Abstract: This invention relates to a combination comprising two vertical cylindrical shaped high temperature pressure vessels coaxially connected. The upper vessel is a refractory lined free-flow partial oxidation gas generator for the production of gaseous mixtures comprising H.sub.2 +CO from liquid hydrocarbonaceous and solid carbonaceous fuels. The lower vessel houses a radiation gas cooler for cooling the raw gas stream which is produced in the upper vessel and which passes down through a coaxial vertical cylindrical annular shaped refractory throat located between said upper and lower vessels. A vertical steel cylindrical gas barrier provided with a flanged bottom surrounds the refractory throat passage so that substantially no gas escapes into a stagnant annular zone outside of said gas barrier. Further the refractory throat is vertically supported by said flanged gas barrier.

Abstract: An apparatus for injecting quench gas (cooled syngas) through an injection ring located around the circumference of the gasifier exit duct and having ports in communication with the interior of said duct to achieve thorough mixing of the gasifier gas with the injected quench gas. Interchangeable rings having different configurations and dimensions of the ports may be used to accomodate various types of coal. The rings may be fabricated in sections for ease of maintenance and replacement.

Abstract: A process for monitoring the conditions in the reaction zone of a gasifier in a process for the gasification of coal to produce synthesis gas is disclosed, the process being characterized by continual or periodic calculation of the rate of steam production by the heat exchange system of the gasifier, and comparison of the calculated rate with a pre-selected value.

Abstract: In an electric energy generating plant including a coal gasification arrangement and a combined gas turbine and steam combine, hot raw gas generated in the gasification arrangement is fed via a heat-exchanging and dust separating unit into a desulfurization unit from which cool purified gas is discharged. The heat exchanging unit includes a tubular pressure resistant housing serving as a feeding passage for the hot raw gas and enclosing a coaxial arrangement of a tubular pipe-wall housing of a waste-heat recovery boiler, and pipe spirals of a raw gas/purified gas heat exchanger. The waste-heat recovery boiler delivers superheated steam to the steam turbine and the raw gas/purified gas heat exchanger delivers heated purified gas to the gas turbine.

Abstract: The gasification device includes a pipe wall structure assembled of a plurality of pipe circuits enclosing in a gas tight manner a reactor space. A pressure jacket surrounds at a distance the pipe wall structure and delimits therewith a water filled interspace. All inlet conduits for supplying cooling water to individual pipe circuits pass through the jacket whereas the outlets of the pipe circuits open into the interspace. A common discharge conduit for cooling water is provided in the pressure jacket and communicates with the interspace. The pressure jacket is assembled of two parts interconnected by a releasable flange connection. All inlet conduits and common outlet conduits are attached to the upper part so as to enable the lifting of the entire pipe wall structure upon the lower part together with the upper part.

Abstract: An arrangement for and a method of gasifying finely divided, particularly solid fuel under increased pressure with a multi-pipe wall having a plurality of pipes arranged to be supplied with a cooling medium, the multi-pipe wall limiting a gas-collecting chamber and also limiting a plurality of recesses which form combustion chambers, wherein each of the recesses having a plurality of parameters including a depth, a width and an angle of inclination of a peripheral wall and being such that at least one of the parameters is changeable

Abstract: A structural member to be subjected to a hot gas atmosphere produced through reaction between coal and a gasifier such as oxygen, air, steam or hydrogen, in a gasification furnace for example. The structural member is made of an anti-sulfur attack Cr-Ni-Al-Si alloy steel which has a composition essentially consisting of, by weight, 0.03 to 0.3% of C, 1 to 10% of Si, not greater than 2.0% of Mn, 8 to 14% of Ni, 16 to 20% of Cr, 0.5 to 10% of Al and the balance not less than 50% of Fe.

Abstract: The gas cooler has a pair of coaxial flues for the cooling of a synthesis gas wherein the flues are resiliently mounted independently of each other. The gas flow connection at the top of the pressure vessel is sized to permit the inner flue to be lifted out of the vessel for cleaning and repair purposes. In addition, the outer flue can be constructed of interconnected wall elements which may also be disconnected for discrete removal through the top of the vessel for cleaning and repair purposes.

Abstract: A device for cooling a stream of hot producer gas exiting from a gasification reactor operating at an increased pressure, includes a set of water spraying nozzles directed against the producer gas stream. Water feeding conduits connected to the nozzles pass through a sealing web provided between the pipe wall structure of the reactor and a separate pipe wall structure of a gas outlet connection piece provided above the discharge opening of the reactor. The geometric locations of respective nozzles are on a circle whose diameter is larger than that of the gas discharge opening and is smaller than the inner diameter of the pipe wall structure of the connection piece.

