Abstract: In a gas treating device liquid is pressurized in a liquid chamber and is fed from this chamber into ejectors which open directly into venturi fittings which are surrounded by a gas chamber. Gas enters through an inlet into this gas chamber. A gas-liquid mixture enters from the venturi fittings into a tank, where the gas is separated from the liquid. Liquid from the tank is fed through a pump into the liquid chamber. Gas escapes from the tank into a discharge line comprising a de-mister.

Abstract: The emission of solid particles during the discharging of a horizontal coking oven or furnace is substantially reduced or eliminated. For this purpose the hot air and gas convection flow which carries the solid particles substantially vertically upwardly is exposed to a shower or spray of water drops which are directed substantially horizontally into the upward convection flow. The volume, surface tension, density and speed of the water drops are coordinated relative to one another so that the water drops are loaded by taking up the solid particles whereupon the loaded drops sink down in a countercurrent flow to the upward convection flow. The solid particles carrying the water drops are removed from the convection flow by a plurality of baffles arranged in a chimney or stack in a staggered relationship so that the upward convection flow can pass through between adjacent baffles which are inclined toward respective collecting channels.

Abstract: The present pressure rod for a coke discharge apparatus is constructed of hollow sectional components or tubular members interconnected with one another, whereby a lightweight structure is achieved. The hollow sectional components or tubular members are interconnected in such a manner that a coolant may flow through the structure of the pressure rod. Flexible coolant supply conduits for the inflow and outflow of coolant are connected to the hollow sectional components of the pressure rod.

Abstract: Fuel briquettes are produced by hot pressing a mixture of a fine grained coal softening at the pressing temperature and a coal component which hardly or not at all softens at the pressing temperature. The starting materials are converted into a granular structure material by the use of pure oxygen or an oxygen/nitrogen mixture having an oxygen content above 21% by volume so that the resulting granular material has a bulk weight of between 0.3 t/m.sup.3 to 0.7 t/m.sup.3.