JP5721612B2 - Slag discharge system - Google Patents

Description

  The present invention relates to a slag discharge system that discharges slag generated in, for example, a gasification furnace.

  For example, a combined coal gasification power generation facility is a power generation facility that aims to further increase the efficiency and environmental performance compared to conventional coal-fired power generation by gasifying coal and combining it with combined cycle power generation. This coal gasification combined cycle power generation facility has a great merit that it can use coal with abundant resources, and it is known that the merit can be further increased by expanding the applicable coal types.

  Conventional coal gasification combined power generation facilities generally have a coal supply device, a drying device, a coal gasification furnace, a gas purification device, a gas turbine facility, a steam turbine facility, an exhaust heat recovery boiler, a gas purification device, and the like. ing. Therefore, the coal is dried and then pulverized, supplied to the coal gasifier as pulverized coal, and air is taken in. The coal gas is combusted and gasified in this coal gasifier, and the product gas (combustible) Gas) is produced. Then, the product gas is purified and then supplied to the gas turbine equipment to burn and generate high-temperature and high-pressure combustion gas to drive the turbine. The exhaust gas after driving the turbine recovers thermal energy by the exhaust heat recovery boiler, generates steam and supplies it to the steam turbine equipment, and drives the turbine. As a result, power generation is performed. On the other hand, the exhaust gas from which the thermal energy has been recovered is released into the atmosphere through a chimney after harmful substances are removed by the gas purification device.

  By the way, in such a coal gasification combined power generation facility, in a coal gasification furnace, coal is combusted and gasified to generate product gas, while slag is generated as a burner. It is necessary to discharge from the furnace. Since the slag is hot, it has fluidity and is continuously discharged from a slag hole provided in the lower part of the coal gasification furnace. And the slag discharged | emitted from the coal gasification furnace is water-cooled with a cooling tank, and becomes a granulated slag particle. This granulated slag is periodically discharged from a slag lock hopper and settled in a slag reservoir, slurried in a slurry tank by a scraper conveyor or a screw conveyor, and then transported to a slag storage tank through a slurry pipe.

  An example of such a slag discharge system is described in Patent Document 1 below.

JP 2011-074274 A

  In the conventional slag discharge system described above, a cooling tank is provided in the lower part of the coal gasification furnace, and a slag lock hopper, a slag reservoir, a slurry tank, and the like are arranged in series below the cooling tank. Therefore, the height of the slag discharge system becomes very high, the height of the gantry for supporting various devices is also high, and it is necessary to ensure sufficient rigidity, so that the construction cost increases. There's a problem.

  The present invention solves the above-described problems, and an object of the present invention is to provide a slag discharge system that simplifies the apparatus and can reduce the construction cost.

  In order to achieve the above object, the slag discharge system of the present invention includes a cooling tank that cools hot slag with water, a slag discharged from a lower portion of the cooling tank, a slag tank that stores water, and the slag tank. A slurry transport path for transporting slurry of slag and water stored in the slurry, a slurry tank for storing the slurry transported by the slurry transport path, a decompression valve for decompressing the slurry tank, and the slurry tank after decompression And a slag storage tank for storing slag discharged from the lower part of the slag.

  Accordingly, when the high-temperature slag is cooled by water in the cooling tank, the slag and water are discharged and stored in the slag tank from below, and the slurry of slag and water stored in the slag tank is slurried by the slurry transport path. The slurry tank is depressurized by opening the pressure reducing valve and then depressurized, and then the slag is discharged from the lower part of the slurry tank to the slag storage tank. For this reason, slurry of slag and water is generated by the slag tank, and the pressure difference between the slurry conveyance area and the slag discharge area is absorbed by the slurry tank, so it is only necessary to arrange the slag tank below the cooling tank. The equipment can be simplified and the construction cost can be reduced.

