• 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:
    An improvement in a process for periodically sluicing residues which are produced when gasifying ash-containing fuels with oxygen or an oxygen-containing composition under a pressure of 10 to 200 bars wherein ash is granulated in a water bath connected to a gasification chamber, suspended in water and passed into a non-pressurized collecting vessel provided with a conveyor is described. The improvement comprises: a. discharging the residue from said water bath which is maintained in fluid communication with said gasification chamber via a lock vessel, said lock vessel being connected to a surge tank which contains water so that the lock vessel remains constantly filled with water; b. equalizing the pressure between said lock vessel and said gasification chamber including said water bath by opening a connection to a process water feed line for said water bath and admitting water therein; c. depressurizing said lock vessel and removing liberated gases (previously dissolved in the water) and steam therefrom by opening a connection between said lock vessel and said surge tank; d. discharging suspended and granulated residues from said lock vessel into a collecting vessel by flushing said lock vessel with an adjustable amount of water flowing from said surge tank; and e. adjusting the water level in the collection vessel during the time the lock vessel is open so that the water level is sufficiently high such that no gas penetrates the lock vessel from the outside and the water level in the lock vessel does not sink.
    公开号:SU993825A3
    申请号:SU792783749
    申请日:1979-07-02
    公开日:1983-01-30
    发明作者:Шмидт Фолькмар；Лидер Бернхард；Шеве Гейнрих；Дорен Ганс
    申请人:Рурхеми Аг (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to the removal of residues, in particular to a method for removing residues from a gasifier, as well as to a device for carrying it out.
    A known method of removing residues 5 to the gasifier, including supplying water to the water bath of the gasifier, granulating the residues in the water bath, supplying water to the gateway from the tank, equalizing the pressure between the gateway u and the gasifier, removing residues suspended in the water from the water bath to the gateway, lowering gateway pressure £ ΐ · 3.
    A device is known for removing residues from the gasifier, including a water bath in the lower part of the gasifier, connected to a gateway located above it through a pipeline with locking elements located in it and equipped with a pipeline for supplying water to the lower part of the gasifier, a tank for supplying water to the gateway located above the lock and at a distance from it, and a container for receiving solid residues, connected to the lower part of the lock through a pipeline with a locking element located in it, the upper part of the lock connected to the lower it part of the tank for supplying water to the airlock through a pipeline with a locking body located in it [1].
    A disadvantage of the known device is that the pressure equalization in the lock is carried out using an inert gas, for example nitrogen, supplied to the tank for supplying water to the lock, which not only complicates the process, but also negatively affects its duration, since the pressure equalization has place only after bringing to a preset value of the gas pad In the upper part of the tank. In addition, the duration of the process is adversely affected by the fact that the slag is removed from its mixture with water. only after release from the second gateway.
    The purpose of the invention is to accelerate the process of removing residues from the gasifier.
    This object is achieved in that according to a method for removing residues from the gasifier 5 Cove, comprising feeding water into a water bath gasifier granulation residues in the water bath, the water supply from the tank to the gateway, to a pressure equalization between the gateway and the gateway gasifier by connecting to a pipeline for water supply to the water bath, removal of suspended water: residues in the water from the water bath to the lock, lowering the pressure of the lock by connecting the lock and the tank for supplying water to the lock,
    Pressure equalization between the gateway and the gasifier is conducted by connecting the gateway to the line m to supply water into the water bath and gateway pressure reduction is carried out by 'connecting the gateway to the container for supplying water to the gateway.
    Removal of residues from the $ 2 water bath to the airlock is carried out using an injector.
    A device for implementing the proposed method comprises a water bath in the lower part of the gasifier, connected to a gateway located above it through a pipeline with locking elements located in it and equipped with a pipeline for supplying water to the lower part of the gasifier, a tank for supplying water to the gateway located above the gateway and at a distance from 35 of it, and a container for receiving solid residues connected to the lower part of the airlock through a pipeline with a locking body located in it, and the upper part of the airlock is connected to 40 lower hours The water tank for supplying water to the airlock through a pipeline with a locking body located in it and characterized in that the lower part of the airlock is equipped with a pipeline for supplying 43 water to the lower part of the gasifier, and the lower part of the tank for supplying water to the airlock is equipped with an additional pipeline with in it, a pressure reducing valve connected to a pipeline 50 connecting the upper part of the airlock with the lower part of the tank for supplying water to the airlock.
    The container for receiving solid residues is located directly under the 55 gateway. . .
