Abstract: A process for utilizing waste heat and for obtaining water gas during the cooling of incandescent coke ejected from a chamber oven is described, this process being in two stages. In the first stage, the coke is dry-cooled with a mixture of water gas and water vapor as the cooling gas. This is circulated, and from the circuit the desired waste heat and the desired water gas are extracted. In the second stage, the coke is wet-cooled with water. The water vapor formed is taken off and returned to the environment and/or to the second stage.

Abstract: A column of hot coke from a shaft furnace moves downwardly into a vessel which it fills and forms a pile. A gap is left between the angle of repose of the coke surface and the upper portion of the vessel. Water is sprayed onto hot coke as it enters the vessel. The gap is vented to an exhaust duct. A baffle near the center of the vessel deflects the material to the sides and creates a void in the center of the vessel, which void is also vented to the exhaust duct. More water is sprayed on the coke adjacent the void. Steam pressure in the vessel is reduced by a fan which pulls steam through the exhaust ducts. The steam pressure is regulated by a pressure controller which modulates a damper in the exhaust duct. A temperature controller regulates the flow of quench water to the vessel. This regulates the temperature and moisture content of the material being cooled.

Abstract: The present specification describes and claims a method and apparatus for use in cooling the solid residue of gasification of a reactor operated at a pressure above atmospheric for the gasification of carbonaceous materials. The residue of gasification is conducted out of the reactor into a cooling apparatus located therebelow and flows through the cooling apparatus from the top to the bottom thereof. A cooling liquid is introduced into the solid residue in the upper region of the cooling apparatus and is metered such that the greater portion of the heat contained in the residue is eliminated in the form of heat of vaporization, sensible heat and chemical binding energy with the resultant steam and reaction products produced. The remaining residual heat which corresponds to the difference between the desired final temperature and the temperature after cooling by the liquid, is eliminated by a gas blown into the bottom region of the cooling apparatus and/or by indirect heat exchange.

Abstract: A process for quenching hot coke in a one-spot coke quench car. The process utilizes a unique arrangement of pipes and spray nozzles to quench the hot coke in a substantially watertight coke quench car having a sloping bottom. A plurality of pipes are directed downwardly from a header mounted on the bench side of the quench car to provide solid streams of water onto the shallow coke bed portion at the top of the sloped bottom for a portion of the quench period. After an initial period a flow of water from a plurality of spray nozzles mounted on additional headers is directed onto the substantially horizontal deep coke bed portion for the remainder of the quenching period. The unvaporized quench liquid is retained in the watertight car until the completion of the quench cycle when it is rapidly drained away.

Abstract: Apparatus for servicing coke ovens has a framework movable along the coke oven battery. A horizontally rotatable and vertically pivotable boom has one end mounted on the gantry and a coke oven work tool on the other. The framework includes a coke quenching apparatus and conveying equipment.

Abstract: A pyrolysis process and system produces a solid residue and a clean, enriched fuel gas. In the process, the pyrolytic oil and filter cake are recycled in such a manner as to produce products of optimal value, and to minimize the need for servicing and downtime of the system. Recycling of water recovered in the process may also be employed to achieve enrichment of the gaseous product. The process may be carried ou in such a manner as to produce a non-polluting wastewater stream that can be discharged directly from the system.

Abstract: An improved plant for coal carbonization or gasification of the type having a vessel with reaction compartment, at least one burner at the top of the reaction compartment for the partial combustion of finely-ground coal at a temperature above the ash-melting temperature to produce a product of gas, coke dust and slag or ashes, the compartment having a bottom opening for the discharge of gas-coke dust current from the compartment, and means for separating the product gas is disclosed. A lower chamber is in the vessel underneath the compartment adjacent to the opening. A heating surface in a vertical wall portion of the vessel surrounding the lower chamber, and a slag trap adapted to trap slag arranged in the bottom of the chamber is provided.

Abstract: Preheated bulk material capable of coking is quenched by flowing the quenching liquid through the loose bulk material, whereby the bulk material is substantially closed off relative to the atmosphere. The liquid is applied to the top of the bulk material in a quenching chamber which is closed at its top by a sealed cover and which has an open grating for a horizontal bottom. The steam formed by the quenching liquid and, if formed, any excess quenching liquid are drawn off from the quenching chamber through the open grating. The total quantity of quenching liquid to be supplied as a function of time is controlled by a valve through a control signal depending on the chemical and physical properties constituting bulk material characteristics prior to the heating of the coal. The control signal also takes into account the type of the intended heat treatment in the form of quenching characteristics.