  In the slag discharge system of the present invention, a shut-off valve capable of opening and closing the slurry conveyance path, a discharge valve for opening and closing the discharge portion of the slurry tank, and a slag storage amount detection unit for detecting a slag storage amount in the slurry tank, A control device capable of controlling the opening / closing of the pressure reducing valve, the shutoff valve, and the discharge valve based on a detection result of the slag storage amount detection unit, and the control device sets a slag storage amount in the slurry tank in advance. When the predetermined slag storage amount is reached, the shut-off valve is closed and the pressure reducing valve is opened, and when the pressure reduction of the slurry tank is completed, the discharge valve is opened.

  Therefore, when the slag storage amount in the slurry tank reaches a predetermined slag storage amount, that is, full load, the control device closes the shut-off valve and opens the pressure reducing valve to make the inside of the slurry tank normal pressure, and the discharge valve By releasing the slag, the slag is discharged to the slag storage tank, and the slag can be discharged safely.

  In the slag discharge system of the present invention, the slurry tank has a separation function of separating slag and water, and is characterized in that a drainage path for discharging water separated from the slag is provided.

  Therefore, the slurry tank separates the conveyed slurry into slag and water, and discharges the slag from the lower part of the slurry tank to the slag storage tank, while draining water from the drainage path. By mainly discharging only the slag, an increase in the size of the slag storage tank can be suppressed.

  In the slag discharge system of the present invention, the water separated from the slag in the slurry tank is returned to the cooling tank or the slag tank through the drainage path.

  Therefore, the slurry tank separates the conveyed slurry into slag and water, drains the water from the drainage path, and returns it to the cooling tank or slag tank. Can be reduced.

  In the slag discharge system of the present invention, a water supply path for supplying water to the slurry tank and a water supply valve capable of opening and closing the water supply path are provided, and when the slurry in the slurry tank is discharged, The discharge valve is closed to open the water supply valve, and when the air in the slurry tank is discharged, the water supply valve and the pressure reducing valve are closed.

  Therefore, when the slurry in the slurry tank is discharged, the control device discharges the air in the slurry tank by closing the discharge valve and opening the water supply valve, and by eliminating the air in the slurry tank, It is possible to prevent the air from entering the cooling tank and the slag tank and to facilitate the slurry conveyance.

  In the slag discharge system of the present invention, a water storage tank for storing water separated from the slag storage tank is provided, and the water supply path supplies water from the water storage tank to the slurry tank, the cooling tank, or the slag tank. It is characterized by doing.

  Therefore, by supplying the water separated from the slag storage tank to the slurry tank, the cooling tank, or the slag tank, the water can be reused as the circulating water, thereby reducing the processing cost.

  In the slag discharge system of the present invention, a plurality of the slurry tanks are provided and selectively used according to the slag storage amount.

  Therefore, by selectively using a plurality of slurry tanks according to the amount of slag stored, it becomes possible to perform slag processing continuously and improve processing efficiency.

  According to the slag discharge system of the present invention, since the cooling tank, the slag tank, the slurry conveyance path, the slurry tank, the pressure reducing valve, and the slag storage tank are provided, the slurry of slag and water is generated by the slag tank. Since the pressure difference between the transfer area and the slag discharge area is absorbed by the slurry tank, it is only necessary to dispose the slag tank below the cooling tank, and the apparatus can be simplified and the construction cost can be reduced.

FIG. 1 is a schematic configuration diagram of a combined coal gasification combined power generation facility to which a slag discharge system according to Embodiment 1 of the present invention is applied. FIG. 2 is a schematic configuration diagram of the slag discharge system according to the first embodiment. FIG. 3 is a time chart showing slag discharge control by the slag discharge system of the first embodiment. FIG. 4 is a schematic configuration diagram of a slag discharge system according to Embodiment 2 of the present invention.

  Exemplary embodiments of a slag discharge system according to the present invention will be described below in detail with reference to the accompanying drawings. In addition, this invention is not limited by this Example, Moreover, when there exists multiple Example, what comprises combining each Example is also included.

  FIG. 1 is a schematic configuration diagram of a combined coal gasification combined power generation facility to which a slag discharge system according to Embodiment 1 of the present invention is applied, FIG. 2 is a schematic configuration diagram of a slag discharge system of Embodiment 1, and FIG. It is a time chart showing the slag discharge control by the slag discharge system of Example 1.