    In the pipeline for supplying water to the lower part of the gasifier, there is a water-jet injector connected to the upper part of the lock through the pipeline with a shut-off element located in it.
    A water jet injector may be located in the pipeline for supplying water to the water bath. Solid residues granulated in a water bath during filling of the lock due to their own weight are automatically * immersed in the lock.
    With a very fine-grained consistency, the remainder is fed from the water bath to the airlock using an injector. The injector is brought by the process water flowing to the water bath. At the same time, he sucks out at least as much water from the airlock as the incoming residues displace.
    During removal through the lock after the opening of one locking element between the lock and the collector, granular residues in the lock go down from the lock to the collector due to their greater specific gravity than the specific gravity of water, or due to the additional opening of the connecting pipe between the collector and the lock through the fresh water sluice is washed away [together with the sluice water in the sbrrni ^. Of particular importance is that according to the proposed method, fresh water from the collector enters the airlock without penetration of gas or steam from the outside. The amount of fresh water can be set by regulating the locking device between the receiver and the gateway and controlled by monitoring the water level in the receiver. Thus, it is possible to maintain the removal of residues from the airlock by means of a directed flushing action, to compensate for the flow of water in the receiver and to control> the temperature of the water in the airlock.
    As fresh water in the receiver, you can use both fresh tap water and chilled, purified and double-circulated circulating water from the flushing system of the gas obtained in the gasifier.
    The receiver is connected on the gas outlet side to a closed gas cycle under constant atmospheric or lower elevated pressure. The granular residues periodically removed from the sluice 5 993825 6 enter the collection tank ’(a tank for receiving solid residues) operating at normal pressure. The water level in the collector is set at least in this way. so that gas cannot penetrate into the airlock from below and the low pressure formed in the upper part of the airlock is not so large that the water column breaks off due to formation of steam. Granular residues can be removed from the receiver in a known manner by means of mechanical conveyors (for example, a scraper conveyor, bucket elevator, belt sieve) or hydraulically. During mechanical transportation, the amount of contaminated water is kept small; if hydropower transportation is used, 20 ku, then after sedimentation of the residues, water is returned to the collection tank.
    Different sedimentation of particles is used in the collection, so that small solid particles from gasification residues, which for the most part consist of carbon-containing particles that are not burnt in the gasifier, can be separated from the rapidly settling large particles of slag and fed again during gasification. ,
    To carry out the proposed method is a gateway system, consisting mainly of a gateway, collector and receiver. The gateway has such dimensions that the number of unloading cycles per unit time is kept small so that it falls into the gas. Slag can be reliably removed. It is advisable to carry out no more
    8-12 cycles ’discharge per hour.
    The dimensions of the collector and receiver are selected in such a way that reliable operation is ensured even at the lowest water level. Suspension of the gateway is advisable to carry out on the surrounding gasification chamber as-. a clave, in which the thermal expansion of both chambers between themselves or with respect to the surrounding supporting structure does not lead to damage. As a result of this, all connections to the compensator are made elastic. To protect against uncontrolled effects of forces on valves and connecting pipelines caused by the large dead weight of pressure-sensitive elements, thermal expansion or external forces, the lock is elastically connected to the autoclave surrounding the gasification chamber so that the lock can move to the side. Additionally, the gateway can be spring-loaded. puppy in an autoclave. Thus, it is achieved that the self-weight of all suspended parts during thermal expansion is fully compensated and does not affect the fittings. The side guides of the airlock in the supporting structure are designed so that a vertical tensile movement is possible.
    A gate is used as a shutoff member between the slag-conducting chambers, however, a spherical crane with a large free cross section is preferred. Spherical cranes can be made with smooth walls, without corners, edges and dead spaces. Slag granules suspended in water can pass through them without hindrance. Balls and landing surfaces, which are particularly subject to the abrasive action of slag, are equipped with wear-resistant armor. The locking elements must be suitable for operation at high water temperatures. The drive of the locking elements is designed for a maximum differential pressure. so that in case of interference they can be closed against the full pressure of gasification. When removing Kd slots through the gateway, switching occurs when pressure is equalized.
    For safety, an additional locking element is provided immediately in front of the gasifier, which is constantly open during normal removal. It is equipped with a separate reliable drive system and, in case of interference, automatically locks the gasification chamber.
    The drawing shows a device for implementing the proposed method.