Abstract: A coke quenching plant comprises vertical quenching chambers arranged in a row and each having a coke-charging means installed in the upper part thereof, hoisting shafts, each of which is located opposite a corresponding quenching chamber, and lifts. Each of the lifts is provided with a carriage transporting a body for carrying coke upwards from the hoisting shaft to the coke-charging means, and downwards. Also provided in the plant is a trestle installed along the quenching chambers on the level of the lifts coming out from the hoisting shafts, and a means for transferring the carriage of the lift in horizontal plane along the trestle and perpendicularly thereto.

Abstract: A process for quenching hot coke in a one-spot coke quench car. The process utilizes a unique arrangement of pipes and spray nozzles to quench the hot coke in a substantially watertight coke quench car having a sloping bottom. A plurality of pipes are directed downwardly from a header mounted on the bench side of the quench car to provide solid streams of water onto the shallow coke bed portion at the top of the sloped bottom for a portion of the quench period. After an initial period a flow of water from a plurality of spray nozzles mounted on additional headers is directed onto the substantially horizontal deep coke bed portion for the remainder of the quenching period. The unvaporized quench liquid is retained in the watertight car until the completion of the quench cycle when it is rapidly drained away.

Abstract: A quenching car comprises an open-topped body arranged to carry a load to be quenched. At least a part of the body is composed of walls of hollow construction to receive a liquid cooling medium, such as water. The hollow walls comprise inner and outer plate-like layers separated by reinforcing members which lie internally of the hollow walls, whereby the exposed surfaces of the inner and outer layers are substantially smooth and self-draining. The body is supported by girders of box-section extending along the length of the car.

Abstract: Flue gas discharged from a recuperator or regenerator of a coke oven battery has the steam thereof removed by means of a direct or indirect cooling and condensation operation. After the steam is removed from the flue gas it is then passed through a coke dry cooling plant in direct contact with hot coke therein to form dry cooled coke while simultaneously increasing the temperature of the flue gas. The flue gas is then passed through a coal preheating plant to directly contact and dry and preheat moist coking coal contained therein. The entire system is open, such that a given quantity of the flue gas passes only once through the system. When the temperature of the flue gas as received from a coke oven battery is extremely high, then the flue gas may be subjected to a partial cooling operation prior to the cooling and condensation operation.

Abstract: A method of quenching coke and scrubbing the resulting gases is disclosed in which a supply of hot coke is placed in an enclosed tower having an open top and subjected to water deposited on it from above. The water is first passed through at least one layer of a liquid gas contact body formed of corrugated sheets of material arranged with the corrugations in each adjacent sheet crossing each other. This water passes in countercurrent relation to the gases rising from the quenched coke and, as a result, particulate matter, liquid drops and water-soluble vapors in the gases are removed in the contact body. The gases passing from the contact body are then passed through a mist-eliminator structure to remove water droplets therefrom.

Abstract: A method and apparatus for the wet quenching of coke is disclosed wherein hot coke is sprayed from above with quenching water, the steam generated by the heat of the coke is condensed by a spray of condensation water from the top of the quenching tower, and the hot condensate-water mixture is collected at the bottom of the quenching tower and recirculating to the top of the tower where it is sprayed between quenching operations to be cooled by a counterflowing stream of air. The cooled condensate-water mixture is suitable for reuse as the condensation spray water.

Abstract: The present specification describes and claims a method and apparatus for use in cooling the solid residue of gasification of a reactor operated at a pressure above atmospheric for the gasification of carbonaceous materials. The residue of gasification is conducted out of the reactor into a cooling apparatus located therebelow and flows through the cooling apparatus from the top to the bottom thereof. A cooling liquid is introduced into the solid residue in the upper region of the cooling apparatus and is metered such that the greater portion of the heat contained in the residue is eliminated in the form of heat of vaporization, sensible heat and chemical binding energy with the resultant steam and reaction products produced. The remaining residual heat which corresponds to the difference between the desired final temperature and the temperature after cooling by the liquid, is eliminated by a gas blown into the bottom region of the cooling apparatus and/or by indirect heat exchange.

