Abstract: In the process of transferring coke from a coke oven chamber in a battery of coke ovens to a quenching car, the coke is quenched by a water spray from above. The resulting steam is collected in a hood located above and movable with the quenching car and is either exhausted from the hood and conveyed to a condenser or is condensed in the hood with the condensate being collected, cooled and recirculated to provide the water for the quenching and condensing sprays. The apparatus and method of this invention provides for transferring and quenching the coke without emitting harmful gases and dust to the atmosphere.

Abstract: Method and apparatus for extruding incandescent coke from a coke oven and for quenching the coke prior to transport thereof from the point where extruded. The method and apparatus include enhanced air pollutant emission control characteristics. The apparatus includes an inverted, truncated-pyramid container cradled within the frame of a vehicle similar to that used to transport molten metal. Prior to coke extrusion the vehicle permits indexing of the container under the plane through which the extruded coke falls so as to receive all of such extruded coke. While indexed and immobile, the container is adapted to mate with a correspondingly indexed hood having emission control means adapted to be operable during both the extrusion and quenching of the coke at the indexed position of the container/hood. Use of the present invention, in comparison to the prior art, further minimizes the escape of uncleaned, air pollutant-emitting fume, both by virtue of combustion suppression and exhaust gas cleaning.

Abstract: Heated bulk material, such as coke, is quenched by a liquid flowing from the top downwardly through the bulk material. During the quenching the bulk material is closed off from the atmosphere. The steam forming from the quenching liquid is carried off downwardly in parallel flow with the quenching liquid. For this purpose the amount of quenching liquid distributed over the bulk material is so measured or dosed that it participates completely in the quenching process, whereby the quenching liquid evaporates completely except for a specific residual moisture in the coke. The flow resistance which varies over the base surface of the bulk material is compensated by a carry-off resistance which is inversely proportional to the respective bulk material height. The varying of the flow resistance is due to a bulk material height which changes from one side of the quenching container to the opposite side as a result of an inclined container bottom.

Abstract: A method and apparatus for cooling dustlike or fine-grained reaction residue emanating from a reactor is disclosed. According to the method reaction residue emanating from a reactor passes downwardly into a cooling shaft where it is maintained in the form of a pile of bulk material under a gas pressure of 20 to 200 bars while cooling gas passes upwardly through said cooling shaft in counter-current and is removed at the top of said cooling shaft into the reactor. The apparatus comprises means for effecting cooling of such reactor residue.

Abstract: An apparatus for the dry cooling of coke is disclosed including a vertical cooling chamber having an open bottom, a gas distribution manifold disposed in the bottom of the cooling chamber and a pair of discharge openings for the continuous withdrawal of the cooled coke from the bottom of the chamber. The cooling gas manifold includes upwardly sloping walls which intersect at an apex located generally centrally of the bottom of the cooling chamber. Gas discharge openings extend through these walls and are so disposed as to make cooling gas available across the entire cross-section of the cooling chamber. Individual, closed gas chambers communicate with groups of the gas discharge openings and the flow of gas to each chamber is individually regulated.

Abstract: Method for the reduction of emissions from the wet quenching of incandescent coke in a quenching tower adapted to receive in its base a quench car containing the coke which comprises positioning the car with the coke in the quenching chamber of the tower, effecting a gas seal to substantially prevent air from infiltrating the quenching chamber and ascending the tower, quenching the coke with the resultant generation of steam and other quenching emissions, cooling and cleaning the emissions with water sprays, demisting the cooled emissions, sensing the external and internal pressures of the tower during the quenching process, maintaining a substantially zero gauge internal pressure by controlling the emissions flow exiting the tower and collecting, cooling and recycling the quenching and cooling waters. Apparatus for practicing the method is also disclosed.

