US1908911A - Oven for carbonizing coal briquettes - Google Patents

Description

May 16, 1933- H. F. MAUREL OVEN FOR CARBONIZING COAL BRIQUETTES lulll Mar-e C 67 i? Filed March 51, 1950 Patented May 16, 1933 lif- HENRY F. MJUREL, OF PROVIDENCE, RHODE SLANBV, .ASSG-NGR T0 .'AUREL IVEST- MENT CORPORATION, GF PROVIDENCE, RHODE ISLAND, A CORPORATION F RHODE ISLAND OVEN FOR CARBONEZING'COL BRQUETTES Application filed MarchkSv., 19@ Serial No. 440,359.

This invention relates to the manufacture of briquettes made from ground fuel, particularly low grade anthracite combined with hydro-carbons used as a binder. Such briquettes require treatment in an oven having a distilling zone and a baking or hardening zone and an apparatus has been Vprovided for treating the brique'ttes in bulk in such a way as to reduce the length of the apparatus.` One of the principal objects of this invention is to provide means whereby the briquettes can be subjected to heat in two zones only, a distilling zone and a hardening or baking zone, without undue length and without the use of the additional apparatus.

The invention also involves the method and means whereby the briquettes aresubjected to their highest temperature when they first entered the oven and the tempera# ture is maintained until distillation has progressed to the point desired. The temperatures to which they are subjected as they progress further through the oven are then X lowered until finally, before Vthey leave the oven, they are subjected to a temperature lower than that of the briquettes themselves, which subsequently acts as a cooling-me diuin. The invention also involves the elimination of a water seal through which the briquettes have been previously passed just before they are discharged from the oven. The improvement here involves the elimination of this wetting of the briquettes and the necessity of subsequent removal of moisture and yet means is provided for preventing transfer of heat or interiniXtui-e of gases from one portion of the oven to another and particularly from the outlet back into the interior.

Other objects and advantages of the invention will appear hereinafter.

Reference is to be had to the accompanying drawing, in which V Fig. 1 is a longitudinal sectional view, partly diagrammatic, of a complete oven constructed in accordance with this invention, showing only thev end at which the briquettes are introduced and discharged; and

Fig. 1qu isa similar view constituting a continuation of Fig. 1 and illustrating the other end ofthe oven.

rf'he invention is designed to be applied to that type of ground coal briquettes in which the coal is miXe/d'with hydrocarbon oils constituting a binder, formed into briquettes, and deposited on anendless conveyor. The conveyor passes through a carbonizing oven lfor the'purpose of treating the briquettes, first to drive off thevolatile constituentsof the `binder and coal, and second, to harden the binder and bring the briquettes into suitable condition for handling and use.

The invention is shown in a form in lwhich a carbonizing oven is provided,

formed at the intake-end with an uptake 11 into which an endless conveyor 12 is introduced through a water seal 13. As will be understoed from the diagrammatic showing at the right in Fig. 1, the endless conveyor 12 is provided with a series of buckets 14 pivotedto the conveyor at 16v and adaptedto re ceive the briquettes in a more or less plastic form and introduced from chutes coming from the machines in which the briquettes are molded but are not shown.v Thel Vconveyor passes around into the water seal and then through the up-take 11 to the top of the oven. The conveyor is supported at various points by suitable sprocket wheels or the like and passes horizontally along the top of the oven from one end-to the other in the first strand and then backwardlyy and forwardly several times from'the top downvv'ardly. VFinally it comes to a floor or partition 17 extending from the' front end of the oven nearly tothe rear end. The chain comes back under this floor or partition and i discharged into a conveyor 22 which takes other end of the oven, into another header 27 which discharges downwardly into a header 28. vThis header is connected by pipes 29 like the pipes 26 to a similar header 30 at the other end. yIt will be seen that the secondstrand `of the conveyor passes backwardly toward the front between these two sets of pipes 26 and 29. The header 30` discharges into the upper half of a header 31 directly beneath it Aand a single series of pipes 32 extends from this header 31 to the oppositeend of the oven. The ends of these pipes are connected by U-shaped couplings with another series of'pipes33 so that the products of combustion pass backwardly in the latter tothe lower half of the header 31.` This is connected with the upper half of another` header 34 which by pipes 35 and 36 in the same way conduct heat back to the lower half ofy this header 31 which fdischarges the heat either outcfmally into the waste stack orinto a'cool gas intake37. Preferably the latter method is employed.

