Abstract: Distilling equipment comprising evaporation apparatus (2) including a boiling chamber (6) and equipment and conduits (46-59, 62, 63, 65-71) for supplying raw liquid to the boiling chamber at a predetermined level (43), a plurality of serial condensation stages (10, 20, 30), the first stage (10) connected to the top (7) of the boiling chamber (6) to receive gas therefrom and condense the gas by contact with cold recycled distillate from the final condensation stage (30), each stage having vertical vacuum producing bubble tubes (15, 25, 35) through which distillate and gas bubble (17) pass downward to a collection vessel (16, 26), gas carrier tubes (19, 29) which carry gas from each collection vessel (16, 26) to the condensation chamber (21, 31) of the following stage, and pump (41, 42) in cooperating conduits (18, 22, 28, 32) for pumping distillate free of gas from each collection chamber (16, 26) to the condensation chamber (21, 31) of the following stage.

Abstract: 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.

Abstract: Charging gases from each coking chamber in a battery of coke ovens are withdrawn through a closable ascension pipe into only a first gas main. The gases liberated during carbonization of the coal charge in each oven chamber are withdrawn through a closable ascension pipe into only a second gas main throughout the remainder of the carbonization process. The gases in each gas main are sprayed with flushing liquor. Gases are continuously transferred from the second gas main through pipes into the first gas main to equalize the gas pressure within the gas mains. Flushing liquor removed from the first gas main is processed to remove the tar content therefrom and to provide a clear flushing liquor which is used to spray charging gases within the first gas main.

Abstract: An apparatus for withdrawing and cleaning emissions of a battery of coke ovens, which emissions occur during the filling, coking, especially within the region of the doors, and during the pushing. The battery of coke ovens includes a charging larry with a withdrawal device for the filling gases. This battery is provided with suction conduits located on both sides of the battery and above the doors, while extending in the longitudinal direction of the battery. Connected to the suction conduits are collecting chambers for dust laden gases which rise within the region of the doors. A coke quenching car is displaceable substantially parallel to the battery. The coke quenching car has associated therewith a collecting hood which extends over the coke quenching car and which is provided with a withdrawing device for dust laden gases and vapors.

Abstract: A battery of horizontal coke ovens which are connected to two gas-collecting mains extending alongside the battery, one of said mains having means for cleaning dust-laden gases emitted from the coke ovens during charging with coal without the use of a flushing liquor and incorporating means for inhibiting the condensation of tar-based matter in the gas. The invention also relates to a method for operating such a battery of horizontal coke ovens.

Abstract: Control of emission from coke ovens during charging. A bank of coke ovens is provided with two gas mains. The first of the gas mains is connected to each of the individual ovens in turn during charging. The second of the gas mains is connected to the bank of ovens during coking. A fluid energized venturi ejector maintains a predetermined level of vacuum at the head of each individual coke oven during charging. Means are provided to automatically reduce the suction provided by the ejector if the level of vacuum exceeds said limit. This means consists of a valve operated by changes in the level of vacuum at the head of the individual oven during charging. The valve connects the second main to the first, thus increasing the gas pressure applied at the throat of the venturi ejector in turn decreasing the degree of vacuum provided by the venturi ejector. The energy for the ejector may be provided by flushing liquor or by a compressible fluid such as steam, air or an inert gas.

Abstract: An in situ oil shale retort in which a cavity filled with broken particles of oil shale is formed within the subsurface oil shale formation and air is forced down through the cavity to sustain combustion of the top layer of oil shale particles. The products of combustion are withdrawn through a plurality of transverse exhaust pipes at the bottom of the cavity, the exhaust pipes each being provided with a series of holes along the length of the pipes within the cavity, the holes being graded in size to compensate for the pressure drop along the length of the pipe so as to provide substantially equal volume of gas flow through each of the openings.