US2382809A - Coking expanding coal - Google Patents
Coking expanding coal Download PDFInfo
- Publication number
- US2382809A US2382809A US433119A US43311942A US2382809A US 2382809 A US2382809 A US 2382809A US 433119 A US433119 A US 433119A US 43311942 A US43311942 A US 43311942A US 2382809 A US2382809 A US 2382809A
- Authority
- US
- United States
- Prior art keywords
- coal
- coking
- coke
- weight
- expanding
- 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.)
- Expired - Lifetime
Links
- 239000003245 coal Substances 0.000 title description 38
- 238000004939 coking Methods 0.000 title description 15
- 239000000571 coke Substances 0.000 description 12
- 239000000203 mixture Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000000034 method Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000009736 wetting Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 2
- 241001122767 Theaceae Species 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 239000000080 wetting agent Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/04—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition
- C10B57/06—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition containing additives
Definitions
- the general object of the present invention is to provide a simple and efiective method of preparing a low volatile, expanding, or swellin coal for conversion into coke suitable for metallurgical use by high temperature carbonation, without subjecting the coking chambers in which the coke is formed to objectionable stresses as a result of the expansion or swelling of the coal coked therein.
- the coking chamber wall temperatures are customarily of the order of 2500 to 2700 F.
- the invention is adapted for use in coking coals containing not more than 22% of volatile matter and can be used in coking inferior coals such as slack coal and coal screenings or fines, as well as in coking better grades of coal.
- finely divided coal with a moisture content high enough to make the coal crumbly is stirred or agitated to enlarge the spaces between the coal particles so that when a charge of such coal'is placed in the coking chamber in which it is to be coked the weight per cubic foot of the coal in the charge is substantially less than it would be if the charge consisted of the same coal, similarly divided, but in a dry condition.
- the coal is subdivided to such fineness that all of it will pass through a No. '7'(micron 2830) screen, and 80% of it will pass through a No. 10 (2000 micron) screen and at least 40% of it will pass through a No. 40 (420 micron) screen.
- the amount of water in the wet coal mass needed to give the latter its characteristic crumbly condition increases with the fineness of the coal, and its weight may vary between 8% to 20% of the weight of the coal.
- wetting material or agent may be used or, for example, soap may be added to the water, or use may be made of some commercial wetting agent now on the market, such as "Wetanol.
- the coal may be given the desired water content during-or preparatory to the final subdivision of the coal.
- the final subdivision of the coal is effected in a hammer mill, the latter subjects the coal to the stirring action or agitation necessary to make the aggregate air and water filled spaces between the coal particles twenty per cent or so greater than the aggregate air filled void spaces in an equal volume of dry coal of the same composition and fineness.
- the weight of the coal in the wet coal mass charge in the oven chamber should be about forty-two pounds per cubic foot.
- Low volatile, expanding coalprepared for coking in the manner described may be coked in ovens of standard type used in the manufacture or metallurgical coke and operated within the temperature and coking time ranges customarily coking in the manner above described and the strength ofthe coke produced, may advantageously be improved in some cases by adding to the coal from two to five per cent by weight of finely'subdivided coke or coke breeze, and further improvement in the coke produced may be obtained in some cases by adding to the above described coal and coke mixture, an amount of. finely, subdivided pitch equal in weight to about five or six per cent of the weight of the coke in the mixture.
- the coke When coke and pitch are thus added to the coal, the coke may be initially mixed with the pitch and the mixture may then be heated to more or less completely melt the pitch and thereby agglomerate the mixture, after which the agglomerated mixture may then be ground to such fineness that all, or practically all of it will pass a No. 40 (420 micron) screen.
