Abstract: A retort heating apparatus for processing a feed material includes a heating chamber bounded at least in part by a side wall. A plurality of baffles are at least partially disposed within the heating chamber. Each baffle includes an elongated body having a top surface, at least a portion of the top surface being arched. The plurality of baffles are vertically and horizontally spaced apart so that substantially all of the feed material that vertically passes through the heating chamber is horizontally displaced as the feed material passes by the baffles. Systems are also provided for heating the feed material within the heating chamber.

Abstract: The invention provides a method and apparatus for decreasing gas flow rates in a sole flue gas system for a coke oven during at least an initial coking operation after charging a coking oven with coal. The method includes providing a duct system between a first coke oven having a first coking chamber and a second coke oven having a second coking chamber to direct at least a portion of gas from a gas space in first coking chamber to the second coke oven thereby reducing a gas flow rate in the first sole flue gas system of the first coke oven. Reduction in sole flue gas flow rates has a beneficial effect on product throughput, the life of the coke oven and environmental control of volatile emissions from coke ovens.

Abstract: An improved delayed coking unit with at least one coke drum wherein said coke drum comprises a substantially closed interior, a top portion having an aperture, an overhead vapor outlet nozzle removably connected to the aperture, and a deflector for deflecting solids and heavy hydrocarbon liquids from exiting said interior of said coke drum through said aperture.

Abstract: A coke oven wall (4) comprising a plurality of bricks (38, 42, 46, 120) laid so as to define first and second wall faces (40, 44), and plurality of flue cavities (14) extending therein characterized in that at least part of the wall is made first, second and third bricks (38, 42, 120) which are laid together and define in part the first and second faces and the flue cavities wherein the first brick comprises a first body portion (48) and an inwardly projecting first leg (50), the second brick comprises a second body portion (64) and an inwardly projecting second leg (66) the third brick comprises a flue wall brick (46, 120) which is located between and aligned with the first and second legs.

Abstract: Gaseous, liguid and solid fuels are recovered from carbonaceous organic waste material by treating charges of waste material in several successive stages including preheating, drying and conversion into solid and gaseous phases, all as a result of heating in a common vessel or in two or three successive vessels. The solid phases are thereupon cooled prior to admission into a bin, either in a separate vessel or in the vessel for conversion into solid and gaseous phases. The gaseous phases are treated to separate oil from reaction water, combustible gases and inert gases. The charges are heated from without and are sealed from the atmosphere during all four stages of treatment. Each charge is mixed during heating and the intensity of mixing action, the heating action and/or the pressure in the vessel can be varied during one or more stages.

Abstract: Pyrolytic apparatus for the rapid and efficient thermal dissociation of matter is disclosed. The apparatus includes a concentric tubular arrangement of high thermal conductivity in a heat sink configuration; inlet members for heat and feedstock; outlet members for solids, gases and heat exhaust; and a plurality of annular passages through which heat is brought into heat transfer relationship with an interior pyrolytic retort section for the dissociation of matter conveyed therein into solid, liquid and gaseous by-products. Provisions are made for the separate liberation of steam produced by the simultaneous interfacing of superheated steam and product gas during pyrolytic decomposition of high moisture content feedstocks. Additional hydrocarbons from the product gas evoluted in the pyrolytic retort section are provided by diversion of the gas to an annulus flanked on either side by adjacent annuli conveying the heat source supply to exit.

Abstract: A heating wall on a horizontal coke oven battery. The liner wall section which separates the flues from the oven chambers is characterized by two or more laterally extending rows of vertical ridges. The ridges in adjacent rows are misaligned so as to establish surface turbulence in rising flue gases. As a result of this turbulence and the increased surface area afforded by this configuration, the rate of heat flow through the liner walls is increased so as to increase the rate of carbonization in the oven chambers.

Abstract: An inclined chamber has vertical heating flues on each side thereof. The floors of the heating flues are vertically staggered in an inclined manner. Pairs of heating flues are joined at the tops thereof by guide openings which are vertically staggered in an inclined manner. Central and upper air inlet openings extend into the heating flues and are vertically staggered in an inclined manner.

Abstract: A coke oven and method of heating a coke oven are provided in which the coke oven has coking chambers with a low burner heating wall on one side of the coking chamber and a high burner heating wall on the other side of the coking chamber. Heating takes place by only low burners in one heating wall and only high burners in the other heating wall.