Abstract: An apparatus for quenching glowing coke in a coke-quenching container or car, comprises a housing with spaced front and rear vertical walls and vertical end walls at each end having respective entrance and exit openings for the quenching car. The housing also has a ceiling portion adjacent the upper end of a vertically elongated gas chamber defined within the housing and it communicates adjacent the rear wall with an upwardly extending flue. In order to ensure that any sensing devices in the flue are not influenced by the direct radiation from the glowing coke of the quenching car positioned in the chamber, the device includes a baffle extending outwardly from the rear wall and covers a cross-sectional area in the quenching chamber, but leaves a free gas flow cross-section for the flow of quenching gases which is as large as the area covered by the baffle.

Abstract: Abrasion-proof coke forms are produced from bituminous coal, brown coal, or peat in the form of briquets, by preheating the briquets, dehydrating or predrying them, carbonizing them and then cooling them in at least three separate stages in which the briquets are dehydrated indirectly by subjecting them to indirect temperature conditions, producing a temperature gradient in the briquets. The briquets are automatically fed into a shaft tower which includes an upper drying shaft portion made up of a plurality of stacked radiators which include tube elements for the passing of a heating fluid, such as steam, therethrough and which define vertical shaft passages through which the briquet forms are passed downwardly and into a carbonizing shaft which has separate gas channels for directing heating gases therethrough and to a heating flue and which subsequently includes a lower cooling zone through which the briquets pass and then into a discharge channel where they are delivered for classification.

Abstract: A system and method are provided for dry quenching coke while simultaneously eliminating pollutants emitted during coke pushing and quenching operations. The method includes pushing the hot coke from a coke oven into a hooded, mobile coke quench car, drawing the pollutants emitted during the push downwardly through the hot coke contained in the quench car to oxidize the pollutants and produce an inert combustion gas, cooling the hot inert gas and utilizing the heat recovered from the gas, cleaning the cooled inert gas, and returning the cooled cleaned inert gas to the quench car for further passage through the hot coke.

Abstract: This invention is directed to a process for making coke and recovering the heat therefrom for preheating the firing gas to the coke oven. The process involves the use of the coke oven firing gas to extract the sensible heat from the hot coke from the coking oven to both preheat the firing gas for the coke oven and cool the hot coke. Significant economies are achieved in the two-fold function of coke production and heat recovery in accordance with the method disclosed.

Abstract: Hot coke produced in a coke plant is introduced into the lower portion of a sealed interior of a quenching tower. Quenching water is supplied to the hot coke, thereby cooling the hot coke and generating steam and quenching gases which rise from the quenched coke to the upper portion of the interior of the quenching tower. Condensing water is supplied into the upper portion of the interior of the quenching tower, thereby condensing the steam to form quenching water condensate. A water mixture of the condensing water and the quenching water condensate is collected at a midportion of the interior of the quenching tower, and such water mixture is prevented from passing to the lower portion of the interior of the tower. The thus collected water mixture is discharged from the interior of the quenching tower, and the quenching gases remaining in the upper portion of the interior of the quenching tower are removed without being directly discharged into the exterior surrounding environment.

Abstract: A one-spot coke quench car is provided with a coke pile dispersement means to evenly distribute the coke within the car to permit additional coke to be accommodated and as an aid in more uniform quenching. The car has a sloping conduit therein and an exterior water metering valve that is fluidly connected to a pressurized tank of water mounted on the quench car frame. A small quantity (about two gallons) of water is pressurized in the water metering valve which can be opened to allow the small quantity of water to flow immediately and almost instantaneously through the sloping conduit and into the pile of incandescent coke. The water suddenly flashes, explosively, into a large volume of steam, expanding rapidly to disperse the coke within the quench car so that it is more nearly level therein.

Abstract: A method and apparatus for quenching coke which obviates the necessity of using a high energy scrubber for the cleaning of the gases by virtue of quenching the coke in a non-oxidizing atmosphere to drop the temperature of the coke below its ignition point for eliminating the emissions of hydrocarbons, confining the steam and vapor for additional quenching and pressure buildup, cleaning of the steam and vapor of particulate matter, and containing the excess quench water including the breeze resulting from the quench.