  The coal gasification combined power generation facility (IGCC: Integrated Coal Gasification Combined Cycle) of Example 1 adopts an air combustion method in which coal gas is generated in a gasification furnace using air as an oxidizer, and is purified by a gas purifier. Coal gas is supplied as fuel gas to gas turbine equipment to generate electricity. That is, the combined coal gasification combined power generation facility of this embodiment is a power generation facility of an air combustion system (air blowing). In this case, pulverized coal (coal) is used as a raw material supplied to the gasifier.

  In Example 1, as shown in FIG. 1, the coal gasification combined power generation facility 10 includes a coal supply device 11, a fluidized bed drying device 12, a pulverized coal machine (mill) 13, a coal gasification furnace 14, and a char recovery device 15. , A gas refining device 16, a gas turbine facility 17, a steam turbine facility 18, a generator 19, and a heat recovery steam generator (HRSG) 20.

  The coal feeder 11 includes a raw coal bunker 21, a coal feeder 22, and a crusher 23. The raw coal bunker 21 can store coal and can drop a predetermined amount of coal into the coal feeder 22. The coal feeder 22 can transport the coal dropped from the raw coal bunker 21 by a conveyor or the like and drop it on the crusher 23. The crusher 23 can crush the dropped coal into a predetermined size.

  The fluidized bed drying device 12 supplies drying steam (superheated steam) to the coal introduced by the coal supply device 11 so as to heat and dry the coal, and the moisture contained in the coal. Can be removed. The fluidized bed drying apparatus 12 is provided with a cooler 31 that cools the dried coal taken out from the lower portion, and the dried and cooled dried coal is stored in the dried coal bunker 32. Further, the fluidized bed drying apparatus 12 is provided with a dry coal cyclone 33 and a dry coal electrostatic precipitator 34 for separating dry coal particles from steam taken out from above, and the dry coal particles separated from the steam are dried coal bunker. 32 is stored. The steam from which the dry coal has been separated by the dry coal electrostatic precipitator 34 is compressed by the steam compressor 35 and then supplied to the fluidized bed drying device 12 as drying steam.

  The pulverized coal machine 13 is a coal pulverizer, and pulverizes coal (dried coal) dried by the fluidized bed dryer 12 into fine particles to produce pulverized coal. That is, in the pulverized coal machine 13, the dry coal stored in the dry coal bunker 32 is dropped by the coal feeder 36, and the dry coal is converted into coal having a predetermined particle size or less, that is, pulverized coal. The pulverized coal after being pulverized by the pulverized coal machine 13 is separated from the conveying gas by the pulverized coal bag filters 37a and 37b and stored in the pulverized coal supply hoppers 38a and 38b.

  The coal gasification furnace 14 can supply pulverized coal processed by the pulverized coal machine 13 and can be recycled by returning the char (unburned coal) recovered by the char recovery device 15. .

  That is, the coal gasification furnace 14 is connected to the compressed air supply line 41 from the gas turbine equipment 17 (compressor 61), and can supply compressed air compressed by the gas turbine equipment 17. The air separation device 42 separates and generates nitrogen and oxygen from air in the atmosphere. A first nitrogen supply line 43 is connected to the coal gasifier 14, and a pulverized coal supply hopper is connected to the first nitrogen supply line 43. Charging lines 44a and 44b from 38a and 38b are connected. The second nitrogen supply line 45 is also connected to the coal gasification furnace 14, and the char return line 46 from the char recovery device 15 is connected to the second nitrogen supply line 45. Further, the oxygen supply line 47 is connected to the compressed air supply line 41. In this case, nitrogen is used as a carrier gas for coal and char, and oxygen is used as an oxidant.

