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Process of making formcoke from non-caking or weakly caking coals

Assignee: Consolidation Coal Co
•
Filing: 1975-07-10
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Granted: 1977-06-21
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Expires: 1995-07-10
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Abstract

Abstract Formcoke suitable for use in a blast furnace is made from a non-caking or weakly caking coal by converting the coal to an agglomeratable material consisting essentially of a blend of the entire product (without separation of extract and undissolved solids) obtained by solvent extraction of the coal in the presence of hydrogen and a suitable amount of hydrocarbonaceous solids. The agglomeratable material is agglomerated under low temperature carbonizing conditions and the agglomerates are thereafter calcined to produce strong formcoke.

Inventors

  • 👤 Everett Gorin
  • 👤 William A. Jasulaitis
  • 👤 Frank W. Theodore
  • 👤 George E. Wasson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 03:57
CPC Classifications
C; C10; C10B; C10B53/00; C10B53/08; C10B57/00; C10B57/08

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 216 words
In the process of making formcoke from a normally non-caking or weakly caking coal wherein a mixture of carbonaceous solids and carbonaceous binder derived from said coal is tumbled under adiabatic conditions at an elevated temperature in a rotary kiln adapted to rotate about its longitudinal axis, to thereby form agglomerates having a predetermined size which are thereafter calcined to produce formcoke suitable for use in a blast furnace, the improvement comprising: a. subjecting said coal, in a finely divided state, to solvent extraction in a solvent extraction zone in the presence of hydrogen under extraction conditions to thereby produce a product consisting of an effluent gas and an effluent slurry; b. subjecting said effluent slurry to distillation in a solvent recovery zone, to thereby recover at least part of the solvent as distillate; c. blending the undistilled remainder of said effluent slurry and any feed coal and any pitch that may be added, with sufficient hot char to maintain the blended product at a forming temperature between about 385° and 475° C. in said rotary kiln; d. tumbling said blended product in said rotary kiln until agglomerates of predetermined size are formed; and thereafter e. heating said agglomerates in a calcining zone until formcoke is produced which is suitable for use in a blast furnace.
Claim 2
Dependent Claim 216 words
In the process of making formcoke from a normally non-caking or weakly caking coal wherein a mixture of carbonaceous solids and carbonaceous binder derived from said coal is tumbled under adiabatic conditions at an elevated temperature in a rotary kiln adapted to rotate about its longitudinal axis, to thereby form agglomerates having a predetermined size which are thereafter calcined to produce formcoke suitable for use in a blast furnace, the improvement comprising: a. subjecting said coal, in a finely divided state, to solvent extraction in a solvent extraction zone in the presence of hydrogen under extraction conditions to thereby produce a product consisting of an effluent gas and an effluent slurry; b. subjecting said effluent slurry to distillation in a solvent recovery zone, to thereby recover at least part of the solvent as distillate; c. blending the undistilled remainder of said effluent slurry and any feed coal and any pitch that may be added, with sufficient hot char to maintain the blended product at a forming temperature between about 385° and 475° C. in said rotary kiln; d. tumbling said blended product in said rotary kiln until agglomerates of predetermined size are formed; and thereafter e. heating said agglomerates in a calcining zone until formcoke is produced which is suitable for use in a blast furnace.
Claim 3
Dependent Claim 48 words
A process according to claim 1 wherein said extraction conditions of said solvent extraction zone are as follows: ______________________________________ Temperature, ° C. 400 - 450 Pressure, Kg/cm.sup.2 30 - 200 H addition, Wt. % MAF coal 0.70 - 2.5 Solvent to coal (wt. ratio) 1.5 - 3.0 ______________________________________
Claim 4
Dependent Claim 19 words
A process according to claim 2 wherein sufficient solvent is left in said effluent slurry to render it pumpable.
Claim 5
Dependent Claim 18 words
A process according to claim 3 wherein said hot char includes comminuted off-size agglomerates from said rotary kiln.

References Cited (Backward Citations)

US2556154A Cited
US3162594A Cited
US3401089A Cited
US3562783A Cited
US3748254A Cited
US3791956A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-06-20 1980-12-20 1981-06-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-06-20 1984-12-20 1985-06-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-06-20 1988-12-20 1989-06-21 $7700.00 Window Closed / Lapsed

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