Firma Carl Still

Firma Carl Still Gmbh & Co Kg

Firma Carl Still Recklinghausen

Janos Bocsanczy

Dieter Stalherm

Johannes Knappstein

Ludwig Offermann

Dieter Stahlherm

Hans Becker

Gerhard Rutkowski

A device for separating gases and solids, particularly coal dust, during the carbonization of coal, particularly predried and preheated fine coal in coke ovens arranged in a battery which includes a standpipe extending upwardly from the top of the battery having a bend extending from the top of the standpipe downwardly into a collecting main, comprises, a vertically extending standpipe which extends upwardly from the top of the battery and has a bend at the top thereof extending outwardly and downwardly from the top and which includes a longitudinally extending collecting main connected into the lower end of the bend with a solids discharge line overlying the bend and extending substantially parallel to the collecting main. The solids matter discharge line includes a connection extending downwardly into the bend. Means are provided for spraying a liquid into the bend over the collecting line and the solids matter discharge line includes a shutoff control in the connection to the bend. Exhauster means are connected to the solids matter discharge line for exhausting the gases enriched with the solids to a combustion furnace where they are burned. The combustion furnace may be one which heats water to form steam which is supplied back into the collecting line. Some of the solids which are removed are directed to a cyclone separator where coal dust is separated therefrom and the gas is returned to the collecting line. With the method of the invention, the bend is selectively connected to the solids matter discharge line so that gases containing solids are withdrawn therefrom and part of them are directed to a separator to remove the coal dust solids and to return the gases to the collecting main and other parts are directed to the furnace for burning therein.

Method and apparatus for separating gases and solids during the

A method reducing fine dust emission during the time that predried and preheated coal is charged into coke ovens comprises directing wet coal to be carbonized into direct contact with a hot process gas so that the coal is transported dry and heated, directing the hot process gas with the heated coal to a plurality of different separators in succession with the first separator being set to separate only around from 80 to 90% of the total amount of the coal and without separating the fine dust, and a subsequent separator separate the remaining amount of the solid matter including the fine dust, compacting the dust removed from all of the separators and mixing them together, and charging the compacted mixed dust into the coke oven. The apparatus for effecting the invention includes a material separator which is designed as a gravity separator or gravity sifter which is arranged to discharge into a connection between the mixed and compacted dust separator in separate additional separators.

Method and apparatus for reducing fine dust emission while charging

A method of preparing and delivering coal to a coking plant, comprises, conveying the coal to the plant on a moving conveyor while an inert combustion gas is directed over the coal being conveyed. The combustion gas is generated by burning a fuel with air to produce a substantially inert combustion gas which is passed over the coal during its conveying and, thereafter, passed through a cooler for removing the moisture which has been picked up from the coal by the gas. The heating and predrying inert gases are advantageously generated by the direct combustion of air and fuel which are passed through flash dryer tubes and one or more separate separator systems and then delivered into a conveyor pipeline through which the coal is conveyed. A portion of the gases which are generated are also directed with a return gas to a filter for removal of any coal therefrom and to a cooler for removing the moisture picked up from the coal and then back into the stream for delivery to the conveyor for the coal. The inert gas may also be a gas which is circulated in heat exchange relationship with combustion gases which are generated by a combustion of the coal itself. In such a system, a portion of the combustion gases generated are also passed through a condenser or cooler and the cooled and dried waste gases are circulated over the coal being conveyed to the coking oven or its bunkers.

Method of operating a coal predrying and heating plant in connection

A method of preheating coal for coking comprises bringing a hot operating gas into direct contact with the coal to preheat the coal. Both the coal and the operating gas are passed into a separator and the separator is operated so as to effect the separation of the coarse preheated coal for delivery to the coke oven from the operating gases and coal dust. The operating gases and coal dust are then passed into a deduster to remove the coal dust from the operating gases. A portion of the removed dust is continuously directed into an accumulator. The dust is either supplied from the deduster or the accumulator to a combustion furnace where it is burned to generate at least a portion of the operating gas. The amount of coal dust which is accumulated in the accumulator is checked regularly and the separator is operated so as to produce sufficient dust to maintain a desired operating level in the accumulator so that dust will always be available in a sufficient quantity to operate the combustion chamber for supplying the operating gases.

Method for preheating coal for coking

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. For this purpose the transfer conveyor housing is pivotally mounted for pivotal movement about a horizontal axis, and it is pivoted so as to bring the connection to the coal transferring opening of the conveyor into alignment below the coal transferring opening and engage with an extension of the chute defining the opening. In addition at the same time, the opposite end is aligned over the coal receiving chute of the oven and it is directed downwardly into engagement therewith so as to define a fuel path between the conveyor through the charging chute.

Coke oven coal charging device

Bunker for supplying alternatively either hot, dry coal or cold, wet coal to a charging hopper or test bunkers of a plurality of coke ovens in a coke oven battery, comprises, a bunker housing having an inlet adjacent its top for charging coal and a lower portion with a plurality of downwardly opening coke oven discharge spouts corresponding to the number of charging hoppers and test bunkers. An inert gas feed line includes a portion branching off to the vicinity of each spout and provided with a plurality of feeder lines at the lower end of the spout and which also includes a plurality of spray nozzles in the line for directing a water spray in the direction of the inert gas flow.

Growing community of inventors

Recklinghausen, Germany

Janos Bocsanczy