Abstract: An apparatus for gasifying coal dust has a housing provided with an output fitting for the removal of generator gas and an output fitting for the removal of granulated slag. An overflow maintains a body of liquid in the bottom of the housing and a coal-dust burner in the housing forms a downwardly moving coal-dust flame in an upper reaction zone of the housing. An annular tube wall in the housing upper and lower ends where its tubes are bent apart and form radially throughgoing upper and lower openings and at the burner and therebelow but above the generator-gas output fitting. This tube wall is radially gastight between its upper and lower openings and radially inwardly delimits an axially extending annular passage that is outwardly defined by the housing. Steam is fed to the upwardly directed lances in the passage to create in the housing a toroidal annular current of moving gas and steam rising in the passage and descending in the zones between the flame and the tube wall.

Abstract: An entrained flow coal gasifier having a combustor zone (16) and a reductor zone (18) separated by a centrally located baffle (14). The baffle (14) covers the projected plan area of a slag tap (44) whereby cool slag falling from the reductor (18) will be heated before flowing through the slag tap.

Abstract: A downflow, gravity type gasifier includes a vertically oriented chamber having a loading zone at the top, followed by a drying zone, followed by a pyrolytic zone for pyrolytic decomposition, followed by a cracking zone for cracking the tars, followed by a reduction zone and an oxidation zone wherein the gas is generated and the combustible material is burned. The cracking zone has a divider, e.g. a cruciform divider, in it, and each of the resulting sections of the cracking zone is individually supplied with air for more uniform distribution of air and more uniform cracking than heretofore available. In addition to the air supplied to the periphery at the cracking zone, air outlets are arranged in respective radial arrays of the outlets for more uniform distribution of air into the reduction and oxidation zone.

Abstract: A pressurized coal gasification system having double wall containment vessels (2,10) is disclosed. The gasification vessel (2) is provided with a gas tight water seal (36) for connecting the lower end of the inner water-cooled vessel (4) with the bottom supported slag tank (32). The seal (36) prevents gas leakage between the vessel interior and the pressurized annular volume (24) formed between the inner and outer gasification chambers (4,6). A flow of clean, particulate-free product gas (60) is routed into the contiguous annular volume (24,26,28) formed between the inner water-cooled gas directing members (4,20,12) and the outer, pressure containing members (6,22,16) to prevent either leakage of raw product gas into the annular volume or dilution of the product gas (46) by leakage of the sealing gas (60) into the hot product gas flowstream.

Abstract: An assembly for supplying gas-conveyed solid fuel to the interior of a double wall gasification vessel includes a conduit (4) for conducting the fuel-gas mixture across the annular region (16) formed between the inner (3) and outer (2) vessel walls. A flexible coupling (11) is provided at one end of the conduit proximate the penetration of the fuel-gas stream across the vessel pressure boundary. An expansion joint (14), disposed about the conduit (4) and sealed to the inner vessel wall (3) conducts secondary gas into the inner vessel across the annular region (16) and prevents leakage of corrosive gases from the inner vessel interior.

Abstract: A gasifier (10) having an associated boiler (26, 32, 42, 48), for converting coal to combustible gas, and also having a desulfurizer (20) downstream of the gasifier. In order to maintain the gas leaving the gasifier and flowing to the desulfurizer above a predetermined temperature, even when operating the unit at reduced loads, a temperature sensing device (56) continuously monitors the gas temperature upstream of the desulfurizer. If the temperature drops below a predetermined value, high temperature boiler water (62) is introduced to the economizer (26) rather than feed water (24), so that less heat is absorbed by the economizer from the gases under these conditions.

Abstract: A waterwall for a twin tower gasification system wherein the two towers are fluidically connected intermediate their ends. The waterwall comprises a plurality of tubes, a portion of which extend from the first tower to the second tower and define a cylinder. The portion of the tubes extending between the towers are twisted into a helix such that the portion of the tubes that define the lower portion of the cylinder at the first tower, define the upper portion of the cylinder at the second tower.

