressure regulating device F set to pressures 1p, 2p, &c. so that when the pressure in two adjacent chambers is equalized, the common pressure is higher than the desired stage pressure and the surplus pressure is withdrawn through the device F. The gases passing through the device F are supplied to a compresser G and the gas released from pressure at H is compressed to a pressure 5p and is supplied to the lowermost chamber B. The withdrawal of the substance can be effected in a corresponding apparatus while reducing the pressure in stages. The stage vessels B may be connected together by intermediate vessels K, Fig. 2, provided on the interior side with elastic pipes or tubings L adapted to be extended by fluid pressure supplied by a pump, to shut off one vessel from another alternately. The gas released from pressure at H is cleaned at M before passing through a compresser G on its way to the chamber N. In a modification a column formed of chambers K with elastic diaphragms L which are alternately expanded and contracted may be used. In Fig. 4 the elastic tubes K1, K2 are adapted to be expanded alternately to grip the cylindrical portion of valves T1, T2. These valves are manually operated and may be provided with screw devices which are rotated to feed the material from one chamber to the other when the elastic tube between them is collapsed. The elastic sealing means may be of U-section or may be a disc attached to one wall of the chamber which is extended by a plunger into the opposing wall of the chamber. In a further modification a compressible tube or connection between the two chambers is squeezed alternately at its upper and lower end by plungers so that the space between the plungers is alternately filled and discharged. In Fig. 8 the compressible connection Y is adapted to be squeezed together by rollers C<1>, C<2>, &c., mounted on endless bands, the material trapped in the connection between opposed pairs of rollers being discharged therefrom by a squeezing and sliding action. Instead of an endless band a series of rollers mounted on rotary arms may be provided to open and close respectively portions of the elastic connection. When the stage vessels are other than vertical the material may be transferred by a conveyer or worm. During the passage of substances through the stage vessels a treatment may be carried out at any place at the same time, for example heating or cooling or treatment with gases, vapours or liquids or a mixing or separation into components. The gas used in the stage vessels may be other than that used in the reaction vessel. The apparatus may be used for feeding carbonaceous material to hydrogenation plants, the reaction residues being removed from the reaction chamber <PICT:0360943/III/1> <PICT:0360943/III/2> <PICT:0360943/III/3> <PICT:0360943/III/4> by similar apparatus. The apparatus is also applicable for introducing metallic substances into the reaction chamber in the manufacture of metal carbonyls from metals and carbon monoxide under high pressure, or for the manufacture of metal carbamates wherein the salts, in the reaction chamber, are acted upon, while suspended in liquid ammonia, with carbon dioxide under pressure.
GB2368230A 1930-08-07 1930-08-07 Improvements in and apparatus for introducing and withdrawing solid substances into and out of vessels containing a medium under high pressure Expired GB360943A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2368230A GB360943A (en) 1930-08-07 1930-08-07 Improvements in and apparatus for introducing and withdrawing solid substances into and out of vessels containing a medium under high pressure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2368230A GB360943A (en) 1930-08-07 1930-08-07 Improvements in and apparatus for introducing and withdrawing solid substances into and out of vessels containing a medium under high pressure

Publications (1)

Publication Number Publication Date
GB360943A true GB360943A (en) 1931-11-09

Family

ID=10199564

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2368230A Expired GB360943A (en) 1930-08-07 1930-08-07 Improvements in and apparatus for introducing and withdrawing solid substances into and out of vessels containing a medium under high pressure

Country Status (1)

