SE309023B - - Google Patents

Info

Publication number
SE309023B
SE309023B SE1783766A SE1783766A SE309023B SE 309023 B SE309023 B SE 309023B SE 1783766 A SE1783766 A SE 1783766A SE 1783766 A SE1783766 A SE 1783766A SE 309023 B SE309023 B SE 309023B
Authority
SE
Sweden
Prior art keywords
bed
vapours
char
space
temperature
Prior art date
Application number
SE1783766A
Inventor
J Kass
J Ackers
Original Assignee
Fmc Corp
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 Fmc Corp filed Critical Fmc Corp
Publication of SE309023B publication Critical patent/SE309023B/xx

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/08Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form in the form of briquettes, lumps and the like

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Industrial Gases (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

1,129,061. Carbonizing coal. FMC CORP. 4 Jan., 1967 [12 Jan., 1966], No. 586/67. Heading C5E. A process for producing char and single phase tar which is heavier than water comprises heating coal particles in a fluidized bed to a temperature not greater than 900‹ F. (482‹ C.) to evolve tarry vapours into a space above the bed, heating the vapours in the space to a .temperature in the range 50‹ to 350‹ F. above the bed temperature, and not less than 950‹ F., removing the heated vapours from the space and condensing them, and removing char particles from the bed. The apparatus is similar to that described in Specification 926,213, and includes means for treating the tar, blending it with the calcined char and making briquettes which are cured and coked, and differs from the earlier apparatus only in having means for discharging char fines from the carbonizer to a receiver, and in having an inlet for air to the space above the bed, for partial combustion of the vapours therein. Alternatively or in addition, excess air or oxygen may be supplied to the base of the bed to provide the oxygen for vapour combustion. The coal may be predried, and two fluidized beds may be employed in series, e.g. the first at 600‹ to 800‹ F. and the second at 900‹ F.
SE1783766A 1966-01-12 1966-12-28 SE309023B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US52014166A 1966-01-12 1966-01-12

Publications (1)

Publication Number Publication Date
SE309023B true SE309023B (en) 1969-03-10

Family

ID=24071370

Family Applications (1)

Application Number Title Priority Date Filing Date
SE1783766A SE309023B (en) 1966-01-12 1966-12-28

Country Status (8)

Country Link
AT (1) AT284782B (en)
BE (1) BE692372A (en)
DE (1) DE1671308A1 (en)
ES (1) ES334909A1 (en)
GB (1) GB1129061A (en)
GR (1) GR33289B (en)
NL (1) NL6700229A (en)
SE (1) SE309023B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117534068B (en) * 2023-11-29 2025-07-29 清华大学 System and method for converting catalytic diesel into porous carbon

Also Published As

Publication number Publication date
AT284782B (en) 1970-09-25
DE1671308A1 (en) 1971-10-21
GR33289B (en) 1967-11-21
GB1129061A (en) 1968-10-02
BE692372A (en) 1967-07-10
NL6700229A (en) 1967-07-13
ES334909A1 (en) 1968-03-01

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