• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Solid fuel is acted on by a gasifying medium in a fluidized bed W. The resulting gas enters a cyclone 20 having an outlet for solid particles connected to a gasification chamber 30 in which the particles are gasified by a separate stream of gasifying medium supplied by an injector 25.
    公开号:SU959633A3
    申请号:SU782661701
    申请日:1978-09-14
    公开日:1982-09-15
    发明作者:Кайманн Валтер；Брахтхойзер Карл-Хайнц
    申请人:Проектирунг Хемише Ферфаренстехник Гмбх (Фирма)；
    IPC主号:
    专利说明:

    (5t) METHOD FOR OBTAINING GAS FROM SOLID FUEL AND GAS GENERATOR The invention relates to the chemical industry, namely to production methods — gas from solid fuel through its gasification and gas generator: to implement the methods. A known method for producing a pelvis from solid fuel includes gasification in a fluidized bed, separation of solid particles from gas under the action of centrifugal forces and cyclone til. A gas generator is known for producing gas from a solid fuel D of a fluidized bed, comprising a vertical housing with means for loading fuel and a pipeline for supplying a gasification agent and a cyclone connected to the gas generator 1. The disadvantages of the known method and gas generator are their complexity due to the fact that placing the cyclone outside the gas generator requires the installation of an additional device for burning solid particles, separated from the gas, which leads to an increase in energy consumption and an incomplete the use of combustion heat. The closest to the proposed technical solution is a method for producing gas from solid fuel, including gasification in a fluidized bed, separation of solid particles from gas under the action of centrifugal forces in a cyclone placed in the reaction space above the fluid bed 2. Also known is a gas generator for producing gas from solid fuels in boiling c / ioe, including a vertical case with means for loading fuel and a pipeline for supplying a gasification agent and a cyclone located in the upper part of the case and having connections for outputting gas and solid gases. particles 2. During solidification of solid fuels from the developed fluidized bed, small solid particles are carried along with the gas stream. In view of the fact that these
    parts 11s are partially or completely non-gasified, have non-healing carbon losses of fuel. . ,
    When the cyclone is placed in the reaction space, the solid particles returned to the bottom layer (are again undersized and insufficiently, again entering the cyclone from the fluidized bed, thereby increasing its load, as a result of which the performance of the gasification process does not improve. whole
    The purpose of the invention is to intensify the process.
    The goal is achieved by the fact that according to the method of producing gas from solid fuel, including its gasification in a fluidized bed, the separation of solid particles from gas by centrifugal forces in a cyclone, placed in the reaction space above the fluid bed, is separated by solid particles leaving the cyclone is subjected to gasification with a superfluous boiling layer in an additional stream of gasifying agent and the gasification products are fed into the fluidized bed.
    The goal is achieved by the fact that in a gas generator for ® obtaining gas from solid fuel in a fluidized bed, comprising a vertical case with means for loading fuel and a pipeline for supplying a gasification agent and a cyclone located in the upper part of the case and having connections for gas and solid particles, the cyclone is equipped with a gasification chamber connected to the nozzle for the removal of solid particles and having an injector for introducing a gasification agent.
    In addition, the injector is located between the nozzle for removing solid particles from the cyclone and the gasification chamber, guide vanes are installed in the upper part of the cyclone, the nozzle for evacuating the gas from the cyclone is located along its vertical axis, the gasification chamber is provided with pipelines for cooling agent supply, . gasification agent in the injector is located inside the pipelines for the supply of the cooling agent.
    According to the proposed method, the separated solid particles exiting the cyclone are gasified over the fluidized bed in an additional stream of gasifying agent and the gasification products are fed to the fluidized bed.
    As the gasification agent, predominantly water vapor and oxygen are used. Particles trapped from the general gas stream can be entrained directly by the gasifying agent stream. Thus, in the gasification process, all carbon contained in the solid particles may be involved. The result is better utilization.
    5 fuel than when gasification according to the known scheme. In addition, the undesirable load of the entire process is removed, especially the particulate trap assembly, associated with
    Q the need to re-process the particles of fuel captured from the resulting gas stream.