Abstract: A low pollution, high yield system for receiving and cooling a hot charge of coke from a coke oven comprising aligning the open end of an otherwise closed coke box having its cross section, volume and surface area substantially equal to that of a charge of coke with the discharge end of a coke oven, pushing the coke directly into the coke box, enclosing the coke within the coke box to substantially isolate the coke from atmospheric oxygen and external cooling media, indirectly cooling the coke within the coke box by passing a cooling medium over the exterior surfaces of the coke box and discharging the cooled coke from the coke box. In a preferred embodiment the coke box is constructed of thin sheet metal panels supported by but not rigidly attached to a support structure and equipped with a cooling water reservoir/metering system for cooling the exterior surfaces of the box from the time the coke is pushed into the box.

Abstract: A heat carrier gas is passed through a coke dry cooling plant in direct contact with hot coke therein to form dry cooled coke while simultaneously increasing the temperature of the heat carrier gas. The heat carrier gas is then passed through a coal preheating plant to directly contact and dry and preheat moist coking coal contained therein. The entire system is open, such that a given quantity of the heat carrier gas passes only once through the dry cooling plant and the coal drying and preheating plant. The heat carrier gas may be a flue gas which is passed directly to the coke dry cooling plant without any preliminary pretreatment, and preferably is a flue gas which is supplied directly from a regenerator or recuperator of a coke oven battery. Alternatively, the heat carrier gas may be in the form of a fuel gas which is inert with respect to the hot coke, for example a waste gas or stack gas supplied from an adjacent metallurgical installation, such as a steel mill.

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: 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: An extendible hopper is mounted to the undercarriage of a pusher machine and is operable to be extended to engage the face of the coke oven battery, between the buckstays and just below the door jamb, to catch hot coke that spills out of coke ovens as the door is removed and the pusher ram is retracted. A bin is also mounted to the undercarriage of the pusher machine to receive the hot coke collected by the extendible hopper. Quench sprays are mounted to the bin to quench the hot coke, and suction means are mounted to the bin to draw off pollutants that emanate from the hot coke and the quench thereof.

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: 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: 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: This invention relates to an improved hood for transfer of coke which prevents binding of the retractable section when it is raised or lowered. The outer surface of the fixed hood section is of circular arc-shape and has at least one track extending therealong. A wheel assembly on the retractable section engages the track so as to guide the retractable section concentrically over the fixed section and prevent binding. Preferably the wheel assembly is outboard of the upper edge of the retractable section. A device is then provided to exert force on the wheel assembly toward the track so as to retain contact between the wheel and track as the retractable section is raised.

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: 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 device for collecting emissions rising from a quenching car of a battery of coke ovens which device is displaceable on rails parallel to the battery of coke ovens and a collecting conduit for the emissions of the quenching car. The device includes a withdrawal connection for the emissions which is connectable to desired spots of the collecting conduit. The device also includes a first hood above which there is provided a collector for the emissions which extends in the longitudinal direction of the first hood. At one end of the first hood the collector is provided with a transition or conveying member from the first hood to the collector. This transition or conveying member has associated therewith a pre-adjustable throttle flap.

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: A hood car having a hood, a coke guide, a coke guide car, and a quench train are all provided for movement parallel to a battery of chamber coke ovens between a quench plant and the ovens. The hood car hood has an opening reaching over the loading area of the quench train and is adapted to be connected through extraction ducts to a gas transition device which is movable on a stationary collection duct alongside the coke oven battery and which has an opening at the top. The opening can be sealed by a flexible cover belt which can be lifted off by the gas transition device. The collection duct is connected to a stationary extraction and purifying device which purifies the dirty gases. The movable hood car and the quench train have coupling means, functional in both directions of movement, for coupling together the hood car and the quench train. The hood car has a brake means for automatically stopping the car upon being uncoupled from the quench train.

Abstract: A one-spot hopper, provided with means for developing layers of coke therein, of even depth, is pivotally mounted to a frame that is movable alongside the coke side of a coke oven battery. Extendible and retractable covers close, and seal the hopper from the ambient atmosphere. A cylinder-piston means is used to pivot the hopper and dump coke therein through pivoted side plates of the hopper. Means are provided to also close off and seal the coke pushing operation of the coke oven battery from the ambient atmosphere. At least one perforated conduit extends transversely through the hopper, and a perforated shield is disposed in spaced-apart relation above the conduit. Means is provided for flowing a cooling fluid in the conduit. A duct is fitted to the hopper to provide a means for extracting gases and entrained particulate matter emanating from hot coke deposited in the hopper.

