Patent US4030982A successfully refreshed from Google Patents.
US4030982A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process of making formcoke from non-caking or weakly caking coals
Assignee: Consolidation Coal Co
•
Filing: 1975-07-10
•
Granted: 1977-06-21
•
Expires: 1995-07-10
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 |