US905693A - Method of briqueting carbonaceous materials. - Google Patents
Method of briqueting carbonaceous materials. Download PDFInfo
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- US905693A US905693A US43100808A US1908431008A US905693A US 905693 A US905693 A US 905693A US 43100808 A US43100808 A US 43100808A US 1908431008 A US1908431008 A US 1908431008A US 905693 A US905693 A US 905693A
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- briqueting
- coal
- heating
- carbonaceous materials
- heated
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
Definitions
- WALTER T. GRIFFIN OF LIh-IOGES, FRANCE; JAMES EDDY BLAKE, ISABELLE S. GRAVES, A-ND' CHARLES H. CLARKE EXECUTOB-S OF SA-ID WALTER 'I. GRIFFIN, DECEASED.
- the heating of the coal has another strik-- ing advantage, in that the more volatile hydrocarbons are driven off during the heating.
- These hydrocarbons when the coal is burned in the ordinary Way, are volat'ilized by the heat of the furnace before the temperature of the coal has been raised to the point of ignition, and they then pass off in the form of smoke. Afterwards the coal ignites, and later these hydrocarbons, if any still remain in the coal, are consumed in the furnace in- But in theare not wasted, but are conducted from the oven to the furnace itself and there burned, heating other quantities of briqu'eting material; or they may be conducted elsewhere to be utilized in any desired manner.
- Fi' ire 1 is a. diagrammatic view thereof, and 2 is a longitudinal section of a heating apparatus.
- 1, 2, are two furnaces, so that two differentkindsof coal may be heated simultaneously.
- the materials are fed into the hoppers 3, 4, from which they are carried through the ovens and finally discharged into the con- I t aining a screw conveyer 8, which carries the may be substantially all anthracite, with a i material through the upper chamber of'the oven, above the baffle 10.
- the comparatively low heat of this chamber converts into. steam such moisture as the material contains, and as the warmed material drops into 5 the second hopper 11 the steam escapes into the air. This extraction of the moisture is of special value in dealing with lignite, which contains a considerable proportion of water.
- the material is carried through the pipe 12 in the middle chamber above the batfle 13, by the screw 14, and is there subjected to a higher temperature.
- the lighter hydrocarbons begin to volatilize, but are carried along with the mate- 15 rial to the third conduit 15.
- the latter alsocontains a screw,.16, which carries the material through the lower chamber 17, in which the temperature is still higher. In this chamber the material receives its final heating and. still more of the hydrocarbons are freed.
- the gases pass out through a ipe 18 and may be elivered therefrom to t e grate 19, by a pipe 20, or may be conducted to a gas holder or other device not shown.
- the semi-plastic sticky material is discharged into the conduit 5, where it may be mixed with material from the other furnace 2. If the coal treated in the latter is of same kind as in the other it may be heated to the same temperature and carried through the furnace at the same s eed, but if the materials in the two are d' erent, as soft and hard coals, or different kinds of soft coal, one
- i 85 furnace may be heated. less than the other and the speed of the material't-herethrough regulated (as by varying the rate of rotation of the screw conveyers), so that the heated material will be delivered to the conduit in the proportion desired for the best combination with 'the other.
- the conduit 5- discharges into. one or more bri ueting machines, as for example, those-in icateddiagrammatically at 21 and 22.
- the mixing 0 cooler material with the more highly heated mass may of itself be sufficient to effect the de- I sired chilling, -or will at least assist in the same.
- the charge for the briqueting machines accumulates above the valve 27 during which the hydrocarbon gases have time to escape into the pipe 18. Where the pro er quantity has been deposited, the upper va vs is closed and the lower one opened, delivering the charge to the briqueting machines without waste of gases, which have had time to pass up into the pipe 18.
- the momentary detention in the valve chamber also facilitates the chilling of the heated material.
- the material may be discharged directly into the briqueting machines, if desired, the valves 26, 27 being left open for that purpose, but for the reason stated I prefer the method just outlined.
- the herein described method of briqueting carbonaceous materials which consists in heating the material to evaporate substantially all the moisture therein, permitting the evaplorated'moisture to escape, continuing the eating at a higher temperature to volatilize the li hter hydrocarbons contained in' the materia and bringing the material to a semi-plastic or sticky condition short of coking, and then forming the material into blocks, as set forth.
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
Description
W. T. GRIFFIN, DEGD.
J. E. BLAKE, I. s. GRAVES 8n 0. 11. CLARKE, EXEGUTOES. METHOD OF BRIQUETING GARBONAGEOUS MATERIALS.
APPLICATION FILED FEB. 21, 1905. RENEWED MAY 5, 1908.
905,693. Patented Dec. 1, 1908.
,2 SHEETS-SHEET 1.
g L Hi W. T. GRIFFIN, DEGD. J. E. BLAKE, I. s. GRAVES &: o. n. CLARKE, ExEoUToEs. METHOD OF BRIQUETING OARBONAGEOUS MATERIALS.
APPLICATION FILED F2121, 1905. RENEWED MAY s, 1908.