    The device includes a water bath 2 located at the bottom of the gasifier 1, a safety shutoff 3, an elastic connection 4, a shutoff 5, airlock 6, pipe 7, valve 8, regulator 9, a throttle body 10, pipe 11, injector 12; level gauge 13, shutoff member 14, pressure reducing member 15, pipelines 16 and 17, receiver 18 (water supply tank
    Ί to the gateway), 19 ”pipeline gauge
    20, a locking member 21, a collection 22 (container for the receiver of solid residues).
    The device operates as follows 5.
    The gasification residues falling in the gasifier 1 at a pressure of 20-80 bar and a temperature of 1100-1500 ° C are fed into the water bath 2, where they are zeroed through a constantly open safety shut-off element 3, an elastic connection 4, for example, a compensator, an open shut-off body 5 slag suspended in water enters the sluice 6, which is under the same high pressure as the gasifier.
    The water bath 2 has a high temperature depending on the partial pressure of water 20 steam in the synthesis gas, for example 180 ° C. In order to prevent a high concentration of dissolved salts and fine-grained solid particles from gasification residues, 25, the amount of circulating water regulated by valve 8 is constantly supplied through line 7. The regulator 9 of a constant level by ^ casting the throttle body ZO 10 maintains a constant water level in the waste pipe 11. Fine-grained residues with poor sedimentation by means of a suction, the action of the injector 12 can be removed from the water bath 2 to the gateway 6. The water withdrawn from the gateway 6 is returned together with the process water as the injector drive medium to the water bath 2.
    Once the gateway 6 is filled with the desired degree of granular residues (or after triggering the transmitter 1-3) | shutoff element 5 (in 45 The case of tea need to shut-off valve 14) closes with the injector face 12, and the gateway 6 by opening the pressure-reducing body 15 is discharged through conduit 16 and the peripheral I water pipeline 17 to the receiver 18. The receiver 18 via a conduit 19 connected to a closed cycle gas which are under constant slightly elevated pressure, e.g. 5,002,000 mm water. Art. or under atmospheric pressure 55 .
    After the pressure gauge 20 indicates a pressure drop in the lock 6, the shut-off member 21 opens the lock, so that the granular residues are immersed in the water-filled collector 22 without pressure. As soon as the slag leaves the lock, which, if necessary, is shown on the second level gauge 23, due to the short-term opening of the large-sized feeding organ 24, a large amount of fresh water is supplied through the pipe 16 from the receiver 18 to the lock 6. The remaining residues, together with the lock, are heated with slag water. washed in the collection 22. With fine-grained residues with poor sedimentation, it is possible to open the supply body 24 before opening the body 21, so that the flushing action of the flowing water from the collection is fully used to remove gasification residues. The rapid decrease in water level in the receiver 18 further indicates that the gateway 6 is free from residues. Idle of the receiver 18 is prevented by the constant level controller 25 by closing the shut-off element 21. The level gauge 26 in the upper part of the gateway 6 gives an alarm and locks both shut-off bodies 3 and 5 or blocks their opening if, in case of malfunctions, the water level in the gateway 6 drops.
    During operation of the injector 12, steam is generated during unloading due to the hot water entering the airlock 6. In this case, the water level in the gateway should be maintained by coordinating the unloading and supply of fresh water.
    After supplying a sufficient amount of fresh water to the airlock 6, the constant-level controller 25 locks the shut-off element 21. In addition, the pressure-reducing organ 15 and the supplying organ are closed. Due to the opening of the equalizing valve 27 through the pipe 28, which is connected to the pipe 7 "there is a pressure equalization between the gateway and the gasifier 1. Differential pressure gauge 29 shows this pressure equalization. Due to the opening of the locking member 5, the newly granulated residues in suspended form from the water bath 2 enter the airlock 6.
    The reduced fresh water level in the receiver 18 by means of a new command of the constant level controller 25 9 993825 due to the opening of the valve 30 into the supply pipe 31 is again replenished. In the collector 22 under atmospheric pressure, the introduced larger particles of slag 5 quickly sink, while the rate of immersion of small carbon-containing particles is much lower. Therefore, after a certain time, together with excess water, they can be removed <0 from collector 22 using pump 32 and recirculated into the gasification process through water treatment. The water level is regulated by means of a constant level controller 33 by locking the shut-off element 34 in the drain pipe 35. Only then a known device for removing slag is used, for example, a mechanical scraper conveyor operating with such a capacity that it takes time until the next discharge gateway slag is removed from the collection.
    The entire removal process usually proceeds automatically. Manual operations are possible, and dangerous erroneous inclusions are reliably prevented.