  The coal gasification furnace 14 is, for example, a spouted bed type gasification furnace, which combusts and gasifies coal, char, air (oxygen) supplied therein or water vapor as a gasifying agent, and produces carbon dioxide. A combustible gas (product gas, coal gas) containing carbon as a main component is generated, and a gasification reaction takes place using this combustible gas as a gasifying agent. In this case, the coal gasification furnace 14 is provided with a slag discharge system 48 that discharges slag generated in the lower part of the reaction furnace 14a. The coal gasification furnace 14 is not limited to a spouted bed gasification furnace, and may be a fluidized bed gasification furnace or a fixed bed gasification furnace. The coal gasification furnace 14 is provided with a gas generation line 49 for combustible gas toward the char recovery device 15, and can discharge combustible gas containing char. In this case, by providing a gas cooler in the gas generation line 49, the combustible gas may be cooled to a predetermined temperature and then supplied to the char recovery device 15.

  The char recovery device 15 includes a dust collector 51 and a supply hopper 52. In this case, the dust collector 51 is constituted by one or a plurality of bag filters or cyclones, and can separate char contained in the combustible gas generated in the coal gasification furnace 14. The combustible gas from which the char has been separated is sent to the gas purification device 16 through the gas discharge line 53. The supply hopper 52 stores the char separated from the combustible gas by the dust collector 51. A bin may be disposed between the dust collector 51 and the supply hopper 52, and a plurality of supply hoppers 52 may be connected to the bin. A char return line 46 from the supply hopper 52 is connected to the second nitrogen supply line 45.

The gas purification device 16 performs gas purification by removing impurities such as sulfur compounds and nitrogen compounds from the combustible gas from which the char has been separated by the char recovery device 15. The gas purifier 16 purifies the combustible gas to produce fuel gas and supplies it to the gas turbine equipment 17. In the gas purifier 16, since the combustible gas from which the char is separated still contains sulfur (H ₂ S), the sulfur is finally removed by removing it with the amine absorbent. Is recovered as gypsum and used effectively.

  The gas turbine equipment 17 includes a compressor 61, a combustor 62, and a turbine 63, and the compressor 61 and the turbine 63 are connected by a rotating shaft 64. The combustor 62 has a compressed air supply line 65 connected to the compressor 61, a fuel gas supply line 66 connected to the gas purifier 16, and a combustion gas supply line 67 connected to the turbine 63. Further, the gas turbine equipment 17 is provided with a compressed air supply line 41 extending from the compressor 61 to the coal gasification furnace 14, and a booster 68 is provided in the middle. Therefore, in the combustor 62, the compressed air supplied from the compressor 61 and the fuel gas supplied from the gas purifier 16 are mixed and burned, and the rotating shaft 64 is rotated by the generated combustion gas in the turbine 63. By doing so, the generator 19 can be driven.

  The steam turbine facility 18 includes a turbine 69 that is coupled to the rotating shaft 64 in the gas turbine facility 17, and the generator 19 is coupled to the base end portion of the rotating shaft 64. The exhaust heat recovery boiler 20 is provided in the exhaust gas line 70 from the gas turbine equipment 17 (the turbine 63), and generates steam by exchanging heat between the air and the high temperature exhaust gas. Therefore, the exhaust heat recovery boiler 20 is provided with the steam supply line 71 between the steam turbine equipment 18 and the turbine 69 of the steam turbine equipment 18, the steam recovery line 72 is provided, and the steam recovery line 72 is provided with the condenser 73. Yes. Therefore, in the steam turbine facility 18, the turbine 69 is driven by the steam supplied from the exhaust heat recovery boiler 20, and the generator 19 can be driven by rotating the rotating shaft 64.

  The exhaust gas from which heat has been recovered by the exhaust heat recovery boiler 20 is freed of harmful substances by the gas purification device 74, and the purified exhaust gas is discharged from the chimney 75 to the atmosphere.

  Here, the action | operation of the coal gasification combined cycle power generation equipment 10 of Example 1 is demonstrated.

  In the combined coal gasification combined power generation facility 10 of the first embodiment, the raw coal is stored in the raw coal bunker 21 by the coal feeder 11, and the coal in the raw coal bunker 21 is dropped on the crusher 23 by the coal feeder 22. Here, it is crushed into a predetermined size. The crushed coal is heated and dried by the fluidized bed drying device 12, cooled by the cooler 31, and stored in the dry coal bunker 32. Further, the steam taken out from the upper part of the fluidized bed drying device 12 is separated into dry coal particles by the dry coal cyclone 33 and the dry coal electrostatic precipitator 34 and compressed by the steam compressor 35 before being supplied to the fluidized bed drying device 12. Returned as drying steam. On the other hand, the dry coal particles separated from the steam are stored in the dry coal bunker 32.

