Abstract: An apparatus for compacting, degassing and carbonizing carbonaceous agglomerates, the apparatus comprising a rotary kiln having an agglomerate inlet means for introducing green agglomerates into the kiln near the inlet of the kiln and a heating medium inlet for introducing a heating medium comprising a finely divided solid into the kiln at a preselected location intermediate the inlet end of the kiln and the outlet end of the kiln to produce a mixture at a temperature above the carbonizing temperature of the agglomerates and a sieve positioned to receive the products from the rotary kiln and separate the heating medium and the compacted, degassed, carbonized agglomerate product. A method for producing compacted, degassed, carbonized carbonaceous agglomerates by the use of the apparatus is also disclosed.

Abstract: In a horizontal type coke oven, high temperature waste gas generated in a heating flue chamber and containing nitrogen oxides is discharged into a regenerator. There are provided nozzle openings for injecting ammonia or ammonia precursor to the high temperature waste gas at a position where the temperature of the waste gas is about 750.degree.-1000.degree. C. so as to reduce the nitrogen oxides in the waste gas with the ammonia or ammonia precursor.

Abstract: A sealing means for a coke oven chuck door. The sealing means includes a metal sealing member which has springiness and flexibility and is supported cantilever fashion on the inside of the door frame. An insulation block is interposed between the sealing member and door frame. The sealing member has a knife edge flange which extends around its perimeter and is automatically aligned with a sealing surface on the main door on which the chuck door is mounted.

Abstract: Sugar is crystallized from aqueous solutions thereof by spraying a supersaturated sugar solution or syrup at elevated temperature into a high velocity air stream, at ambient temperature, whereby crystallization and drying occur rapidly and the sugar crystals are entrained in the air stream and carried away from the spray zone in pneumatic transport.

Abstract: In the multi-stage fluidized carbonization of coal to produce, oil, gas and char, oil containing vapors from the first stage are used as the fluidizing gas to dry the incoming coal feed. The oil vapor pressure of the fluidizing gas is maintained at a value under 10 mm. to prevent oil condensation in the fluidized drying vessel. The technique makes possible the recovery of sensible heat from the first stage overheads.

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: An apparatus for carrying out polymerizations from the gas phase comprising a sealable reactor with a spiral stirrer which is rotatable in the reactor about a vertical axis to generate circulatory streams of the materials employed, in which the stirrer rotating within the reactor is surmounted by a stirrer rod, which extends upward beyond the uppermost flight circle of the stirrer and is attached to the stirrer at a certain distance from the axis of the stirrer, the distance of the side face of the stirrer rod from the reactor wall is at least 10 mm, and the surface of revolution of the moving rod matches the contour of the reactor in this zone.

Abstract: A device for charging coke ovens of a horizontally disposed coke oven battery through charging chute in the roof of each coke oven which is openable at its top and from a coal supply which includes a circulating conveyor for circulating the coal in a path over the roof comprises a transfer conveyor housing having a conveyor operable therein. The transfer conveyor housing is pivotally mounted, and it includes one end with a coal receiving connection which is alignable with a connectable coal transferring opening of the conveyor so as to receive coal therefrom. The other end of the transfer conveyor housing is provided with a connection with may be aligned over an opening of the coke oven for supplying coal into the receiving chute thereof.

Abstract: A toilet brush and deodorant holder has a base and a child-proof, removable, elongated, upright cylindrical column supported thereon. The column comprises inner and outer concentric walls radially spaced from one another to define an elongated, annular, compartmented passage therebetween. The base contains a vented cavity for holding a deodorant cake. Vapors from the cake flow upwardly through the annular passage to the upper ends of the concentric walls. A cap is removably supported at the upper ends of the walls and has vents in registration with the annular passage. The cap has a central opening for supporting the handle of a toilet brush which is insertable for storage in the cylindrical chamber defined by the inner wall. The brush is supported in spaced relation from the cake by the lower portion of the inner wall which has an aperture to permit drainage of moisture from the brush onto the cake.

Abstract: A process comprising heating coal in a substantially air-free environment to liberate volatile materials and produce coke, condensing at least some of the volatile materials so liberated to liquefied products and dispersing the coke therein to form a coke slurry, feeding the coke slurry to a slurry pipeline, and pumping the coke slurry through the pipeline to a destination.Apparatus comprising a tube furnace having an external heating means for indirectly heating powdered coal therein in a substantially air-free environment to a temperature adequate to liberate volatile materials and produce coke, means to feed powdered coal to the furnace under pressure and force the volatile materials and coke produced in the furnace through the furnace to a condensing means in which at least some of the volatile materials are condensed with the coke dispersed therein to form a coke slurry, and means to convey the coke slurry from the condensing means to a pipeline for transport to a destination.

Abstract: A jumper pipe forms a passageway between the free spaces above coal charges in adjacent coking chambers for the natural flow of relatively cooler coke oven gas from the free space above the coal charge in the most recently charged one of the coking chambers into the free space above the coal charge in the other of the coking chambers to reduce the relatively higher temperature therein. An inert atmosphere is maintained along at least part of the passageway to prevent the flow of coke oven gas essentially during decarburization and the pushing of coke from either of the two adjacent coking chambers. Valve members at opposite end portions of the jumper pipe are moved to at least partially-closed positions to facilitate the maintenance of an inert atmosphere therein. A supply or steam or gaseous nitrogen is used to maintain the inert atmosphere in the jumper pipe. The inert gas prevents the entrance of coke oven gas into a coking chamber while undergoing decarburization.