Thereis no connection betweenthe lower half and the upper .half of the headers 31 and 34 and the circulation of the heat in' these two series of pipes 32, 33, 35 and 36 is different, as will. be clear, from the circulation in the pipes 26 and 29.

The different strands of the conveyor pass between the pipes in themanner shown. It will 4be observed that the. direct heat of the products of combustion n does not as yet come into contact with the briquettes. It willv also be observed that the hottest heat from the furnace comes in at 25 and bythe time it gets down to the outlet 38, these gases .necessarily have cooled off somewhat. Furthermore, theheat in the oven rises naturally and the whole process results in applying the maximum volume of heat to the briquettes carried by the first strand of the conveyor at the top of the oven. perature lwhich may be convenientlybrought up to about 700o F. is Vmaintained until distillation has progressed as far as desired and then the temperatures in the spaces below will gradually fall until, whenin the bottom of the oven, that is,`in the cooling zone below the floor. 18, the temperature will be vapproximately 100o F. This is cooler than the briquettes and therefore this is a cooling zone. Y

The conveyor passes back under the floor 18to the rear end of the oven and mechanical` sealing-plates 40, freely pivoted at 44, are employedfto prevent the escape of the products' "of combustion from the cool gas intake This tem* Y 37 into the part of the oven above the floors 18 and 19. In other words, the briquettes are heated by indirect heat in the distilling zone above these floors and heated or cooled by the direct products of combustion, mixed or not with air, in the cooling Zone. The hardening takes place partially by the action of the air and the gases coming in at 37 on the binder of the briquettes. It is desired to have these gases and air flow throughout the area ofthe oven through which the conveyor passes to come into Contact with the briquettes repeatedly; For that reason, alternating baiiies 11 are employed above and below the return strand of the conveyor. These gases finally ,escape through the olftalre 42. -I have shown a series of offtalies a3 having dampers which can be openedl and Y closedA to exhaust the products of distillation at` different elevations in the oven. Y

In describing the apparatus, I have described also the process andthe operation in full. 'By the means shown, the briquettes are first-,brought up to the maximum degree ofgheat which is maintained until distillation hasf.prog1essed as far as desired and whenthe temperature is reduced as they pass down through the oven. All elements of the device tend to retain this relationship and there is nothing to disturb it, such as having the gases or heat pass in the wrong way through the oven. The briquettes, after having been heated to their highest temperature A,and subjected to that temperature as longas required are cooled down in the hardening Zone. where they are subjected to the action of spent products of combustion containing air to harden and oxidize the briquettes sutliciently to permit of their being handled, shipped and sold in the condition in which they are delivered from this apparatus. 1 l

Although IV have illustrated and described only a single form of the apparatus 'for carrying out this method, I am aware ofthe fact that other modifications can be made therein by any person skilled in the art without departing from the scope of the invention as expressed in the claims. Therefore, I do not wish to be limited to all the details of construction herein shown and described, but what I do claim ist--T 1. The combination of an endless conveyer having Abuckets for receiving fuel briquettes for treatment, of Va carbonizing oven having means therein for guiding said conveyer across the topof it and back and fort-h a number of'strands to the bottom of the oven, a series of headers located transversely and oppositely under the several strands ofthe conveyor, conducting pipes extending from one set of headers to the other headers, means for introducing heated gases into one of said headers at the top, wherebythe gases will be moved along the top, means for connecting the two headers at the opposite end of the oven adjacent to each other, whereby the gases will flow back through the pipes to one header, and means for keeping the gases from contact with the atmosphere of the oven so that the briquettes will be subjected to a high heat when they first enter the oven and will gradually be cooled off but still subjected to a. degree of heat less than the maximum as they pass down through the oven.