  The dry coal stored in the dry coal bunker 32 is fed into the pulverized coal machine 13 by the coal feeder 36, where it is pulverized into fine particles to produce pulverized coal, and through the pulverized coal bag filters 37a and 37b. And stored in the pulverized coal supply hoppers 38a and 38b. The pulverized coal stored in the pulverized coal supply hoppers 38 a and 38 b is supplied to the coal gasification furnace 14 through the first nitrogen supply line 43 by nitrogen supplied from the air separation device 42. Further, the char recovered by the char recovery device 15 described later is supplied to the coal gasification furnace 14 through the second nitrogen line 45 by nitrogen supplied from the air separation device 42. Further, the compressed air extracted from the gas turbine equipment 17 to be described later is boosted by the booster 68 and then supplied to the coal gasification furnace 14 through the compressed air supply line 41 together with oxygen supplied from the air separation device 42.

  In the coal gasification furnace 14, the supplied pulverized coal and char are combusted by compressed air (oxygen), and the pulverized coal and char are gasified to generate combustible gas (coal gas) mainly composed of carbon dioxide. Can be generated. The combustible gas is discharged from the coal gasifier 14 through the gas generation line 49 and sent to the char recovery device 15.

  In the char recovery device 15, the combustible gas is first supplied to the dust collector 51, whereby the char contained in the gas is separated from the combustible gas. The combustible gas from which the char has been separated is sent to the gas purification device 16 through the gas discharge line 53. On the other hand, the fine char separated from the combustible gas is deposited on the supply hopper 52, returned to the coal gasifier 14 through the char return line 46, and recycled.

  The combustible gas from which the char has been separated by the char recovery device 15 is subjected to gas purification by removing impurities such as sulfur compounds and nitrogen compounds in the gas purification device 16 to produce fuel gas. In the gas turbine facility 17, when the compressor 61 generates compressed air and supplies the compressed air to the combustor 62, the combustor 62 is supplied from the compressed air supplied from the compressor 61 and the gas purification device 16. Combustion gas is generated by mixing with fuel gas and combusting, and the turbine 63 is driven by this combustion gas, so that the generator 19 can be driven via the rotating shaft 64 to generate power.

  The exhaust gas discharged from the turbine 63 in the gas turbine equipment 17 generates steam by exchanging heat with air in the exhaust heat recovery boiler 20, and supplies the generated steam to the steam turbine equipment 18. . In the steam turbine facility 18, the generator 69 can be driven through the rotating shaft 64 to generate electric power by driving the turbine 69 with the steam supplied from the exhaust heat recovery boiler 20.

  Thereafter, in the gas purification device 74, harmful substances in the exhaust gas discharged from the exhaust heat recovery boiler 20 are removed, and the purified exhaust gas is discharged from the chimney 75 to the atmosphere.

  In the above description, coal is used as a raw material. However, this coal can be applied to high-grade coal and low-grade coal, and is not limited to coal. Biomass used as a resource may be used. For example, thinned wood, waste wood, driftwood, grass, waste, sludge, tires, and recycled fuel (pellets and chips) made from these materials may be used. Is possible.

  Hereinafter, the slag discharge system 48 in the coal gasification combined power generation facility 10 described above will be described in detail.

  The slag discharge system 48 discharges the molten slag 201 accumulated at the bottom of the coal gasification furnace 14. In the slag discharge system 48, as shown in FIG. 2, the coal gasification furnace 14 (reaction furnace 14 a) is provided with a slag hole 101 for dropping the molten slag 201 at the bottom, and the slag is provided below the slag hole 101. A cooling tank 102 for storing the molten slag 201 dropped from the hole 101 is integrally provided. The cooling tank 102 is provided with a slag hopper 103 inside. The slag hopper 103 is formed in a funnel shape having a smaller inner diameter toward the lower side in the vertical direction, and the slag stored in the bottom of the cooling tank 102 is stored in the cooling tank 102. It is immersed in cooling water (cooling water) 202. The slag hopper 103 has an upper large-diameter opening located in the slag cooling water 202 and a lower small-diameter opening penetrating the bottom of the cooling tank 102 to the outside. Is installed so that the small-diameter opening can be opened and closed.