Abstract: An enclosed quenching car movable along a battery of coke ovens and adapted to receive coke from each oven in succession and quench it without polluting the atmosphere. The car includes an enclosure containing a pivotal quenching tank with interior dimensions substantially corresponding to the dimensions of the carbonized coke cake to be accommodated therein. One side of the pivotal tank is formed from a water-permeable grid such that the coke cake within the tank can be rotated into a horizontal plane and the coke completely immersed in water passing through the permeable grid; while dust and gases are extracted without polluting the atmosphere. In this manner, the coke is quenched in such a way that it is yielded in large pieces with a defined uniform water content in the coarse and fine coke.

Abstract: Equipment for receiving and transporting red-hot coke, pushed out of the oven chambers of a chamber coke-oven with vertical flue, and for extracting and purifying the dust-containing gases rising from the coke. The equipment includes duct means and associated suction means for initially extracting the dust-containing gases from an extractor hood and subsequently from the container collecting the hot coke.

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: The device is positioned in a stack arranged above a location where coke quenching is performed. The coke quenching, which takes place below the stack, evolves steam and gases containing solid coke particles or dust, and which must be prevented from passing into the outside atmosphere. The steam and gases flow upwardly through the stack and the device separates the solid coke particles and dust from the steam and gases. The device comprises a support beam carrying a plurality of shutter-like baffles, of plastic material, and liquid spray elements, and which is variable in length and positioned either obliquely or horizontally across the upper portion of the stack. In between successive coke quenching operations, the liquid spray elements are activated to flush the trapped solid coke particles and dust from the shutter-like baffles. The adjustable length of the device provides for the device to be positioned to extend across the stack at varying angles, or even horizontally.

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: A generally cylindrical drum of heat stress and corrosion resistant construction, and having an opening therein, is rotatably mounted on a frame movable on rails along the coke side of the coke oven battery. A movable cover is fixed to the shell and covers the opening in the shell 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 positions. Means are included to quench the hot coke and to extract the particulate laden steam which is generated by the quenching operation. Additional means are included to remove noxious gases and particulate matter which emanates from the hot coke.

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: Coke from a non-recovery type coke oven is pushed onto a downwardly-inclined floor within a smoke hood joined along one edge of the coke oven. The coke is quenched by water discharge nozzles inside the hood. The coke is discharged through a gate at the bottom edge of the floor onto a conveyor after quenching is completed. The smoke and effluent within the hood pass into the top of two interconnected ignition chambers filled with checkerbrick to incinerate the effluent after which it is drawn from the top of the last ignition chamber into a conduit for discharge by a stack. The ignition chambers include walls isolating the flow spaces for the smoke and quenching fumes from the other flow spaces within checker-filled portions that conduct countercurrently partially-burned distillation products delivered by sole heating flues and downcomers from the space above a coal charge in the coke oven chamber.

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: Quenching car having an inclined surface for supporting coke to be quenched, a moveable gate which in a first position retains the coke and in a second position permits discharge of coke from the inclined surface, and a bottom wall which guides the coke from the inclined surface across a space and over the wall of a reservoir carried on said quench car which will catch and hold excess quench water which drains between the inclined surface and the gate means.

Abstract: Delayed petroleum coke is produced by conventional processing, including steaming of the coke in the drum to remove volatile material. After the steaming operation, the coke is quenched by injecting water onto the top of the steamed coke and passing the quench water downwardly through the coke, whereby the coke bed acts as a filter to trap fines which would pass overhead when the normal method of quenching by injecting quench water upwardly is used. Apparatus including retractable spray nozzles extending into the coke drum from the top is described.

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: An arrangement adapting a slatted top to a single-spot quench car. The slats are opened and closed in selected groups.

Abstract: An electrical pulsing unit in the pusher ram drive emits a pulse for every preselected incremental distance traveled by the ram from the face of the oven at the start of the push to the completion of the push. The pulses are received in the quench car locomotive and are converted to signals that show the position of the ram during its travel. The quench car has a similar pulsing unit, and pulses from this unit are converted to signals that show the position of the quench car. The quench car locomotive operator can then coordinate the signals to achieve proper coke distribution in the quenching car.