Metallgesellschaft Aktiengesellschaft

Hans Kupfer

Paul Rudolph

Carl Hafke

Heinz Jockel

Gerhard Cornelius

Emil Supp

Friedemann Marschner

Herbert Bierbach

Rudolf Kohlen

Heinz Hiller

Heinz Wolf

Paul Lange

Helmut Vierrath

Lutz Weidemann

Werner Schmidt

Gert Schuster

The reactor for the gasification of the fuel in a fixed bed comprises a rotary distributor, which is disposed over the fixed bed and includes at least one outlet structure for the fuel. The outlet structure consists of a tube, which is formed at its lower end with two arcuate cutouts through which the fuel flows out approximately at right angles to the direction of movement of the tube. Each cutout lies in a plane which includes an angle of about 25.degree. to 50.degree. with the horizontal. The outlet end of the tube has preferably the same elevation on the leading and trailing sides of the tube.

Fuel distributor in a reactor for gasifying solid granular fuels

The fuel constitutes a fixed bed in the reactor, which is provided in its lower portion with a rotating grate, which is adapted to be speed-controlled. The gasifying agents consisting of oxygen, steam and/or carbon dioxide are introduced through the rotating grate into the fixed bed. Under the action of the rotating grate the incombustible mineral constituents are delivered as solid ash to a lock chamber container. The speed of the rotating grate is controlled in dependence on the temperature in the lock chamber container. The speed will be decreased when the temperature in the lock chamber container exceeds a desired value, and increased when the temperature is too low. The desired temperature in the lock chamber container is taken into account as a range, which varies with time. The speed can be controlled by hand or can be automatically controlled with the aid of a computer. The rate at which oxygen as a gasifying agent is supplied to the reactor is also taken into account in the speed control.

Method of operating a reactor for gasifying solid fuels

A reactor is provided for producing methanol by the reaction of synthesis gases containing carbon oxides and hydrogen in contact with a copper containing catalyst positioned in the reactor in catalyst tubes surrounded by boiling water under pressure. The catalyst tubes are made from a metallic material which is catalytically inactive with respect to the methanol synthesis gas and have approximately the same coefficient of thermal expansion as the shell of the reactor. The catalyst tubes are made of a steel composed of mixed austeniticferritic structure and containing 10-30% by weight chromium.

Reactor for producing methanol and process

Solid fuels are gasified in a fixed bed with gasifying agents passed through the fixed bed from below. The gasification residues are withdrawn as solid ash or as liquid slag under the fixed bed. The reactor is charged with solid fuels through a lock chamber and with tar through a supply conduit. The tar is delivered to the fuel in numerous individual streams, which are distributed over the cross-section of the fixed bed. In the gasifying reactor, an inclined distributor surface is disposed over the fixed bed and has numerous passage openings for the tar and the solid fuels. The outlet end of the tar supply conduit is directed to the upper portion of the distributor surface. A tar tub having outlet openings is associated with the distributor surface and serves to receive the tar. The distributor surface is rotatable on a vertical axis.

Reactor for gasifying solid fuels

The apparatus serves to continuously charge coarse-grained and fine-grained solid fuels by means of a rotary distributor onto a fixed bed of fuel. The fixed bed is disposed within a reactor for gasifying the fuels. Gasifying agents comprising oxygen, steam and/or carbon dioxide are passed through the fixed bed from below. Residual matter left after the gasification is withdrawn under the fixed bed as solid ash or liquid slag. Fine-grained fuel having a mean particle size up to 5 mm are placed onto the fixed bed as helical layers separately form more coarsely grained fuel having a mean particle size above 5 mm. The more coarsely grained fuel is deposited directly on fine-grained fuel which has just been deposited. The gasifier comprises a rotary distributor that includes at least one passage for the fine-grained fuel and at least one passage for the more coarsely grained fuel. The inlet of the passage for fine-grained fuel is disposed near the center of the rotary distributor. The inlet of the passage for the more coarsely grained fuel is disposed near the periphery of the rotary distributor.

Process and apparatus for charging solid fuels into a fixed-bed gasifier

A reactor for reacting hydrocarbons with steam to produce carbon monoxide and hydrogen containing gases in the presence of a catalyst contained in a reaction tube and indirectly heated by heating fluid which is a gas that has been used to cool a nuclear reactor. The reaction tubes are surrounded by the heating fluid over a portion of their length in a heating zone and the other portion thereof is positioned outside of the heating zone. The reaction tubes are provided with one or more conduits for feeding of reactants and one or more conduits for discharging product gas.

Tubular heater for cracking hydrocarbons

An apparatus for gasifying solid fuels such as coal, in a packed bed by a treatment with a gasifying agent such as free oxygen-containing gas and water vapor under pressure, comprising a water-cooled reactor housing provided in its lower portion with gasifying agent inlet openings, a fuel distributor mounted on a vertical axis, a stirrer on a shaft disposed in the fuel bed in the upper portion of the reactor, and independent first and second drive means for independently rotating the fuel distributor and stirrer. Advantageously the distributor includes a hollow bearing shaft coaxial with the shaft of the stirrer and the stirrer shaft also has a bearing, a common bearing support cooperating with both of the bearings.

Reactor for gasifying solid fuels, particularly coal, under

A reactor for the pressure gasification of coal by treatment with oxygen and steam and, if desired, additional gasifying agents, at elevated temperatures and pressures, includes a water-cooled jacket and a rotary grate for moving the material to be gasified and for distributing the gasifying agents introduced into the reactor. The rotary grate is made of at least two concentric parts each of which rotates independly of the other part.

Reactor for the pressure gasification of coal

A reactor for reacting gaseous or vaporized hydrocarbons with water vapor to produce carbon monoxide and hydrogen containing gases in the presence of a catalyst. The catalyst is contained in indirectly heated tubes in a heating zone which contains the gaseous heating fluid. The catalyst tubes extend through the reactor housing and at least partly into a heating zone defined by the reactor housing. The portion of the tubes extending into the reactor housing are surrounded by an inner shielding wall which is permeable to an outer shielding wall disposed within the reactor housing and defining a flow passage therewith.

Reactor for cracking hydrocarbons

Coal is gasified under elevated pressures and temperatures in a reactor having a rotatably mounted grate and supply conduits for oxygen-containing and oxygen-free gasifying agents. The rotary grate contains an internal chamber adjacent to the bearing for the grate and one of the supply conduits is adapted to feed an oxygen-free fluid to this internal chamber. The uppermost portion of the rotary grate contains a substantially closed internal chamber which has a supply conduit for feeding an oxygen-free fluid thereto. A mixing chamber is positioned between the uppermost chamber and the chamber adjacent the bearing for the grate and is provided with passages which lead to the charge to be gasified. The mixing chamber communicates with the uppermost chamber as well as the chamber adjacent the bearing and also has a supply conduit for feeding gasifying agents containing free oxygen thereto. The process disclosed involves maintaining those portions of the rotary grate having the least resistance to free oxygen in a steam atmosphere.

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Frankfurt am Main, Germany

Hans Kupfer