  Accordingly, the molten slag 201 generated in the coal gasification furnace 14 falls from the slag hole 101 into the slag cooling water 202 of the cooling tank 102, and the molten slag 201 dropped into the slag cooling water 202 is rapidly cooled to several. It becomes particles of glassy granulated slag (slag) 203 of about millimeters to several tens of millimeters. The slag hopper 103 moves the granulated slag 203 downward in the vertical direction, collects it in one lower position, and switches the open / close valve 104 to open / close, thereby discharging and stopping the granulated slag 203. Can be switched. The slag hopper 103 can discharge the slag cooling water 202 including the granulated slag 203 by opening the on-off valve 104.

  Further, the cooling tank 102 has a liquid level adjusting device 105. The liquid level adjusting device 105 includes a water supply pipe 106, a water supply pump 107, a level meter 108, and a liquid level control unit 109. Accordingly, in the liquid level adjusting device 105, the liquid level control unit 109 activates the water supply pump 107 when the liquid level of the slag cooling water 202 in the cooling tank 102 detected by the level meter 108 falls below a preset specified value. Thus, water is supplied to the cooling tank 102 through the water supply pipe 106.

  The slag discharge system 48 includes a slurry transport device 112, a separation tank (slurry tank) 113, and a slag storage tank 114 in addition to a slag lock hopper (slag tank) 111 located below the coal gasification furnace 14 (reaction furnace 14a). have.

  The slag lock hopper 111 is a storage unit that temporarily stores the slag cooling water 202 including the granulated slag 203, and is disposed below the slag hopper 103 in the coal gasification furnace 14. The slag lock hopper 111 can receive and temporarily store the slag cooling water 202 including the granulated slag 203 discharged from the small-diameter opening of the slag hopper 103 when the on-off valve 104 is opened. The slag lock hopper 111 is provided with an on-off valve 120 at the lower opening. The on-off valve 120 can be opened during maintenance of the slag lock hopper 111 to discharge the slag cooling water 202 including the granulated slag 203 temporarily stored downward.

  The slurry conveying device 112 conveys the slurry 204 of the slag cooling water 202 and the granulated slag 203 stored in the slag lock hopper 111 to the separation tank 113, and includes a slurry pipe (slurry conveying path) 121, a slurry A pump 122 and a slurry suction pipe 123 are provided.

  The slag lock hopper 111 is a tank that stores the slag cooling water 202 and the granulated slag 203. The slag lock hopper 111 is in a state in which the granulated slag 203 is dispersed in the slag cooling water 202 and stored as the slurry 204. The slurry pipe 121 has a base end portion disposed in the slag lock hopper 111, a slurry pump 122 disposed in the middle portion, and a slurry 204 in which the granulated slag 203 in the slag lock hopper 111 is dispersed with the slag cooling water 202. Is pumped through the slurry pipe 121. The slurry suction pipe 123 is connected to the base end portion (the most upstream portion in the slurry transport direction) of the slurry pipe 121, and the front end faces downward, that is, the bottom portion of the slag lock hopper 111.

  Therefore, the slurry conveying device 112 disperses the granulated slag 203 in the slag cooling water 202 in the slag lock hopper 111 to form the slurry 204, and operates the slurry pump 122. The slurry 204 can be sucked and the slurry 204 can be pumped from the slurry pipe 121 to the separation tank 113.

  The separation tank 113 includes a first separation tank 113a and a second separation tank 113b. The slurry pipe 121 has a tip branched into two, a first branch pipe 121a is connected to the first separation tank 113a, and a second branch pipe 121b is connected to the second separation tank 113b. A first cutoff valve 131a is attached to the first branch pipe 121a, and a second cutoff valve 131b is attached to the second branch pipe 121b. The first and second separation tanks 113a and 113b are centrifuges (for example, cyclones) having a separation function for separating the slag cooling water 202 and the granulated slag 203.