    The lock 6 with an elastic connection 4 is movably suspended on the autoclave surrounding the gasification chamber 1, which in turn is supported by a plurality of vanes 36 in the supporting structure. Net weight of the suspended parts is compensated by springs 37 and is not affected by such ob- 3J time on fixtures 3 ~ 5.
    权利要求:
    Claims (3)
    [1]
    39 The purpose of the invention is to accelerate the process of removing residues from the gasifier. This goal is achieved in that according to the method of removing residues from the gasifier, which includes pouring water into the water bath of the gasifier, granulating the residue in the water, supplying water to the lock from the tank, equalizing the pressure between the lock and the gasifier by connecting the lock to the pipeline to supply water in a water bath, removal of residues suspended in water from the water bath to the sluice, pressure decrease in the sluice by connecting the sluice and the tank for water supply to the sluice. The equalization of pressure between the gateway and the gasifier is carried out by connecting the gateway to the pipeline for supplying water to the water bath and by reducing the pressure of the gateway by connecting the gateway to the tank for supplying water to the gateway. Removal of residues from the water bath to the sluice is carried out by means of an injector. The device for carrying out the proposed method contains a water bath in the lower part of the gasifier connected to the sluice located above it through a pipeline with shut-off members located in it and equipped with a pipeline for supplying water to the lower a portion of the gas fixator, a tank for supplying water to the gateway located above the gateway and at a distance from the Negro, and a tank for receiving solid residues connected to the lower part of the gateway through a pipeline located in it an anchor body, the upper part of the gateway is connected to the lower part of the tank for supplying water to the gateway through a pipeline with a shut-off element in it, which is dispersed in it, and characterized in that the lower part of the gateway is equipped with a pipeline for supplying water to the lower part of the gasifier The water supply tanks to the gateway are provided with an additional pipe with a reduction valve placed in it and connected to the pipeline that connects the upper part of the gateway with the lower part of the tank to supply water to the gateway. A container for receiving solid residues is located directly below the gateway. In the pipeline for supplying water to the lower part of the gasifier, there is a water jet and an injector connected to the upper part of the sluice through the pipeline with a stop valve placed in it. A water jet injector may be located in the pipeline to supply water to the water bath. The solid ocf granulated in the WATER TUB, during the filling of the sluice due to their own weight, are automatically immersed in the sluice. With a very fine-grained consistency, residues are transferred from the water bath to the sluice by means of an injector. The injector is driven by the process water flowing to the water bath. At the same time, it sucks at least as much water from the sluice as it displaces incoming residues. During the removal through the gateway after opening one valve body between the gateway and the collector, the remains of the granular remains in the gateway are lowered down from the gateway into the collection due to their greater specific weight than the specific weight of water, or due to the additional opening of the connecting pipe between the collection and the gateway through the incoming the fresh water gateway is washed out with the water of the gateway in the dump. Of particular importance is that, according to the proposed method, fresh water from the collection enters the sluice without penetration of gas or vapor from outside. The amount of fresh water can be set by adjusting the locking device between the receiver and the gateway and monitored by monitoring the water level in the receiver. Thus, it is possible to maintain the removal of residues from the sluice by directing the flushing action, to compensate for the water flow in the receiver and to regulate the water temperature in the sluice. As fresh water in the receiver, it is possible to use both fresh tap water, and cooled, purified and out-circulated circulating water from the washing system of the gas produced in the gasifier. The receiver is connected on the gas outlet side with a closed gas cycle, which is under constant atmospheric pressure or lower overpressure. The granular residues periodically removed from the sluice enter the water-filled collector (capacity for receiving solid residues), p) 6o1, at normal pressure. The water level in the collector is set at least so high that the gas cannot penetrate from below into the junction and the reduced pressure formed in the upper part of the sluice is not so large that the water column breaks off due to the formation of steam. The granulated residues can be removed from the receiver in a known manner by mechanical conveyors (e.g. a scraper conveyor, a bucket elevator, a belt sieve) or hydraulically. During mechanical transport, the amount of contaminated water is kept low, but if hydroelastic transportation is used, after sedimentation residual water is returned to the collection. The collection uses different sedimentation of particles, which are small solid particles from gasification residues, which are mostly composed of carbon-containing particles unburned in the gasifier, can be separated from