Abstract: A method and apparatus for quenching coke which comprises the quenching of the coke in a non-oxidizing atmosphere in a chamber during the push to drop the temperature of the coke below its ignition point for eliminating the emissions of hydrocarbons at the source, confining the steam and vapor for additional quenching within said chamber by virtue of pressure build-up, forcing the steam out of said chamber for direction to condensing means, condensing the steam to eliminate the plume, precipitating particulate matter and dissolving condensables, scrubbing the non-condensables for the removal of sub-micron particulate matter, containing the excess quench water and condensate including the breeze resulting from the quenching and condensing and exchanging the heat from the quench water and condensate for heat recovery.

Abstract: In the dry quenching apparatus for red hot coke, the amount of quenching gas to a cooling chamber is controlled by controlling the speed of rotation of a blower in order to fix a diverging point between the positive pressure and the negative pressure at one point. The pressure around the diverging point is controlled so that the pressure is maintained at 0.+-.5 mm in Aq.

Abstract: A dry coke quenching process comprises the steps of preheating coke from a coke oven to a temperature of not lower than 1200.degree. C. by way of burning over its layer a combustible gas mixed with heated air, cooling the coke first to a temperature of not lower than 700.degree. C. with a mixture of hydrocarbons and water vapor, and then with an inert gas to a temperature of from 200.degree. to 250.degree. C.In the course of operation, coke, heated to a temperature of not lower than 1200.degree. C., is passed to the middle part of a chamber wherein a flow of a gas-steam mixture heated to a temperature of up to 700.degree. C. is introduced in countercurrent relation to the flow of coke. Resulting from the process of conversion of hydrocarbons with water vapor is gas containing hydrogen and carbon monoxide. The blast-furnace coke with a temperature of not lower than 700.degree. C. is passed from a middle part of the chamber to a lower part thereof wherein it is cooled to a temperature of 200.degree. to 250.

Abstract: A process for quenching hot coke discharged from an oven of a battery of coke ovens into a one-spot car. The process utilizes a unique arrangement of two sets of narrow angle spray nozzles to quench the coke. In addition to quenching the coke, one set of spray nozzles initially knocks down the peak portion of the coke pile and distributes the coke so that the exposed surface of the coke is substantially level. The quench liquid discharged through the narrow angle spray nozzles contacts about 50% to about 70% of the substantially level, exposed surface of the hot coke. Sufficient openings are provided adjacent the bottom of the one-spot car to drain the quench liquid to prevent the buildup of quench liquid in the quench car.

Abstract: Cooling water for cooling coke in a coking drum is charged into the interior of the coking drum from a plurality of orifices located on the lateral surfaces of the coking drum so as to uniformly distribute the cooling effect provided by the cooling water.

Abstract: A cylindrical drum having a lining spaced apart from the shell of the drum is rotatably mounted on a frame movable on rails along the coke side of a coke oven battery. A fume shield is fixed to the frame and covers openings in the shell and lining through which hot coke passes, when pushed from a coke oven chamber. A hood is fixed to the structure supporting a coke guide and has a movable portion that coacts with the rotatable shell when coke gravitates into the shell. The drum is rotatable to several operative positions.

Abstract: A carbonaceous residue or char having novel properties is produced from particulate agricultural waste material, such as peanut shells, which upon heating exhibits an exothermic decomposition into an off gas component and a solid component in which the off gas component is more highly reactive to oxygen than is the solid component. By introducing air into the reaction zone whereat the decomposition is effected and controlling the amount of air so introduced such that not all of the off gas component may be oxidized, the preferential reaction of the air with the off gas component will protect the solid component from any significant oxidation while at the same time it will elevate the temperature in the reaction zone sufficiently to effect substantially complete decomposition of the material so that the recovered product is of very high carbon content. At the same time, a temperature gradient is established in the reaction zone which will allow some of the vapor component of the decomposition (i.e.

Abstract: An improvement made to quenching coke during the push wherein the coke is physically opened for increased exposure to the quenching medium.

Abstract: Method and apparatus for receiving and transporting hot coke in a coke oven pushing operation and controlling emissions resulting therefrom comprising a one spot quench car having a receptacle which is tiltable to a coke receiving position, a travel and quench position, and a coke discharging position. A hood structure is provided to confine the gases during pushing and a collecting main removes the gases to a remote location for cleaning thereof.