Patented Dec. 1, 1908.
2 SHEETS-SHEET 2.
N m JV w pr I A M AJ. m l n .w\ [Y RN .QN m A :W Q Q a 3 *N QM a UNITED srar zs rarnnir OFFICE.
WALTER T. GRIFFIN, OF LIh-IOGES, FRANCE; JAMES EDDY BLAKE, ISABELLE S. GRAVES, A-ND' CHARLES H. CLARKE EXECUTOB-S OF SA-ID WALTER 'I. GRIFFIN, DECEASED.
METHOD OF BRIQUETING CARBONACEOUS MATERIALS.
Specification of Letters Patent.
Patented Dec. 1, 1908.
Application filed February 21, 1905. Serial No. 246,800. Renewed May 5, 1908. Serial No. 431,008.
To all whom it may concern:
Be it known that I, WALTER T. GRIFFIN, a citizen of the United States, residing at Li" moges, Department of Haute-Vienne, France, have invented a certain new and useful Method of Briqueting Carbonaceous Materials, of which the following is a specification, reference being had to the drawings accompanying and forming part of the same. 7
In the manufacture of briquets from pulverized or granular carbonaceous materials it has heretofore been necessary to employ as a binder some material other than the carbonaceous material itself, such as tar, molasses, etc. I have found, however, that with the possible exception of anthracite, the coals may be briqueted satisfactorily without the use of a special binder. I have also found that bituminous coal may be used as a binder for anthracite coal with the most satisfactory results.
In carrying out my method I heat the bituminous coal to a pointbelow the temdegrees above the other, the coherence of the In fact= perature at which coking takes place, but at which the coal acquires a slightly plastic consistency. The temperature at which the desired degree of plasticity is produced cannot be stated with definiteness, as it depends entirely on the proportion of bituminous material in the coal. Thus very soft ca-nnel may not require more than 200 F., whereas a'harder coal may need to be heated to something like 500 F. The degree necessary for the best results may in any case, however, be readily ascertained by heating a small portion or sample of the coal which is to be briqueted, and observing the temperature at which it becomes sufficiently plastic. After the coal has been heated I chill it slightly, either by artificial means or by simple exposure to the atmosphere,'until it begins to harden again, that is, until it begins to lose its plastic or sticky consistency. in condition for compression into blocks or briquets. The briquets thus prepared will It is then I be found to be firm and durable, and to re- I tain their form well while burning. also found that by llllXlllg wlth the carbonaceous material, which is to be briqueted, a
I have 1 quantity of anthracite coal heated to a tem perature about one hundred to two hundred particles is much more tenacious. the coherence is so great that the briquets comparatively small proportion of bituminous coal as a binder. I have obtained excellent results with 95% anthracite heated to about 500, and 5% cannel heated to about The best proportions for articular coals may readily be ascertained y testing samples thereof, as will be understood.
The heating of the coal has another strik-- ing advantage, in that the more volatile hydrocarbons are driven off during the heating. These hydrocarbons, when the coal is burned in the ordinary Way, are volat'ilized by the heat of the furnace before the temperature of the coal has been raised to the point of ignition, and they then pass off in the form of smoke. Afterwards the coal ignites, and later these hydrocarbons, if any still remain in the coal, are consumed in the furnace in- But in theare not wasted, but are conducted from the oven to the furnace itself and there burned, heating other quantities of briqu'eting material; or they may be conducted elsewhere to be utilized in any desired manner.
Any suitable apparatus may be employed for carrying out my process, but that shown in the accompanying drawings gives excellent results and is the one I prefer.
Fi' ire 1 is a. diagrammatic view thereof, and 2 is a longitudinal section of a heating apparatus.
1, 2, are two furnaces, so that two differentkindsof coal may be heated simultaneously. The materials are fed into the hoppers 3, 4, from which they are carried through the ovens and finally discharged into the con- I t aining a screw conveyer 8, which carries the may be substantially all anthracite, with a i material through the upper chamber of'the oven, above the baffle 10. The comparatively low heat of this chamber converts into. steam such moisture as the material contains, and as the warmed material drops into 5 the second hopper 11 the steam escapes into the air. This extraction of the moisture is of special value in dealing with lignite, which contains a considerable proportion of water. From the second hopper the material is carried through the pipe 12 in the middle chamber above the batfle 13, by the screw 14, and is there subjected to a higher temperature. Here the lighter hydrocarbons begin to volatilize, but are carried along with the mate- 15 rial to the third conduit 15. The latter alsocontains a screw,.16, which carries the material through the lower chamber 17, in which the temperature is still higher. In this chamber the material receives its final heating and. still more of the hydrocarbons are freed. At the end of the conduit 15 the gases pass out through a ipe 18 and may be elivered therefrom to t e grate 19, by a pipe 20, or may be conducted to a gas holder or other device not shown. From the conduit 15 the semi-plastic sticky material is discharged into the conduit 5, where it may be mixed with material from the other furnace 2. If the coal treated in the latter is of same kind as in the other it may be heated to the same temperature and carried through the furnace at the same s eed, but if the materials in the two are d' erent, as soft and hard coals, or different kinds of soft coal, one
i 85 furnace may be heated. less than the other and the speed of the material't-herethrough regulated (as by varying the rate of rotation of the screw conveyers), so that the heated material will be delivered to the conduit in the proportion desired for the best combination with 'the other. The conduit 5- discharges into. one or more bri ueting machines, as for example, those-in icateddiagrammatically at 21 and 22.