  Therefore, the first and second separation tanks 113a and 113b have first and second branch pipes 121a and 121b connected to an intermediate part in the vertical direction, and first and second drain pipes (drainage paths) 132a and 132b at the upper part. Are connected to each other, and the first and second discharge pipes 133a and 133b are connected to the lower part. The first and second drain pipes 132a and 132b are equipped with the first and second drain valves 134a and 134b, and the first and second discharge pipes 133a and 133b are fitted with the first and second discharge valves 135a and 135b. Has been. Then, the first and second drain pipes 132 a and 132 b join together in the middle to become the drain pipe 132, and the leading end is connected to the cooling tank 102. The lower ends of the first and second delivery pipes 133 a and 133 b are inserted into the slag storage tank 114.

  Accordingly, the slurry 204 of the slag cooling water 202 and the granulated slag 203 in the slag lock hopper 111 is transferred from the slurry pipe 121 to the first and second branch pipes 121a and 121b by the slurry transfer device 112. Although supplied to the separation tanks 113a and 113b, the slurry 204 can be selectively supplied to the separation tanks 113a and 113b by alternately opening and closing the first and second shut-off valves 131a and 131b. . Each of the separation tanks 113a and 113b can separate the supplied slurry 204 into the slag cooling water 202 and the granulated slag 203, and by opening the first and second drain valves 134a and 134b, The separated slag cooling water 202 can be drained from the first and second drain pipes 132a and 132b through the drain pipe 132 to the cooling tank 102 as the circulating water 206, while the first and second discharge valves 135a and 135b are opened. Thus, the separated granulated slag 203 can be discharged to the slag storage tank 114 through the first and second discharge pipes 133a and 133b.

  In the first and second separation tanks 113a and 113b, the first and second pressure reducing pipes 136a and 136b are connected to the first and second drain pipes 132a and 132b, and the first and second pressure reducing valves 137a and 137b are connected. It is installed. And the 1st, 2nd decompression piping 136a, 136b joins on the way, becomes decompression piping 136, and is connected with water storage tank 145 mentioned below. Further, the first and second separation tanks 113a and 113b are connected to the water supply pipes 138a and 138b downstream of the first and second shutoff valves 131a and 131b in the first and second branch pipes 121a and 121b, respectively. The second water supply valves 139a and 139b are mounted. And the 1st, 2nd water supply piping 138a, 138b joins on the way, becomes the water supply piping 138, and while being connected with the water storage tank 145, the water supply pump 140 is equipped.

  Therefore, the first and second separation tanks 113 a and 113 b store the high-pressure slurry 204 because the slurry 204 in the slag lock hopper 111 is pumped from the slurry pipe 121 by the slurry pump 122. Therefore, after the first and second pressure reducing valves 137a and 137b are opened to reduce the internal pressure to normal pressure, the granulated slag 203 separated by the first and second separation tanks 113a and 113b is discharged to the first and second sides. The pipes 133a and 133b are discharged to the slag storage tank 114. Here, by opening the first and second pressure reducing valves 137a and 137b, a part of the slag cooling water 202 in the first and second separation tanks 113a and 113b is removed from the first and second drain pipes 132a and 132b. The water is discharged to the water storage tank 145 through the first and second pressure reducing pipes 136a and 136b and the pressure reducing pipe 136. Further, when the slurry 204 is received again in the first and second separation tanks 113a and 113b, the air in the first and second separation tanks 113a and 113b needs to be excluded, so the first and second pressure reducing valves 137a, By operating the feed pump 140 and opening the first and second feed valves 139a and 139b with the 137b kept open, the slag cooling water 202 in the water storage tank 145 is used as the circulating water 207, the feed pipe 138, the first The first and second separation tanks 113a and 113b can be filled with water through the second water supply pipes 138a and 138b and the first and second branch pipes 121a and 121b.