    Gasification of fuel is carried out mainly at temperatures above the Melting Zone temperature. As a result, the solid ash particles do not appear in the process, but liquid slag falls out, which enters the fluidized bed, cools and hardens and then drops down from its relatively high specific gravity, from where it is removed by any known method. Thus, in the gas stream rising from the fluidized bed, there are no small solid particles that would need to be reintroduced into the fluidized bed.
    In addition, with separate gasification of the captured particles, it is removed completely to use the heat of the new stream. Hot gases give up their heat to the fluidized bed, where this energy contributes to the flow of e (prethermal reactions.
    Compared with the usual method of gasification in installations with a fluidized bed, in the proposed method, the resulting gas leaves the reaction zone relatively cold.
    权利要求:
    Claims (2)
    [1]
    The advantage of the proposed method also lies in the separate gasification of particles captured after the process in the fluidized bed and in the fixed bed. This is confirmed by the quality of the final product, as well as by satisfactory indicators of the individual stages of the process s up to the discharge of ash from the apparatus with the help of a drum screen. The gasification process is expediently carried out under pressure, however, it is allowed to work without pressure. It is advisable to connect the gasification chambers to the output end of the cyclone. Particles caught in this case, the gasification agent stream leaving the injector can immediately be picked up. The injector may be located directly between the cyclone and the gasification chamber in the transition zone or be installed at the outlet of the cyclone-. In different forms of execution, the injector itself or its output nozzle can be positioned either obliquely with respect to the J axis of the gasification chamber axis, or off center. Thus, it is possible to influence the movement of particles in the process of gasification, in particular, it is possible to impart to the particles of a spiral or spiral-like motion in the flow of a gasification agent, which is characteristic of their length in a cyclone. . . . Cyclone mainly places with. at the top of the head of the case. Its technical characteristics must satisfy the technical requirements with regard to the velocities and sizes of particles in the gas stream passing through the cyclone. Cyclones are made of a heat-resistant material, and also ceramic materials can be used as a steel edge. Since the cyclone is located inside the generator casing, its design does not impose any pressure requirements, even if the gasification process itself is carried out under pressure. , I Gas can be introduced into the cyclone through special devices. Such a device has, for example, gas passage openings evenly spaced around the circumference, or made with guide plates,. set on the ring. For removal of the produced gas, there is an outlet in the upper part of the cone. It is advisable to arrange the gas outlet in the direction of the longitudinal axis of the cyclone. FIG. .1 shows a gas generator, a cut; in fig. 2 is a section A-A in FIG. one; in fig. 3 top of the gas generator. The gas generator for producing gas comprises a vertical housing 1 with fuel loading means having drive screw conveyors 2 installed in the lower part of the fuel receiving box 3, a gateway of a known type is located above. Instead of a screw conveyor, some other device can be used, such as a swing conveyor or a vibrator, etc. Below the fuel loading means is a pipeline 5 with nozzles 6 for introducing a gasification agent, for example air, oxygen, water vapor. The nozzles 6 are located at different heights. The part of the housing 1, which includes the fluidized bed gasification zone, has a conical section at the bottom. The upper and lower sections of this part are chosen in such a way that the face-1-i light fuel with a predetermined degree of graininess can be transported by the gasification agent from the gasification zone with a fixed bed and maintained in a suspended state. In the upper part of the housing 1, a cyclone 7 is centrally located, which operates in the usual way, swirling the gas flow entering it, and serves for the deposition of solid parts contained in the gas after the gasification in the fluidized bed, having an inlet device for gas 8 The device 8 consists of fixed blades 9 located in the TO ring (Fig. 2). In the upper part of the cyclone 7 there is a branch pipe 11 for the removal of gas. The gasification chamber 12 is adjacent to the cyclone 7, and a transition 13 is provided between the cyclone 7 and the gasification chamber 12, which is also the output of the cyclone. In junction 13, an injector 1 is located. A gasifying agent is supplied to injector k through line 15. The pressure of the agent may be higher than the gas pressure of the generator. Superheated steam and oxygen