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US3969088A Expired / Lapsed US ⏱️ 0.0 years remaining

Formcoke process

Assignee: ULTRASYSTEMS ENGINEERS AND CONSTRUCTORS INCORPORATED A CORP OF
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Filing: 1975-04-28
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Granted: 1976-07-13
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Expires: 1995-04-28
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Abstract

Abstract Raw coal is charred in pre- and post-treatment carbonizers, then pulverized, mixed with pitch, briquetted, re-circulated through the pre- and post-treatment carbonizers with succeeding green coal, cooled, and finally separated from the as yet un-briquetted char.

Inventors

  • 👤 Vaughn Mansfield
  • 👤 Charles M. Whitten

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 18:13
CPC Classifications
C; C10; C10B; C10B49/00; C10B49/02; C10B49/04; C10B53/00; C10B53/08

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 132 words
A process for producing formcoke comprising, charring sized green coal and reducing the volatile content thereof by continuously feeding the same through pre-treatment carbonizer having an oxidizing atmosphere and rapidly increasing the temperature thereof by combustion of primarily volatile matter in the green coal and limited quantities of air, further reducing the volatile content of the char by feeding the same through a post-treatment carbonizer having a reducing atmosphere, passing the char from the carbonizer through a cooler, crushing the cooled char, mixing the crushed char with pitch, forming the mixture of crushed char and pitch into green briquettes, curing and cooling the green briquettes by recycling the same with the sized green coal through at least one of the carbonizers and the cooler, and separating the cooled briquettes from the char.
Claim 2
Dependent Claim 132 words
A process for producing formcoke comprising, charring sized green coal and reducing the volatile content thereof by continuously feeding the same through pre-treatment carbonizer having an oxidizing atmosphere and rapidly increasing the temperature thereof by combustion of primarily volatile matter in the green coal and limited quantities of air, further reducing the volatile content of the char by feeding the same through a post-treatment carbonizer having a reducing atmosphere, passing the char from the carbonizer through a cooler, crushing the cooled char, mixing the crushed char with pitch, forming the mixture of crushed char and pitch into green briquettes, curing and cooling the green briquettes by recycling the same with the sized green coal through at least one of the carbonizers and the cooler, and separating the cooled briquettes from the char.
Claim 3
Dependent Claim 22 words
The process claimed in claim 1, characterized in that the green briquettes are recycled with the sized green coal through both carbonizers.
Claim 4
Dependent Claim 14 words
The process claimed in claim 1, wherein the pre-treatment carbonizer is a static-bed reactor.
Claim 5
Dependent Claim 17 words
The process claimed in claim 3, wherein the static bed reactor is of the horizontal chain-grate type.
Claim 6
Dependent Claim 14 words
The process claimed in claim 1, wherein the post-treatment carbonizer is a shaft furnace.
Claim 7
Dependent Claim 42 words
The process claimed in claim 1, wherein the pitch mixed with the char is derived by removing from the pre-treatment carbonizer low-temperature volatiles driven from the green coal by the said increasing of the temperature thereof, and condensing the removed low-temperature volatiles.
Claim 8
Dependent Claim 26 words
The process claimed in claim 1, wherein the temperature within the atmosphere within the post-treatment carbonizer is maintained at between about 1700° F to 2200° F.
Claim 9
Dependent Claim 25 words
The process claimed in claim 7, wherein the residence time of the green coal and green briquettes in the pre-treatment carbonizer is about twenty minutes.
Claim 10
Dependent Claim 26 words
The process claimed in claim 8, wherein the temperature of the green coal and green briquettes is raised to about 2000° F in the pre-treatment carbonizer.
Claim 11
Dependent Claim 23 words
The process claimed in claim 9, wherein the residence time of the char and briquettes in the post-treatment carbonizer is about 1 hour.
Claim 12
Dependent Claim 35 words
The process claimed in claim 1, wherein the pitch has a softening point of from about 120° F to 230° F, and including the step of heating the pitch and crushed char in the mixer.
Claim 13
Dependent Claim 46 words
The process claimed in claim 1, wherein the green coal is sized to 2 × 0 inch with no more than about 40% being more than 1/4 inch and briquettes are larger in two dimension than the maximum dimension of char emerging from the post-treatment carbonizer.

References Cited (Backward Citations)

US955970A Cited
US1918162A Cited
US3671401A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-07-13 1980-01-12 1980-07-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-07-13 1984-01-12 1984-07-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-07-13 1988-01-12 1988-07-13 $7700.00 Window Closed / Lapsed

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