Abstract: In an aspiration chamber of a carbon black reactor, the discharge end of a hydrocarbon inlet and the aspiration inlet of a hydrocarbon reaction section are arranged in such a proximate relationship that the hydrocarbon feed entering from said inlet into said reaction section aspirates surrounding hot combustion gases. The aspiration chamber has a wall converging from the end to which the reaction section is attached towards the end to which the hydrocarbon inlet is attached. Inlets for the combustion gases comprising coal are provided for the tangential feed of the combustion gases into the annulus formed between the reaction section and the converging wall of the aspiration chamber. At least one ash outlet for discharging the ash from the chamber is arranged upstream of the discharge end of the hydrocarbon feed means.

Abstract: A fluidized bed reactor for the pyrolysis of pieces of rubber or the like, especially old tires the reactor comprising a container at the lower part of which there is discharge device for non-volatile pyrolysis products; gas blowing nozzles arranged in a zone above the discharge device for supplying a fluidizing gas and for producing a fluidized bed from material such as sand or alumina added to the reactor; preferably a heating device, especially one comprising heating tubes extending across the container; a gas outlet disposed in the zone above the fluidized bed; and supply means for conveying pieces of material to be pyrolized to the container; this apparatus is characterized by the fact that the gas blowing nozzles are arranged to direct the gas downwardly, that at least one group of nozzles are arranged in a common horizontal plane, and that the material supply device is such that its dimensions are comparable with the cross-sectional surface of the fluidized bed.

Abstract: A self-adjusting powder distributor--which is particularly intended for use with alumina calcination apparatus--comprises a casing with a permeable partition, a plurality of outlets, and means for introducing preheated hydrate above the partition and fluidizing air therebelow. The fluidized hydrate withdraws through outlets of the casing for further treatment or partly as final product. The casing is provided with means by which the amounts and mutual ratios of the withdrawing material can be adjusted according to preselected values by altering the cross-sectional flow area or the level of the outlets.

Abstract: An improved method for producing calcined coke agglomerates having good stability including adjusting the fluidity of coals or blends of coals to within a range of 1300 DDPM and 3000 DDPM, mixing the coals or blends of coals with char and optionally topped tar in a rotating agglomerating drum and agglomerating the mixture at a temperature between 750.degree. F. and 875.degree. F. (399.degree. C.and 468.degree. C.) for a time to form partially coked green coal agglomerates generally spherical in shape and calcining the partially coked green coal agglomerates at a temperature between 1500.degree. F. and 2000.degree. F. (815.degree. C. and 1093.degree. C). The calcined coke agglomerates are characterized by having a stability of not less than 60%.

Abstract: Access to a space is impeded by the generation of a sticky foam from a tacky polymeric resin and a low boiling solvent.

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 warp-resistant doorjamb is mounted next to the refractory at the outer end of a coke oven chamber. The doorjamb includes a rectangularly-shaped frame with end segments joining together two side segments each having a length substantially corresponding to the height of the coke oven chamber. Both side segments have an outwardly-extending rigid beam section with openings to releasably engage with hanger bars on a coke oven door. A plurality of web sections extends at spaced-apart intervals from each rigid beam section to define window openings between the web sections to minimize the conductive transfer of heat to the rigid beam section and dissipate heat to the atmosphere. A base plate section extends along the end and side segments and forms a face surface for mounting next to the refractory of a coke oven chamber. The base plate section is divided by transverse slots into individual base segments each joined with at least one of the web sections for the support thereby.

Abstract: An ammonium nitrate particle removal apparatus is joined with an exhaust gas flow of a nitrogen oxides abatement system as utilized in a nitric acid producing plant for removing ammonium nitrate particles carried in the gas flow. The apparatus includes a filter element for receiving the gas flow and substantially trapping the ammonium nitrate particles. Injection nozzles inhabit a conduit which delivers the exhaust gas flow to an inlet of the filter and inject a water mist into the gas flow which mist acts to irrigate the filter. As a result of this irrigation, the trapped ammonium nitrate particles go into solution and drop by the action of gravity to a tank or reservoir below the filter element, where the solution may be recovered for other uses as desired.

Abstract: Method and apparatus for continuous preparation of an acrylonitrilebutadienestyrene copolymer comprises on-stream mounted: a prepolymerization reactor, a polymerization reactor, a reactor for the final polymerization and an apparatus for the removal of the non-polymerized monomers from the reaction mass. The polymerization reactor contains a stirring means which has a tube fixedly mounted coaxially with a shell and a mixing member disposed inside the tube. The stirring member is embodied in the form of a closed cylinder. At least one slot is provided in the tube wall. This slot is extending over the entire length of the tube. In the reactor there is also a partition positioned between the reactor shell wall and the stirring member. The partition is passing through the middle of the slot and intended for division of the reactor shell cavity into a suction zone and a pumping zone.