Country Link
GB (1) GB360943A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2420392A (en) * 1942-12-21 1947-05-13 Herbert S Simpson Foundry sand reclaiming system and method
US2470744A (en) * 1945-10-22 1949-05-17 Airborne Conveyors Corp Air lock and valve for pneumatic conveying systems
US2693283A (en) * 1950-02-11 1954-11-02 Allied Chem & Dye Corp Air lock
US2703654A (en) * 1948-09-03 1955-03-08 Overton Machine Company Discharge mechanism for vacuum driers
US2826320A (en) * 1954-01-28 1958-03-11 Socony Mobil Oil Co Inc Transfer of granular contact material
US2835272A (en) * 1952-11-25 1958-05-20 Taupin Andre Lock
US2854156A (en) * 1954-11-08 1958-09-30 Socony Mobil Oil Co Inc Hydrocarbon conversion
US2906417A (en) * 1951-09-22 1959-09-29 Rossi Giovanni Material conveying device
US2923575A (en) * 1956-03-19 1960-02-02 Allis Chalmers Mfg Co Fuel feeding mechanism for a gas turbine
US2985324A (en) * 1958-04-21 1961-05-23 Universal Oil Prod Co Apparatus for passing particles from a high pressure vessel
US2990048A (en) * 1959-04-22 1961-06-27 Mervan & Co Apparatus for pumping materials
DE1117555B (en) * 1957-11-05 1961-11-23 Commissariat Energie Atomique Device for the production of pure uranium tetrafluoride

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2420392A (en) * 1942-12-21 1947-05-13 Herbert S Simpson Foundry sand reclaiming system and method
US2470744A (en) * 1945-10-22 1949-05-17 Airborne Conveyors Corp Air lock and valve for pneumatic conveying systems
US2703654A (en) * 1948-09-03 1955-03-08 Overton Machine Company Discharge mechanism for vacuum driers
US2693283A (en) * 1950-02-11 1954-11-02 Allied Chem & Dye Corp Air lock
US2906417A (en) * 1951-09-22 1959-09-29 Rossi Giovanni Material conveying device
US2835272A (en) * 1952-11-25 1958-05-20 Taupin Andre Lock
US2826320A (en) * 1954-01-28 1958-03-11 Socony Mobil Oil Co Inc Transfer of granular contact material
US2854156A (en) * 1954-11-08 1958-09-30 Socony Mobil Oil Co Inc Hydrocarbon conversion
US2923575A (en) * 1956-03-19 1960-02-02 Allis Chalmers Mfg Co Fuel feeding mechanism for a gas turbine
DE1117555B (en) * 1957-11-05 1961-11-23 Commissariat Energie Atomique Device for the production of pure uranium tetrafluoride
US2985324A (en) * 1958-04-21 1961-05-23 Universal Oil Prod Co Apparatus for passing particles from a high pressure vessel
US2990048A (en) * 1959-04-22 1961-06-27 Mervan & Co Apparatus for pumping materials

Similar Documents

Publication Publication Date Title
GB360943A (en) Improvements in and apparatus for introducing and withdrawing solid substances into and out of vessels containing a medium under high pressure
US2080578A (en) Apparatus for treating gases
DE29522033U1 (en) Device for impulse media discharge
US2300849A (en) Sulphuric acid manufacture and apparatus therefor
DE618502C (en) Device for continuous drying and cooling in a vacuum
US3575842A (en) Recovering tar from tar sand
US2941619A (en) Process of and apparatus for separating gas and liquid fractions from petroleum gas oil stream
US2684729A (en) Adsorption process and apparatus
US2799363A (en) Cyclic adsorption process
US3552211A (en) Mixed phase sampling system
US51124A (en) Improved filtering-press
US236265A (en) James semplb and wilkinson ceqssley
US409973A (en) Racking-off apparatus for beer
DE161491C (en)
US2319365A (en) Fractionating apparatus
US441076A (en) Carl steffen
GB451110A (en) An improved process for the transport of solid or solid and liquid substances mixed with vapours and/or gases
GB397128A (en) Improvements relating to apparatus for the recovery by adsorption of gases, vapours or liquids
US642948A (en) Apparatus for sterilizing liquids.
DE202011003222U1 (en) Fluid swirling in the pipe
US363019A (en) Heineich stockheim
US1336264A (en) Process of destructive distillation
US477208A (en) gehrke
FR2255381A1 (en)
US1282407A (en) Apparatus for extracting soluble substances.