- the method of preparing and coking a low volatile, expanding coal for high temperature carbonization in a coking chamber which consists in finely subdividing the coal to such fineness that about eighty per cent of the coal will pass a No. 10 (1 680 micron) screen and wetting the coal with water to give it a moisture content of from eight to twenty per cent by weight of the coal to thereby form a crumbly mass and agitating said mass and thereby increasing the aggregate volume of the space between the coal particles so that the weight of the coal in a cubic foot of the wetted, coal mass is less than fortyfive pounds, and in coking the coal so prepared in a deep, narrow and horizontally elongated coking chamber of standard type used in the manufacture of metallurgical coke.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Coke Industry (AREA)
Description
Patented Aug; 14, 1945 COKING EXPANDING COAL Carl Otto, Manhasset, N. Y., assignor 'to Fuel Refining Corporation, New York, N. Y., a corporation of Delaware No Drawing. Application March-3, 1942,
Serial No. 433,119
1 Claim:
The general object of the present invention is to provide a simple and efiective method of preparing a low volatile, expanding, or swellin coal for conversion into coke suitable for metallurgical use by high temperature carbonation, without subjecting the coking chambers in which the coke is formed to objectionable stresses as a result of the expansion or swelling of the coal coked therein. In high temperature carbonation, the coking chamber wall temperatures are customarily of the order of 2500 to 2700 F.
The invention is adapted for use in coking coals containing not more than 22% of volatile matter and can be used in coking inferior coals such as slack coal and coal screenings or fines, as well as in coking better grades of coal.
In accordance with the present invention finely divided coal with a moisture content high enough to make the coal crumbly is stirred or agitated to enlarge the spaces between the coal particles so that when a charge of such coal'is placed in the coking chamber in which it is to be coked the weight per cubic foot of the coal in the charge is substantially less than it would be if the charge consisted of the same coal, similarly divided, but in a dry condition.
In the practical use of the present invention, the coal is subdivided to such fineness that all of it will pass through a No. '7'(micron 2830) screen, and 80% of it will pass through a No. 10 (2000 micron) screen and at least 40% of it will pass through a No. 40 (420 micron) screen. The amount of water in the wet coal mass needed to give the latter its characteristic crumbly condition, increases with the fineness of the coal, and its weight may vary between 8% to 20% of the weight of the coal.
To facilitate the thorough wetting of the coal, some suitable wetting material or agent may be used or, for example, soap may be added to the water, or use may be made of some commercial wetting agent now on the market, such as "Wetanol. The coal may be given the desired water content during-or preparatory to the final subdivision of the coal. When the final subdivision of the coal is effected in a hammer mill, the latter subjects the coal to the stirring action or agitation necessary to make the aggregate air and water filled spaces between the coal particles twenty per cent or so greater than the aggregate air filled void spaces in an equal volume of dry coal of the same composition and fineness. In ordinary practice the weight of the coal in the wet coal mass charge in the oven chamber should be about forty-two pounds per cubic foot.
Low volatile, expanding coalprepared for coking in the manner described may be coked in ovens of standard type used in the manufacture or metallurgical coke and operated within the temperature and coking time ranges customarily coking in the manner above described and the strength ofthe coke produced, may advantageously be improved in some cases by adding to the coal from two to five per cent by weight of finely'subdivided coke or coke breeze, and further improvement in the coke produced may be obtained in some cases by adding to the above described coal and coke mixture, an amount of. finely, subdivided pitch equal in weight to about five or six per cent of the weight of the coke in the mixture. When coke and pitch are thus added to the coal, the coke may be initially mixed with the pitch and the mixture may then be heated to more or less completely melt the pitch and thereby agglomerate the mixture, after which the agglomerated mixture may then be ground to such fineness that all, or practically all of it will pass a No. 40 (420 micron) screen.
While in accordance with the provisions of the statutes, I have illustrated and described the best form of embodiment of my invention now known to me, it will be apparent to those skilled in the art that changes may be made in the form of procedure disclosed without departing from the spirit of my invention, as set forth in the appended claim and that in some cases certain tea, tures of myinvention may be used to advantage without a corresponding use of other features.
Having now described my invention, what I claim as new and desire to secure by Letters Patent is:
The method of preparing and coking a low volatile, expanding coal for high temperature carbonization in a coking chamber, which consists in finely subdividing the coal to such fineness that about eighty per cent of the coal will pass a No. 10 (1 680 micron) screen and wetting the coal with water to give it a moisture content of from eight to twenty per cent by weight of the coal to thereby form a crumbly mass and agitating said mass and thereby increasing the aggregate volume of the space between the coal particles so that the weight of the coal in a cubic foot of the wetted, coal mass is less than fortyfive pounds, and in coking the coal so prepared in a deep, narrow and horizontally elongated coking chamber of standard type used in the manufacture of metallurgical coke.