the rapidly coarse slag particles and fed back to the gasification process. For - carrying out the proposed method serves as a lock system, consisting mainly of a gateway, a collector and a receiver. The gateway is of such dimensions that the number of unloading cycles per unit of time is supported in a large way so that the slag that falls in the gasifier can be reliably removed. It is advisable to spend no more than 8-12 discharge cycles per hour. Dimensions of the collector and receiver are chosen in such a way that even at the lowest level of water, it provides reliable operation. Suspension of the sluice is advisable to be carried out on the autoclave, which surrounds the gasification chamber, in which the thermal expansion of both chambers between themselves or with respect to the surrounding supporting structure does not lead to disruption. As a result, all connections to the compensator are elastic. To protect against uncontrolled forces acting on the armature and the connecting pipelines causing a large own weight of pressure-sensing elements, thermal expansion or external forces, the sluice gate is connected to the surrounding gasification chamber by an autoclave so that the gateway can be moved to the side. Additionally, the gateway can be spring-loaded in an autoclave. In this way it is achieved that the own weight of all suspended parts during thermal expansion is fully compensated and does not affect the valve. The side guides of the sluice in the support structure are designed in such a way that a vertical tensile movement is possible. A gate is used as a closure member between the slag-conducting chambers, however, a spherical valve with a large free cross-section Sfe is preferred. Spiral taps can be made with smooth walls, without corners, edges and dead spaces. Slag granules suspended in water can pass through them without obstruction. Balls and seating surfaces, which are particularly subject to -. abrasive slag, equipped with wear-resistant armor. Constipated organs should be suitable for operation at high temperatures. The drive of the locking bodies is designed for a maximum pressure difference, so that in case of interference they can close against the full pressure of gasification. When slag is removed through a bridging / transfer gateway, pressure equalization occurs. For the purpose of safety, an additional closure member is provided directly in front of the gasifier, which, during normal removal mode, is permanently open. It is equipped with a separate reliable drive system and automatically locks the gasification chamber in case of interference. The drawing shows a device for carrying out the proposed method. The device includes a water bath 2, located at the bottom of the gasifier, 2, a safety valve 3, an elastic connection li, a valve 5, a gateway 6, a pipeline 7, a valve B, is adjustable (H 9, a throttle body 10, a pipeline 11, an injector 12i gauge 13 shutoff valve ik, reduction sphgan 15, pipelines 1b and 17, receiver 18 (tank for supplying water to the sluice), pipe 19, pressure gauge 20, stop valve 21, collector 22 (tank for solid residue collectors). Discharged into the gas indicator 1 at a pressure of 20-80 bar and a temperature of 1100-1500С gasification residues are fed into a water bath 2, where they are granulated and through a permanently open safety valve 3, an elastic connection k, such as a compensator, an open valve 5, the slag suspended in water enters The water at bath 2 has a high temperature dependent on the partial pressure of water vapor in the synthesis gas, for example 180 ° C. In order to prevent a high concentration of dissolved salts and fine-grained TREE of particles from gasification residues, the amount of circulating water, which is controlled by means of valve 8, is continuously supplied through pipe 7. The constant level regulator 9 maintains a constant water level in the drain pipe 11 by bringing in the throttle body 10. Medium grain residues with poor sedimentation using suction. the actions of injector 12 can be removed from water bath 2 to gateway 6. The water discharged from gateway 6 is returned together with the process water as the driving medium of the injector to the water bath 2. As soon as gateway 6 is filled to the desired degree granular with residues (or after triggering of unemer 13) i, the locking member 5 (if necessary, the locking member 14 is closed on the side of the injector 12 and the gateway 6 by opening the reducing member 15 is discharged through the pipeline 16 and the circumferential pipeline 17 to the receiver 18. The receiver 18 The gutter 19 is connected to a closed gas cycle, which is under a constant slightly increased pressure, for example, 5002000 mm of water or atmospheric pressure. After the pressure gauge 20 shows the pressure drop in the gateway 6, 9 58, the stop valve 21 opens the gateway, that the granulated residues are immersed in a pressure-filled reservoir 22. Without the slag leaving the sluice, which, if necessary, is shown on the second level gauge 23, due to the short-term opening of the large feed body 2 through pipeline 1b and From receiver 18, a large amount of fresh water is supplied to gateway 6. The remaining residues together with the water heated by slag are the gateway. washed into the collector 22. With fine-grained residues with poor sedimentation, it is possible to open the delivery organ 2k before opening the organ 21, so that the washing action of the flowing water from the collection is completely used to remove the gasification residues. The rapid lowering of the water level in the receiver 18 further indicates that gateway 