Abstract: In a dry type method and apparatus for quenching coke wherein hot coke charged in a coke quenching installation is cooled by circulating cooling gas in the installation through a closed circulating system including a blower and a heat exchanger, the composition of the cooling gas is analyzed and compared with a reference gas composition and air or nitrogen gas is supplemented to the closed circulating system in accordance with the result of comparison. A portion of the circulating gas is discharged to the atmosphere when air or nitrogen gas is supplemented. Air is supplemented on the high temperature discharge side of the circulating cooling gas while nitrogen gas is supplemented on the low temperature inlet side. The cooling gas is discharged to the atmosphere before the supplementation of the nitrogen gas.

Abstract: The coke forms are produced in four stages, each constituted by a respective oven chamber, and in which the briquets are, respectively, preheated, dehydrated or dried, carbonized and cooled. Hot gas circuits are provided, in which the hot gas is composed substantially of burnt lean gas of the carbonization, and, for each stage, the hot gases are recirculated in a separate respective circuit. In the preheating, dehydrating and carbonization stages, the hot gases are heated and produced, or supplemented, in a respective separate combustion chamber with the recirculating hot gas in the carbonization stage being supplemented with cooled lean gas from this stage. The recirculating hot gases are dedusted separately in a dust settling chamber in which their flow velocity is reduced to approximately 0.2 to 2.0 m/sec, with the dust being collected.

Abstract: An apparatus and method for performing a continuous thermal treatment of organic carbonaceous materials under controlled pressure in which the feed material is introduced into the system in the form of a slurry, and the level of liquid is maintained at a preselected operating level, serving as a gas-tight seal. The feed material is conveyed upwardly of the liquid operating level and is thereafter introduced into a reaction chamber in which it is heated to within a controlled elevated temperature range under controlled pressure in a manner to effect vaporization of at least a portion of the volatile substances therein, forming a gaseous phase composed of condensible and noncondensible vapors.

Abstract: Retrofit method and apparatus for minimizing the emission of particulate-laden smoke to the ambient atmosphere during the movement of slot-oven-produced, incandescent coke prior to the time it is quenched in an open-topped rail vehicle.A cyclically used, moveable hood is selectively positioned around and over a guide through and from which extruded, incandescent coke drops into an open-top vehicle which concurrently is moving at right angles to the path of the extruding coke. The hood confines potentially air polluting emissions during extrusion. Use is made of the latent heat in the extruded, incandescent coke to make steam out of water introduced within the hood from a plurality of water sprays so as to create a substantial steam atmosphere which envelopes the coke and thereby suppresses combustion when it would otherwise be most extensive. Further, the steam atmosphere is used to screen and protect the apparatus from excessive radiant heat and thereby protect its integrity.

Abstract: A pollutant collection and removal system is provided for use with a horizontally arranged battery of coke ovens. A receptacle having a coke entry opening is positioned in front of the coke guide and receives the total coke pushed from an oven and a hood carried by the support for the coke guide substantially encloses the coke guide and overlies the coke entry opening and enshrouds the discharged coke and pollutants generated during the coke pushing operation. Means are provided for distributing the coke within the receptacle while said receptacle is being maintained stationary (i.e. one-spot) for quenching and, after the pushing operation, the receptacle is moved from the coke guide and transported to a quenching station.

Abstract: In a dry type quenching facility for red hot coke wherein an operation pressure at the upper portion of the quenching station is set up within the range of 0 to +10 mmH.sub.2 O, red hot coke is charged into said station under a reduced pressure of 0 to -30 mmH.sub.2 O, to prevent escape of dust and smoke from said station and thereby prevent polluting of the environment.

Abstract: A column of hot, particulate char from a shaft furnace is moistened with quench water as it moves downwardly into a vessel which it fills and forms a pile. The material in the pile is shifted from a central core at the base of the column to a zone which surrounds the sides and bottom of the column by material flowing from the lower portion of the column; and steam is exhausted from the upper portion of the vessel.

