JPS50114404A - - Google Patents

Info

Publication number
JPS50114404A
JPS50114404A JP50012635A JP1263575A JPS50114404A JP S50114404 A JPS50114404 A JP S50114404A JP 50012635 A JP50012635 A JP 50012635A JP 1263575 A JP1263575 A JP 1263575A JP S50114404 A JPS50114404 A JP S50114404A
Authority
JP
Japan
Prior art keywords
liquid
flow path
particles
flow
wheel
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.)
Granted
Application number
JP50012635A
Other languages
Japanese (ja)
Other versions
JPS613837B2 (en
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
Priority claimed from US05/542,407 external-priority patent/US4017270A/en
Application filed filed Critical
Publication of JPS50114404A publication Critical patent/JPS50114404A/ja
Publication of JPS613837B2 publication Critical patent/JPS613837B2/ja
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02Fixed-bed gasification of lump fuel
    • C10J3/20Apparatus; Plants
    • C10J3/30Fuel charging devices
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00Details of gasification apparatus
    • C10J2200/15Details of feeding means
    • C10J2200/156Sluices, e.g. mechanical sluices for preventing escape of gas through the feed inlet
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00Details of gasification apparatus
    • C10J2200/15Details of feeding means
    • C10J2200/158Screws

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Centrifugal Separators (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Financial Or Insurance-Related Operations Such As Payment And Settlement (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

1483135 Wet separating KAMYR Inc 30 Jan 1975 [31 Jan 1974 20 Jan 1975] 4102/75 Heading B2H [Also in Division C5] A method of delivering to a gasifier vessel 10, Fig. 1, coal, oil shale or lignite of particle sizes falling within a predetermined range of sizes (free of fines), the lower limit of which is approximately “" nominal diameter e.g. in the range “"-2" nominal diameters involves the establishment of a continuous flow of liquid (water or oil and light tar) along a first continuous flow path 20 at low (atmospheric) pressure, feeding coal or like particles from a hopper 42 downwardly through the free surface of the liquid in the chamber 50 forming part of the first flow path, transferring coal particles of the required size in incremental volumes of liquid into a second continuous flow path of liquid 26 at elevated pressure by use of a sluicing aparatus 30 (described below) provided with a screen 92 of the requisite size, and conveying the particles in the liquid of the second flow path by line 70 to a mechanical separator 32 mounted at the inlet 12 to the gasifier vessel 10. In the separator the particles are moved by a screw conveyor 96 upwardly through the free surface of the liquid, thereby falling into the inlet 12. Liquid and entrained fines passing through a screen 98 surrounding the screw conveyor, flow along line 102 to a centrifuge 36 where such fines are removed. The purified liquid is pumped back to the sluicing apparatus. Entrained fines in the first liquid flow are similarly removed by centrifuge 34. The apparatus includes provision for counteracting the net loss of liquid, particularly from the second flow path to the first. The sluicing apparatus, Figs. 2 to 4, consists of a pocketed wheel 72, see Fig. 4, mounted for rotation within a liner 76 having ports 78, 80, 82 and 84 which register with the inlets 52, 64 and outlets 58, 68 to the apparatus, in the first and second flow paths, respectively, see Fig. 2. During filling of a pocket 74 in the rotating wheel 72, fine coal particles are drawn through the peripheral slots in the screen 92. The liner may be provided with peripherally projecting grooves 94 acting as flow breakers adjacent the port openings 80 and 84 of the second flow path. The pocketed wheel 72 may be either cylindrical or tapered with the wheel diameter increasing in the direction of a clearance adjusting hand wheel 88, Fig. 3.
JP50012635A 1974-01-31 1975-01-31 Expired JPS613837B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US43827374A 1974-01-31 1974-01-31
US05/542,407 US4017270A (en) 1974-01-31 1975-01-20 Coal gasification process with improved procedures for continuously feeding lump coal under pressure

Publications (2)

Publication Number Publication Date
JPS50114404A true JPS50114404A (en) 1975-09-08
JPS613837B2 JPS613837B2 (en) 1986-02-04

Family

ID=27031608

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50012635A Expired JPS613837B2 (en) 1974-01-31 1975-01-31

Country Status (11)

Country Link
JP (1) JPS613837B2 (en)
AU (1) AU7756975A (en)
CA (1) CA1060210A (en)
DE (1) DE2503400C2 (en)
FI (1) FI56695C (en)
FR (1) FR2259893B1 (en)
GB (1) GB1483135A (en)
IE (1) IE41132B1 (en)
IT (1) IT1031401B (en)
NO (1) NO750192L (en)
SE (1) SE405013B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3950147A (en) * 1974-08-08 1976-04-13 Kamyr, Inc. Process for feeding coal to a fluidized bed or suspended particle pressurized processing chamber and apparatus for carrying out the same
DE2734728C2 (en) * 1977-08-02 1986-07-31 Metallgesellschaft Ag, 6000 Frankfurt Method for introducing coal into a pressurized gasification reactor
JPH0578671A (en) * 1991-09-20 1993-03-30 Hitachi Ltd Gasification of coal and apparatus therefor

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2669509A (en) * 1948-09-16 1954-02-16 Texaco Development Corp Process for gasifying carbonaceous solids
DE1054199B (en) * 1955-04-29 1959-04-02 Kohlenscheidungs Ges Mit Besch Method for operating the fuel lock of a gas generator
SE300755B (en) * 1964-04-16 1968-05-06 Kamyr Ab
SE324949B (en) * 1965-11-17 1970-06-15 Kamyr Ab

Also Published As

Publication number Publication date
GB1483135A (en) 1977-08-17
CA1060210A (en) 1979-08-14
FI56695B (en) 1979-11-30
IE41132L (en) 1975-07-31
DE2503400A1 (en) 1975-08-14
AU7756975A (en) 1976-07-29
JPS613837B2 (en) 1986-02-04
SE405013B (en) 1978-11-13
SE7500762L (en) 1975-08-01
FR2259893B1 (en) 1979-01-05
FI56695C (en) 1980-03-10
IT1031401B (en) 1979-04-30
IE41132B1 (en) 1979-10-24
FR2259893A1 (en) 1975-08-29
DE2503400C2 (en) 1986-09-18
NO750192L (en) 1975-08-25
FI750251A (en) 1975-08-01

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