6 is free from residues. The idle of the receiver 18 is prevented by the constant level controller 25 by closing the shut-off organ 21. The level gauge 26 in the upper part of the gateway 6 gives an alarm and locks both the shut-off parts 3 and 5 or blocks their opening if the level of the water in the gateway 6 drops in case of malfunctions During operation of the injector 12, steam is formed during unloading due to the hot water entering the gateway 6. In this case, the water level in the airlock should be maintained by coordinating the unloading and supplying fresh water. After supplying a sufficient amount of fresh water to the gateway 6, the constant level regulator 25 closes the shut-off member 21. In addition, the reducing member 15 and the supply member 2 are closed. Due to the equalizing valve 27 opening through line 28, which is connected to line 7, pressure is equalized gateway and gasifier 1. Differential pressure gauge 29 shows E1O pressure equalization. Due to the opening of the closure body 5, the newly granulated residues in suspended form from water bath 2 enter gateway 6. The reduced level of fresh water in the receiver 18 is through a new command of the constant level controller 25. Because of the opening of the valve 30, the supply line 31 is again returned. In atmospheric pressure collector 22, the injected, larger slag particles are quickly submerged, while the submerged speed of the fine carbonaceous particles is much lower. Therefore, after a certain time, along with the excess water, they can be removed from the collector 22 by means of a pump 32 and recycled through the water treatment to the gasification process. The water level is controlled by a constant level regulator 33 by locking the shut-off member 3 in the drain pipe 35. Only then a known slag removal device is used, for example, a mechanical scraper conveyor operating at such a rate that the slag yut from collection. The entire removal process usually proceeds automatically. Manual operations are possible, and dangerous erroneous inclusions are reliably prevented. Gateway 6 with an elastic joint l is movably suspended from the surrounding autoclave gasification chamber 1, which in turn is supported by a plurality of blades 36 in the support structure. The own weight of all the hanging parts is compensated by the springs 37 and, therefore, does not affect the valves 3-5. Formula of the invention 1. Method of removing residues from ha. zifikatora, including the flow of water into the water bath of the gasifier, granulation of residues in the water bath, the flow of water into the gateway from the tank, pressure equalization meA (do gateway and gasifier, removal of water suspended in the water bath into the gateway, lowering the gateway pressure characterized in that, in order to speed up the process, pressure equalization between the gateway and the gasifier is carried out by connecting the gateway to the pipeline for supplying water to the water bath and lowering the gateway 5 pressure by connecting the gateway to the tank the water supply to the gateway.
    [2]
    2. A method according to claim 1, characterized in that the removal of residues from the water bath to the sluice is carried out by means of an injector.
    [3]
    3. A device for removing residues from the gasifier, including a water bath in the lower part of the gasifier, connected to a gateway located above it through a pipeline with shut-off members located in it and equipped with a pipeline to supply water to the bottom part of the gasifier, a container for supplying water to the gateway, located above the gateway and at a distance from it, and a container for receiving solid residues, connected to the lower part of the gateway through a pipeline with a locking organ placed in it, the upper part of the gateway being connected to the lower hour Capacities for supplying water to the sluice through a pipeline with a shut-off valve placed in it, characterized in that, in order to speed up the process, the lower part of the lock is equipped with a pipeline with a shut-off valve placed in it connected to the pipeline for gasifier, and the lower part of the tank for supplying water to the gateway is equipped with an additional pipeline with a pressure relief valve placed in it, connected to the pipeline connecting the upper part of the gateway with the lower part of the tank for supplying water to the gateway. . A device according to claim 3, characterized in that the container for receiving solid residues is located directly under the gateway. 5. An apparatus according to claim 3, characterized in that a water jet injector is located in the pipeline for supplying water to the lower part of the gasifier, which is connected to the upper part of the sluice through a pipeline with a locking member located in it. Sources of information, taken into account in the examination 1. US patent number 3235313, CL, 302-1, 1966.
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    同族专利:
    公开号 | 公开日
    JPS6024832B2|1985-06-14|
    IN152244B|1983-11-26|
    US4425139A|1984-01-10|
    ZA793249B|1980-07-30|
    DE2829629A1|1980-01-24|
    GB2026145B|1982-11-24|
    BR7904201A|1980-03-25|
    PL117287B1|1981-07-31|
    GB2026145A|1980-01-30|
    US4381924A|1983-05-03|
    NL176866C|1985-06-17|
    AU4869079A|1980-01-10|
    AU528822B2|1983-05-12|
    PL216744A1|1980-03-24|
    JPS5512181A|1980-01-28|
    CA1147556A|1983-06-07|
    NL7808331A|1980-01-08|
    DE2829629C2|1982-07-29|
    引用文献:
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    法律状态:
    优先权:
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