Abstract: In a coke dry quenching system utilizing a waste heat boiler, the sensible heat of bleeder gas exiting from the top of a coke dry quenching station is stored in a regenerator, and when heat input to the boiler falls below a predetermined level the stored heat is conducted to the waste heat boiler, whereby substantially constant heat input to the boiler is maintained.

Abstract: A coke quenching steam generator comprising a vertical, refractory-lined pressure vessel for quenching of incandescent coke and producing useful steam from the sensible heat in the coke. Included in the pressure vessel are pressure-tight doors for receiving and discharging the coke, water sprays for quenching the coke, a hopper for receiving the coke and a gate and feeder for controlling the discharge of the quenched coke. External to the pressure vessel are a crane for lifting containers of incandescent coke to the receiving hopper of the pressure vessel, valves for controlling the flow of steam and water, a high efficiency cyclone for cleaning the steam, a belt conveyor for receiving the quenched coke, pumps, water storage tank, piping and controls.

Abstract: In a coking installation moist coal to be converted into coke is dried and preheated by being contacted by a hot drying gas. The hot coke which is formed is subjected to a dry quenching in which at least a portion of the heat lost by the hot coke during the drying quenching thereof is imparted to the drying gas. There is provided a closed flow circuit for the continual recirculation of a body of drying gas. The closed flow circuit includes a portion in which the drying gas comes into contact with moist coal which is to be dried and preheated. When the drying gas comes into contact with the moist coal water vapor becomes mixed with the drying gas. The water vapor is removed from the drying gas by means of condensation.

Abstract: An improved method of rapid liquid quenching of coke wherein hot coke is distributed on a surface, preferably an inclined surface, and a substantially uniform stream of quench liquid is flowed through said hot coke at spaced apart locations so that the quench liquid penetrates the depth of the bed prior to complete vaporization and percolates through the bed quenching coke as it goes. Particularly good results are obtained by oscillating the stream or streams slowly over the coke.

Abstract: An inclined track adjacent a dry coke cooler includes a counterweighted and pivoted hot coke container hoist that coacts with a hot coke container to raise it to a level above the coke cooler and then to lower it onto the open top of the coke cooler. After the hot coke has been discharged into the coke cooler, the hot coke container is returned to the car on which it travels alongside a coke oven battery to receive coke pushed from an oven chamber.

Abstract: A method and apparatus for the production of coke from coal by a dry distillation operation wherein the coking plant is provided with a computer unit that receives signals from the coal leveling mechanism, the door mechanism, the quenching car mechanism, and a signal value for the time required to achieve the coking of the coal. The computer prevents the opening of any given coking chamber until the minimum coking time has lapsed and the opening of the chamber and discharging and quenching of the coke is correlated to the actual operating conditions rushing at that time. If desired, the charging and emptying operations may be carried out on a completely automatic basis.

Abstract: A method of treating a waste combustion gas from a coke oven comprising the steps of deoxidizing the waste gas, introducing the deoxidized gas into a dry-quenching unit as a gas for quenching red-hot coke, recovering the sensible heat of the red-hot coke given to the gas discharged from the dry-quenching unit for use as a heat source for generating steam and thereafter discharging the gas.

Abstract: A quenching track extends alongside of and away from a coke oven battery, and coke receiving apparatus is movable on the track to a remote location at which supporting structure for the coke receiving apparatus is located. Associated with the supporting structure is conveyor means onto which incandescent coke is discharged from the coke receiving apparatus. Coke on the conveyor means is quenched, and vapors arising from the coke during quenching are conveyed to a stack and are discharged to the atmosphere. Fumes arising from the coke receiving means during discharging of the coke are withdrawn into a gas scrubber and cleaned therein. From the scrubber the cleaned fumes are discharged to the stack and to the atmosphere.Various types of coke receiving means are disclosed, and various types of supporting means and arrangements of conveyors at the remote location are also disclosed.