As before stated, I prefer to chill the material slightly before briqueting. This may occur in sufficient degree in the conduit 5; during the passage therefrom into the hoppers 23, 24:;1n the briqueting machines themselves; by means of an air blast, as diagrammatically indicated at 25; 'or in an other convenient manner. The mixing 0 cooler material with the more highly heated mass may of itself be sufficient to effect the de- I sired chilling, -or will at least assist in the same.
I prefer to provide the supply conduit 5 with two valves, as 26, 27, so that it need not be at any time in communication with air. The charge for the briqueting machines accumulates above the valve 27 during which the hydrocarbon gases have time to escape into the pipe 18. Where the pro er quantity has been deposited, the upper va vs is closed and the lower one opened, delivering the charge to the briqueting machines without waste of gases, which have had time to pass up into the pipe 18. The momentary detention in the valve chamber also facilitates the chilling of the heated material. Of course the material may be discharged directly into the briqueting machines, if desired, the valves 26, 27 being left open for that purpose, but for the reason stated I prefer the method just outlined.
From the foregoing it will be seen that my method produces bri uets which contain only coal, (or other car onaceous material), without the use of a special binder.. At the same time the briquets thus made are so firm, wear but slightly in handling, retain their form admirably in burning, and they are also practically smokeless. The method itself. is mexpensive in practice.
It will be understood, of course, that the method may .be varied somewhat without departure from the proper scope of my invention and that being a method or process, the invention is independent of any particular apparatus for performing it.
What I claim is:
1. The herein described method of briqueting carbonaceous materials, which consists in heating the material to evaporate substantially all the moisture therein, permitting the evaplorated'moisture to escape, continuing the eating at a higher temperature to volatilize the li hter hydrocarbons contained in' the materia and bringing the material to a semi-plastic or sticky condition short of coking, and then forming the material into blocks, as set forth.
2. The herein described method of briqueting carbonaceous materials, which consists in heat' the material to evaporate-substantially a the moisture therein, permitting the eva orated moisture to escape, continuing the heating at a higher temperature to volatilize the lighter hydrocarbons and bring the material to a semi-plastic or sticky condition no short of coking, conducting ofi the volatilized hydrocarbons, chilling the material till it begins to set, and then forming it into blocks, as set forth.
3. The herein described method of briqueting carbonaceous materials, which consists in heating one material to a semi-plastic or sticky condition short of coking, heating to a different temperature another material having a d'ifierent pro ortion of bitumen, mixing the materials, an forming the mixture into blocks, as set forth.
I 4. The herein described method of briqueting carbonaceous materials, which consists in heating one material to a semi-plastic or sticky condition short of coking, heating to a higher temperature another material containing a smaller roportion of bitumen, mixing the materia and forming the mixture into blocks, as set forth.
a 5. The herein described method of making minous coal to a semi-plastic or sticky con- 10 fuel briquets, which consists in heating bitu dition short of coking, heating anthracite minous material to a semi-plasticor sticky coal to a temperature higher than .the other, condition shortof coking,heating a non-bithe two, and forming the mixture 5 tuminous material to a higher temperature, into b ocks, as set forth.
mixing the materials; and forming the mix- WALTER T. GRIFFIN. [L. s.] ture into blocks, as set forth. Witnesses:
6. The herein described method of making I. S. GRAVES,
fuel briqnets, which consists in heating bitu- G. GOUTERON
Priority Applications (1)
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US43100808A US905693A (en) | 1908-05-05 | 1908-05-05 | Method of briqueting carbonaceous materials. |
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US43100808A US905693A (en) | 1908-05-05 | 1908-05-05 | Method of briqueting carbonaceous materials. |
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US905693A true US905693A (en) | 1908-12-01 |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2424012A (en) * | 1942-07-07 | 1947-07-15 | C D Patents Ltd | Manufacture of molded articles from coal |
US2825679A (en) * | 1948-03-30 | 1958-03-04 | Baum Kurt | Briquetting of coke by direct heating |
US3093463A (en) * | 1960-06-13 | 1963-06-11 | Coal Industry Patents Ltd | Smokeless briquettes |
-
1908
- 1908-05-05 US US43100808A patent/US905693A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2424012A (en) * | 1942-07-07 | 1947-07-15 | C D Patents Ltd | Manufacture of molded articles from coal |
US2825679A (en) * | 1948-03-30 | 1958-03-04 | Baum Kurt | Briquetting of coke by direct heating |
US3093463A (en) * | 1960-06-13 | 1963-06-11 | Coal Industry Patents Ltd | Smokeless briquettes |
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