Abstract: An upright apparatus for cooling high pressure gases with a high dust component includes a radiation/convection cooler with longitudinally extending heat exchanger elements and a convection cooler follows the radiation/convection cooler on the gas side. As distinguished from known devices for the cooling of high pressure gases, the apparatus provides a largely uniform distribution of the gas at the cooling elements and hence a uniform thermal load of the individual elements in the radiation/convection cooler. A uniform cleaning of these cooling elements and easy removal of the dust from the cooling surfaces of these cooling elements is made possible, in order thereby to ensure a good heat transfer. The radiation/convection cooler heat exchanger elements are combined in finned tube walls forming lanes between them, which walls extend from one inner wall section to the opposite inner wall section.

Abstract: The gas cooler arrangement includes a first pressure vessel in which heat is yielded by radiation and a following convection gas cooler. The pressure vessel of the convection gas cooler includes a faller flue and at least one riser flue for cooling the gas. The flues comprise heat-removing tubes which are parts of a steam generator. The bottom of the pressure vessel contains an ash collection chamber which is connected to the ends of the flues and which can be emptied via a suitable closure element.

Abstract: The gas cooler has a downcomer bounded by radiant cooling walls and a waterbath at the end of the downcomer. The depth of the waterbath is several times its horizontal extent and the waterbath is flowed through downwardly by water. The bath is connected by way of a pump, heat exchanger and a feed line to a water circuit. Means are provided to control the water temperature at its entry into the waterbath so that the entry temperature is maintained at a value somewhere between the dew point of the synthesis gas and the evaporation point of water at the working pressure of the synthesis gas.The result is substantial obviation of evaporation of water from the waterbath and the associated heat losses.

Abstract: A combustible gas producer plant is described in which a finely divided inert particulate material fluidized bed is divided into a first, combustible-gas producing section and a second, heating section, to both of which sections fuel is fed. Heat transfer, by bed material migration, from the second to the first section sustains the reaction in the first section leading to the production of combustible gas. A diaphragm water wall divides and surrounds the volumes above bed sections and is part of a boiler generating steam used (optionally with added oxygen) to fluidize the first bed section. The steam is also used to fluidize the bed material at the boundary of the bed sections and prevent in-bed gas migration across that boundary. The second section of the bed is fluidized with air or an air/inert gas mixture. Fluidization is effected with sparge tubes and the plant may include evaporator, superheater and economizer sections for the boiler.

Abstract: An arrangement for producing gaseous products from solid and liquid, ash-containing fuels and mixtures thereof in an air stream in a reactor. The fuels are introduced into the reactor parallel to the axis thereof. The solid and liquid ash constituents are extensively separated from the gaseous products of the fuel in a slag bath before further cooling-off. The gaseous products are reversed by 180.degree. after leaving the reactor, and subsequently flow into one or more consecutively or parallel connected annular chambers, which are provided with heat exchanger heating surfaces and concentrically surround the reactor. The gaseous products are cooled in these annular chambers.

Abstract: A flue-stream reactor for gasifying fossil fuels which contain ballast. The reactor comprises two cylindrical, cooled, and insulated reaction chambers which are disposed one after the other in the axial direction. The first reaction chamber is provided with an axial inlet for accommodating a gasification burner. The second reaction chamber is provided with an opening for the addition of gasification material. A cooled, coaxial channel provides communication between the two reaction chambers. The reactor further includes a radial discharge and a device for removing liquid and solid ash and slag.

Abstract: A plant for the gasification of fossil fuels which includes a reactor container and a further plant component attachable to the reactor container. The reactor container has a discharge opening and includes a connection part extending outwardly from the discharge opening. A fireproof lining, which determines the inner cross-sectional area of the container, is provided within the container. An intermediate ring is interposed between the connecting part of the reactor container and the further plant component for attaching the connecting part to the further plant component. This intermediate ring is provided with a fireproof lining having an area of reduced inner cross-section which is less than the inner cross-sectional area of the fireproof lining of the reactor container, the area of reduced cross-section being the smallest cross-sectional area in the connection between the reactor container and the further plant component.

Abstract: The hot gas cooler comprises a vertical cylindrical pressure vessel and, disposed axially thereof, an insert which is closed over its periphery and embodied by sealingly welded-together tubes. The tubes are part of the heated pressure system of a vapor generator. The chamber bounded by the insert communicates at the top, by way of a gas supply passage extending through the pressure vessel with a reaction chamber and at the bottom, by way of a discharge passage, with a slag removal facility. Extending around the insert is a jacket embodied by sealingly welded-together tubes, so that an annular chamber closed off from the casing of the pressure vessel extends around the insert. The annular chamber communicates at the bottom with the insert chamber. Disposed in the top part of annular chamber is a coolable gas discharge passage which is connected to the jacket and extends through the pressure vessel.