Abstract: The quenching apparatus includes a collector or receiver positioned above and connected to a quenching vessel. Incandescent coke pushed from a coke oven is deposited in the receiver and fed at a controlled rate from the receiver into the upper portion of the quenching vessel. Nozzles positioned adjacent the top of the quenching vessel spray quenching water on the incandescent coke as it is introduced into the quenching vessel. A suction device is provided adjacent the lower portion of the quenching vessel to draw the vaporized quenching water downwardly through the bed of quenched coke in the quenching vessel and discharge the quenching vapors to the atmosphere. The bed of quenched coke serves as a filter to remove the particulate material from the quenched water vapor.

Abstract: A coke quencher car apparatus comprises a receptacle that is similar to a standard quencher car, but having one internal baffle forming coke compartments, and a frame at each end thereof on which is supported metal curtain material. Each curtain is stretchable to cover one of the coke compartments during and after the pushing of coke is completed. The quencher car is connected to a traction car carrying equipment to remove and clean gases arising from the pushed coke in the quencher car and to move the quenching car.

Abstract: An improved method and apparatus for by-product coke oven operation wherein the problems of pollution caused by charging, oxidation of the coke during pushing, transportation of the incandescent coke to a quenching tower and quenching of the coke is eliminated by the evacuation of the gases during charging, by quenching the coke in a closed system during the push so that the temperature of the coke leaving the guide is below its ignition point; the combustion gases created by the charging and the steam and gases generated by the quenching are extracted and cleaned in a centralized dust collection system. The coke being quenched in a sealed system to a temperature lower than its ignition point, eliminates the oxidation thereof and the efficiency of the oven is increased by being able to push in shorter schedules as the necessity for extra coking time now taken to insure that all the green coke is coked, is obviated.

Abstract: A coke guide spray system on a coke guide disposed on a track between a row of coke side doors and a coke quenching car, the coke guide including an outer frame mounted on wheels for movement along a coke guide track and mounting on the outer frame a track carrying a coke guide chute provided with wheels engaging the track for movement toward and away from an associated coke side door, a water inlet pipe mounted on the outer frame and connected to a source of water under pressure, a first water spray mounted on the outer frame above the coke guide chute adjacent to the end thereof disposed toward the associated coke quenching car, and a second water spray mounted on the outer frame above the coke guide chute and disposed outwardly with respect to the end thereof disposed toward the associated coke quenching car; another system is provided with a hood housing, an induced draft fan and a condensing spray system, while yet another system is provided with a hood having a mist eliminator tower housing a spray cond

Abstract: In the present method the bulk material, especially coke, is maintained at a substantially constant level on a substantially horizontal support surface. The quenching liquid is permitted to flow uniformly through the bulk material for about 45 to 90 seconds until the vapor temperature is cooled down to at least 400.degree.C. The quantity of the quenching liquid which is uniformly distributed over the bulk material is selected so that it evaporates substantially completely, except for a small moisture content in the quenched material. The present bulk material quenching apparatus has a fireproof container resting on a supporting box, the top of which is a grid structure which simultaneously forms a permeable bottom for the quenching container which is provided with a tightly closing cover. A pipe conduit is connected to the cover which has a plurality of conduit outlet openings directed into the container. The box on which the container rests has at least one hinged side wall.

Abstract: Upon discharge from a coke oven, highly heated coke is cooled by charging the hot coke to a shaft cooler wherein it is contacted with an inert cooling gas to a temperature of between 600.degree.-800.degree.F, the coke then being discharged through a pressure retention device and to a quench bunker by means of a feeding device, with the coke further cooled to a temperature of below 300.degree.F by water sprays, while preventing entrance of steam into the shaft cooler. The feed means and quench bunker are enclosed so as to prevent discharge to the atmosphere of steam produced on contact of the spray with the coke as well as particulate material carried thereby. The coke at below 300.degree.F is then fed to a conveyor for removal from the cooling area.

Abstract: In the delayed coking process wherein hot coke is formed by destructive distillation of a petroleum feed in a coking drum to provide solid coke and distillate petroleum products, the method of regulating the rate of quenching the hot coke after the drum is full and coking has ceased which comprises regulating the rate of feeding quench water to the coking drum in accordance with the internal pressure measured within the drum.