. CARL b'r'ro.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US433119A US2382809A (en) | 1942-03-03 | 1942-03-03 | Coking expanding coal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US433119A US2382809A (en) | 1942-03-03 | 1942-03-03 | Coking expanding coal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2382809A true US2382809A (en) | 1945-08-14 |
Family
ID=23718927
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US433119A Expired - Lifetime US2382809A (en) | 1942-03-03 | 1942-03-03 | Coking expanding coal |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2382809A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2504150A (en) * | 1947-02-18 | 1950-04-18 | Koppers Co Inc | Coking expanding coals |
| US2591496A (en) * | 1946-08-06 | 1952-04-01 | Walter G Berl | Coking coal |
| US2787585A (en) * | 1951-01-29 | 1957-04-02 | Kaiser Steel Corp | Production of metallurgical coke |
| US3010882A (en) * | 1952-07-14 | 1961-11-28 | American Cyanamid Co | Process of extruding anthracite coal to form a metallurgical coke-like material |
| US3140240A (en) * | 1960-07-21 | 1964-07-07 | Consolidation Coal Co | Process for carbonizing coal |
| US3151040A (en) * | 1952-05-23 | 1964-09-29 | Lorraine Houilleres | Process for preparing extremely large cakes of coal for coking |
-
1942
- 1942-03-03 US US433119A patent/US2382809A/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2591496A (en) * | 1946-08-06 | 1952-04-01 | Walter G Berl | Coking coal |
| US2504150A (en) * | 1947-02-18 | 1950-04-18 | Koppers Co Inc | Coking expanding coals |
| US2787585A (en) * | 1951-01-29 | 1957-04-02 | Kaiser Steel Corp | Production of metallurgical coke |
| US3151040A (en) * | 1952-05-23 | 1964-09-29 | Lorraine Houilleres | Process for preparing extremely large cakes of coal for coking |
| US3010882A (en) * | 1952-07-14 | 1961-11-28 | American Cyanamid Co | Process of extruding anthracite coal to form a metallurgical coke-like material |
| US3140240A (en) * | 1960-07-21 | 1964-07-07 | Consolidation Coal Co | Process for carbonizing coal |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2382809A (en) | Coking expanding coal | |
| US2640016A (en) | Manufacture of coke | |
| US4186054A (en) | Process and apparatus for producing blast furnace coke by coal compaction | |
| US2234769A (en) | Heat treatment of carbonaceous materials | |
| US2177226A (en) | Method of making coke | |
| US2473987A (en) | Process of coking high volatile coal involving incorporation therein of a limited amount of blast furnace flue dust | |
| US2787585A (en) | Production of metallurgical coke | |
| US2353752A (en) | Preparing coal for conversion into metallurgical coke | |
| US1838882A (en) | Process of producing carbonized particles from coking coal | |
| US2353753A (en) | Coking high volatile coal | |
| JPS5845995B2 (en) | Manufacturing method of artificial caking coal | |
| US4257848A (en) | Apparatus for producing blast furnace coke by coal compaction | |
| US2091711A (en) | Medium temperature carbonization of coal | |
| US1667906A (en) | Manufacture of carbonized fuel | |
| USRE21651E (en) | Method of making coke | |
| US2753243A (en) | Production of titanium tetrachloride | |
| US2399096A (en) | Production of magnesium-containing mixtures | |
| JPH07268348A (en) | Blast furnace coke manufacturing method | |
| US1443618A (en) | Process of making coke | |
| DE2106769A1 (en) | Process and manufacture of foundry coke | |
| US1213763A (en) | Method of manufacturing coke from pitch and the product thereof. | |
| US1407700A (en) | Process of forming fuel | |
| US3300550A (en) | Method of forming graphite articles | |
| GB761153A (en) | Process for the production of aggregates of calcined petroleum coke fines in the form of lumps or moulded bodies | |
| CN115029151A (en) | Coke preparation method and coke |