Abstract: A synthesis gas cooler has concentric water walls to provide for heat transfer to a fluid in the water wall tubes. The inner water wall is concentric with the cooler shell and has a gas tight inlet connection for introducing hot synthesis gas. The inlet is located at the top of the shell. The bottom of the shell contains a body of water for quenching entrained solids which are carried with the synthesis gas, and there is a baffle to direct the flow of synthesis gas back up in the annulus between the two concentric water walls. The annulus has a closed upper end except for an outlet for the synthesis gas which is located near that end of the annulus. Also, there may be soot blowers along the length of the water walls to keep the heat transfer surfaces clean.

Abstract: Garbage to be converted is fed into the upper end of a vertical chamber. A gas collection chamber is provided around the upper end of the chamber and a blower is used for lowering the pressure in this gas collection chamber. The lower pressure causes a draw within a combustion zone defined at the lower end of the garbage chamber. The draw promotes combustion of garbage in the combustion zone much in the same manner that the draw by a pipe smoker will promote combustion within the bowl of his pipe. The gas collected in the gas chamber is delivered through a water filled cleaner or filter. The gas discharged from the upper end of the filter is ready for use in a power device or a furnace, or it may be collected and compressed or even liquified, into a storage container, for easy mobility and later use.

Abstract: A shaft furnace is provided for gasifying granular fuels in a fluidized bed. Such a furnace comprises a gasification zone containing the fluidized fuel bed and an overlying gas cooling zone having surfaces cooled by the tube surfaces of a radiation tube boiler. By providing such a gas cooling zone with a cross-sectional area substantially greater than that of the gasification zone, the gas effluent is cooled in such a manner that residues entrained in the effluent do not sinter onto the surfaces of the equipment in the subsequent path of the effluent.

Abstract: The reactor for the production of CO and H.sub.2 containing gases by means of a partial oxidation of powdery or liquid high ash fuels in a carburation fluid including free oxygen, at high temperatures and increased pressure, includes a pressure vessel enclosing a gas-tight housing whereby an interspace is formed between the inner wall of the vessel and the outer surface of the housing. Within the housing is arranged a cooling wall enclosing the reaction chamber proper. The cooling wall includes a coil of cooling pipes embedded in a mass of refractory material such as silicium carbide. The pipes are partially supported on web sections projecting from the inner surface of the housing into the refractory lining. The web sections prevent propagation of leaking hot gas from the reaction chamber along the inner surface of the housing.

Abstract: A water jacket for coal gasification in which the gas producer is provided with an inwardly directed collar spaced from the water jacket and a plurality of apertures through the collar formation such that the collar can assist in supporting the refractory material of the wall of the gas producer.

Abstract: A pressure container forms a shaft gasifier for receiving coarse coal in the form of a coal bed. A burner extends through the pressure container into a chamber therein and produces at least one primary gas jet directed against the coal bed, thereby gasifying the coal and generating a product gas and forming liquid slag. The liquid slag collects in a slag bath tank having an overflow weir over which the collected slag flows and falls freely toward a cooling water bath beneath the chamber. A water jet nozzle directs at least one water jet against the liquid slag as it falls freely between the weir and the cooling water bath. This atomizes the liquid slag, thereby cooling the slag and generating steam. At least a part of the steam is supplied as process steam to the coarse coal.

Abstract: In a device for the treatment of synthesis gas produced by coal gasification, a vertically extending shell is connected to a coal gasification reactor so that the interior of the shell is in direct communication with the interior of the reactor. The interior surface of the shell is lined with upwardly extending heat exchange tubes. Additional heat exchange tubes in combination with the tubes lining the shell form a plurality of upwardly extending chambers projecting radially inwardly from and spaced angularly apart about the tube lining. Tubes coextensive with the heat exchanger tubes forming the lining, are located within the chamber for conveying a cleaning fluid. The tubes are arranged to direct the cleaning fluid approximately tangentially of the heat exchanger tubes lining the shell for cleaning the exterior surfaces of such tubes.

Abstract: Apparatus for purification of synthesis gas produced by coal gasification is provided with a vertical gas distribution chamber which is internally pressurized and within which the synthesis gas leaving the reactor is cooled. The chamber is formed with a gas take-off line which opens into the gas distribution chamber and extends therefrom at an angle, the gas take-off line leading to a serially connected waste heat boiler. A coolant bath is contained in a lower portion of the gas distribution chamber and a heat exchanger is formed in this lower portion by tube coils which are arranged in the wall of the distribution chamber defining the lower portion.