2. The combination of an endless conveyer for receiving fuel briquettes for treatment, of a. carbonizing oven having ends, means therein for guiding said conveyer across the top of it and back and forth in a number of strands to the bottom of the oven, a series of headers at opposite ends of the oven under the several strands of the conveyor, horizontal conducting pipes extending from the headers at one end of the oven to the headers at the other end, means for introducing heated gases into the header at the top, and means for connecting the two headers at the opposite end adjacent to each other.

3. The combination with a carbonizing oven, of an endless conveyer having buckets thereon for receiving and carrying ground coal briquettes, said conveyer being adapted to pass directly to the top of the oven and then back and forth along the oven in a series of horizontal strands and then finally te pass out adjacent the bottom, a plurality of pipes for conducting products of combuslion, without admitting them into the atmos- .(l. phere of the oven at the top gradually down toward the bottom of the oven so that the top strand of theconveyer will be located in an atmosphere of the highest'temperature and the temperature will gradually diminish all the way to tie bottom of the oven, this part of the oven constituting a distilling zone, the conveyerl being adapted to pass down to the bot-tom of the oven to an outlet, means for introducing cool products of combustion mixed with air into the atmosphere ot the lower` part of the oven, this part of the oven constituting a hardening zone, and a series of mechanical sealing plates nea the bottom of the oven comprising plates in an upper series and lower series between which the conveyer passes, exclude the air and gases introduced into the bottom of the oven from the gases in the upper distilling zone. Y

i. ln an apparatus for carbonizing ground coal briquettes, the combination with a carbonizing oven, of a conveyer consisting of plurality of horizontal strands and having buckets for receiving the briquettes, a water seal through which the conveyer enters the oven, the oven having a vertical passage adjacent one end and through which the conveyer passes upwardly in the oven and then across the top to the opposite end of the oven and'back and forth from one end ofthe oven to the other downwardly to the bottom thereof, means for heating the oven between the horizontal strands of the conveyer by indirect heat to ahigh degree at the top of the oven and to lower degrees at the lower parts of the oven, the oven having two partitions in the bottom portion, one extending from one wall nearly to the opposite wall of the oven and the other extending from the opposite wall in the opposite direction, spaced apart, through which space a lower strand of the conveyer passes, plates located between the partitions to practically prevent the exchange of gases from below the lower partition to the oven above the upper partition, and means for introducing cool prodf ucts of combustion directly into the oven below the lower partition.

5. The combination with a carbonizing oven, of an endless conveyer consisting of a plurality of horizontal strands and having buckets thereon for receivingand carrying ground coal briquettes, said conveyer being adapted to pass directly to the top of the f oven and then back and forth along the oven in a general downward direction and then finally to pass out at the bottom at the same end of the oven at which it enters, a plurality of pipes for conducting hot products of combustion, without admitting them into the atmosphere of the oven, horizontally arranged between thedifferentstrands of the conveyer, said conducting means in cluding a header for admitting hot combustion gases at the top, pipes for passing the combustion gases gradually down toward the bottom of the oven so. that the top strand of the conveyer will be located in an atmosphere of the highesttemperature and the temperature will gradually diminish as the conveyer move's down in the oven, the strands of the conveyer being adapted to move downwardly to the bottom of the oven to an outlet, and means for introducing,

products of combustion mixed with air into the atmosphere of the lower part of the oven at a temperature lower than theibri-y quettes so as to cool them ofi.

6. In an apparatus for ground coal briquettes, the combination with a carbonizing oven, of a conveyer having buckets for receiving the briquettes, the conveyer being adapted toL pass up in the oven and then across the top to the opposite i extending from one wall nearly to the op-i carbonizing posite end of. the oven andthe other extendingrfrom. the opposite Wall, in the opposite direction, spaoedvapart, through Which space a lower strand of the conveyer passes,and means for introducing cool products of combustion, loelovvr ythe lowest partition.

In testimony whereof I have hereunto aliXed my signature,

HENRY F. MAUREL

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