can be supplied as an agent. The particles captured in the cyclone 7 are picked up by the gasifying agent flow coming through the injector 1 A and fed to the ra-i chamber 10. At the same time, at temperatures exceeding the temperature nnaB of the lazy AOLA, for example, in the range from 1300 to 1500 ° C, full gasification of the fuel particles occurs. To remove the slag, a drum screen 16 is located in the lower part of the housing 1 and the gateway 17 Process is carried out as follows. Fuel is supplied to the housing 1 by means of charging. Pipeline 5 and nozzles 6 are fed into the housing 1 with a gasification agent. The gas containing solid particles formed as a result of gasification in a fluidized bed is directed to the cyclone 7 through the device 8. By means of the device 18 with guide vanes 19 the gas is brought into a helical or spiral motion. In the lower part the cyclone 7 has a funnel-shaped junction 13 connecting to the cooling system of the charging chamber 12. The latter is made in the form of a coil 20 enclosed in a shell of a refractory mass through which cold water flows. Water enters through conduit 21, which passes along the walls of the cyclone 7, and, after being used in coil 20, is directed along conduit 2, which also passes along the wall of the cyclone 7, to waste water supply system 23. In junction 13 there is an injector 1 with one or more nozzles made inclined with respect to the central axis and / or off-center. To the injector l, there are two pipelines 2k and 25 from above, which run along the walls of the cyclone 7 inside the cold water pipelines 21 and 22. Pipeline 2k can serve to supply oxygen, and pipe 25 to supply water vapor to the injector 14. , there is a concentric arrangement of pipelines, i.e. the pipelines for supplying the gasification agent pass inside the pipelines with water, as if they are in the head. Gasification of particles coming from the cyclone 7 is carried out in chamber 12. The gas, purified from solid fuel particles, exits the cyclone 7 through the central nozzle 11. The design of the described device can be different. This applies, for example, to the crepe / 1eni, support or suspension assemblies of the cyclone 7 in the head section. The head of the cyclone 7 in its upper part can be tightly closed with a cover. To install the cyclone 7 or for disassembly, it is enough just to remove this cover. Ometeto the cover you can also install a smaller flange. The cyclone head 7 can enter directly into the body 1 or be an independent unit that is attached to the body with sufficient density. To do this, you must have a connecting flange 26, shown in the drawing by the dotted line. Such an implementation of the method and implementation of a gas generator allows to intensify the process by gasifying the captured particles above the gasified fuel layer, which allows to increase the carbon utilization rate of fuel, Claim 1. Method of producing gas from solid fuel, including its gasification in the fluidized bed. , the separation of solid particles from gas under the action of centrifugal forces in a cyclone placed in the reaction space above the fluidized bed, characterized in that, for the purpose of pecifications process, the separated solids outlet of a cyclone is subjected to gasification of the fluidized bed in the supplementary gasifying agent flow and gasification products are fed into the fluidized bed. 2. A gas generator to produce gas from a solid fuel in a fluidized bed, comprising a vertical body with means for loading fuel and a pipeline for supplying a gasification agent and a cyclone located in the upper part of the body and having nozzles for gas and solid particles, that the cyclone is equipped with a gasification chamber connected to a nozzle for the removal of solid particles and having an injector for introducing a gasification agent. 3. Gas generator according to claim 2, Q..T, characterized in that the injector is located between the pipe for extracting solid particles from the cyclone and the gasification chamber. k. The gas generator on the PP. 2 and 3, which is based on the guide vanes installed in the upper part of the cyclone. 5.Gasogenerator on PP. 2-A, which is the case with the fact that the pipe for gas withdrawal from the cyclone is located along its vertical axis. 6.Gasogenerator on PP. 2-5 ° t l and h and y and the fact that the gasification chamber is provided with pipelines for supplying a cooling agent. 7. The gas generator on the PP. 2- $, differing t "", which is true; A gas supply agent injection line and an injector located inside the pipelines for supplying a cooling agent. / Sources of information received in cInaNie during examination 1.US Patent 1G 2803530, cl. W-206, pub. 1957.
    [2]
    2. F.H. Kohlevergasung Warme, 1976, p. 43 (prototype).
    //
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    引用文献:
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    法律状态:
    优先权:
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