Abstract: The reactor for producing gas from powdery fuels comprises an outer metal sheet jacket, an inner pressure resistant jacket defining with the outer jacekt a first interspace for a cooling liquid, reinforcing brick lining adjoining the inner wall of the inner jacket, a cooling shield enclosing a reaction chamber and defining with the brick lining a second interspace for an inert cooling fluid. The cooling shield has at its upper end a gap communicating with the second interspace and the lower end of the reactor is provided with a pressure releasing conduit communicating with the bottom of the second interspace so that when the gas generating process is interrupted and the conduit is opened the pressurized gas escapes from the reactor chamber through the upper gap and flows through the major part of the second interspace to be cooled down before the discharge from the connecting conduit.

Abstract: Product gas resulting from the partial oxidation of finely divided fuel in a reactor is discharged as a stream into a tube leading downwardly into a vessel containing a water bath in which the lower end of the tube is immersed. Liquid slag produced during the partial oxidation is also discharged as a solid stream within and surrounded by the stream of product gas. The tube is cooled by circulating cooling water upwardly through an annular clearance in the tube which is discharged from the annular clearance at the upper end of the tube for gravity descent as a liquid film along the inside of the tube. The slag becomes cooled and granulated on contact with the water bath and is discharged from the vessel in granulated condition. The gas escapes from the lower open tube end, travels upwardly through the water bath to become cooled thereby, and is then discharged from the vessel in cooled condition.

Abstract: The apparatus of U.S. Pat. No. 3,988,123 is improved by constructing the heat recovery stage as a relatively elongated water-wall type of heat exchanger within a pressure shell, rather than of shell and tube type. The heat exchanger is advantageously formed from contiguous, externally finned, vertical tubes that are rigidly joined together to form a laterally closed, heat recovery chamber, the fin portion of one being welded along its tip to the tube portion of another adjoining such fin portion. The heat exchanger tubes preferably continue vertically throughout substantially the entire height of the gasification reaction i.e. combustion chamber of the first stage of the apparatus, completely eliminating the intermediate quench stage of the patented apparatus and serving to recover heat from the combustion stage as well as from the heat recovery stage by a heat exchange fluid, such as water, flowing through the tubes.

Abstract: A coal gasification reactor is disclosed which includes a gasification chamber surrounded by a pressure shell, a tubular quench section above the gasification chamber and a superposed waste heat boiler. Heat expansive members are provided in the form of bellow type expansion members between the waste heat boiler and the quench section as well as between the quench section and the gasification chamber to absorb or compensate for relative thermal expansion differences due to the temperature ranges involved in gasification.

Abstract: A system is provided for cooling high-temperature, high-pressure gasifiers having cooling tubes which extend vertically through the walls of the gasifier and are connected in a closed cooling water circulation system.In accordance with the invention, the cooling tubes are coated on the inside of the gasifier with a plasma or flame sprayed ceramic coating, preferably consisting of alumina, and are embedded in a ramming compound such as tamped clay.

Abstract: A system for cooling high-temperature gasifiers and method for its operation wherein cooling conduits extend vertically through the walls of the gasifier and are connected at their ends to a closed-water circulation system which incorporates heat exchangers for removing heat from the system. Boiling in the system is prevented, and good heat transfer characteristics are achieved, by maintaining a high pressure system, at least 40 bar, coupled with a flow velocity of between 5 and 7 meters per second at a maximum internal diameter of the cooling conduits of 51 millimeters. Means are provided for maintaining the temperature of the water exiting from the cooling conduits at least 10.degree. C below the boiling point at the pressure and flow rate of the system.

Abstract: A method and apparatus for gasifying fine-grained fuel, e.g., coal and a gasifying medium, e.g., oxygen in a slag bath generator. The fine-grained fuel and gasifying medium are injected at a downwardly-inclined angle to tangentially impinge with a turbulent rotary motion upon a slag bath in the lower end of a vertically-extending reactor shaft within a pressure vessel. A desired slag bath level is maintained in the bottom of the vessel by using an overflow to discharge slag from the bath through the bottom of the vessel. A first treatment zone for the high temperature gasification of the fuel is formed between the slag bath and a circular constriction to the reactor shaft. A second treatment zone for the final gasification of the fuel at a lower temperature as compared with the temperature in the first treatment zone extends above the circumferential constriction along the reactor shaft. Fuel and gases passing through the circumferential constriction are essentially free of a turbulent rotary motion.