  The slag storage tank 114 is a tank that stores the granulated slag 203 discharged from the separation tank 113 (first and second separation tanks 113a and 113b). In this case, since the separation tank 113 cannot completely separate the slag cooling water 202 and the granulated slag 203, the granulated slag 203 containing the slag cooling water 202 is discharged to the slag storage tank 114. The slag storage tank 114 has a main body 141 and a plurality of filters 142. The main body 141 is a hollow tower, and in this embodiment, has a square tube shape with a horizontal cross section being a quadrangle, and is provided with an end portion in which the inner diameter gradually decreases downward in the vertical direction. Each filter 142 is a member that does not allow the granulated slag 203 to pass therethrough and allows only the slag cooling water 202 to pass therethrough, is disposed along the side surface (wall surface) of the main body 141 in the vertical direction, and has a diameter of the side surface of the main body 141. Is arranged in a part where gradually decreases. Therefore, when the granulated slag 203 is supplied from the separation tank 113, the slag storage tank 114 discharges only the slag cooling water 202 from each filter 142 to make the discharged water 205, while The granulated slag 203 is stored.

  The slag storage tank 114 is provided with a water receiving portion 143 on the lower side of each filter 142 disposed on the side surface of the main body 141 and on the lower side of each filter 142 disposed on a portion where the inner diameter of the side surface of the main body 141 gradually decreases. It has been. The water receiving part 143 is connected to the water storage tank 145 through a recovery pipe 144. Each water receiving part 143 collects the discharged water 205 separated and discharged by the filter 142. The recovery pipe 144 discharges the discharged water 205 recovered by the water receiving unit 143 to the water storage tank 145.

  The slag storage tank 114 has a discharge port 146 at the lower end. The discharge port 146 discharges and stops the granulated slag 203 stored in the slag storage tank 114. The granulated slag 203 discharged from the discharge port 146 is discharged to the transport vehicle 115 waiting immediately below. The transport vehicle 115 is a vehicle that carries the granulated slag 203 discharged from the slag discharge system 48 to a predetermined place. A truck can be used as the transport vehicle 115.

  Further, the slag discharge system 48 is provided with weight sensors (load cells, etc.) 151a and 151b as slag storage amount detection units for detecting the slag storage amount in the separation tank 113 (first and second separation tanks 113a and 113b). The detection result is output to the control device 152. Based on the detection results of the weight sensors 151a and 151b, the control device 152 includes first and second shut-off valves 131a and 131b, first and second drain valves 134a and 134b, first and second discharge valves 135a and 135b, The first and second pressure reducing valves 137a and 137b and the first and second water supply valves 139a and 139b can be controlled to open and close.

  Specifically, the control device 152 closes the first and second cutoff valves 131a and 131b when the slag storage amount in the first and second separation tanks 113a and 113b reaches a predetermined slag storage amount. Then, the first and second pressure reducing valves 137a and 137b are opened, and when the pressure reduction of the first and second separation tanks 113a and 113b is completed, the first and second discharge valves 135a and 135b are opened. Further, when the slurry 204 in the first and second separation tanks 113a and 113b is discharged, the control device 152 closes the first and second discharge valves 135a and 135b, and the first and second drain valves 134a and 134b. When the air in the first and second separation tanks 113a and 113b is discharged, the first and second water supply valves 139a and 139b and the first and second pressure reducing valves 137a and 137b are closed.

  Here, the discharge process of the molten slag 201 by the slag discharge system 48 configured as described above will be described in detail.

  In the slag discharge system 48, as shown in FIG. 2, the molten slag 201 generated at the bottom of the coal gasification furnace 14 is cooled by the slag cooling water 202 in the cooling tank 102, whereby the slag hopper 103 is formed as a granulated slag 203. It is collected at. At this time, in the cooling tank 102, the liquid level is maintained within a certain range by the liquid level adjusting device 105. In the slag hopper 103, the slag cooling water 202 including the granulated slag 203 is discharged and stored in the slag lock hopper 111 by opening the lower end on-off valve 104. The granulated slag 203 stored in the slag lock hopper 111 is sent to the separation tank 113 by the slurry conveying device 112.

  That is, the granulated slag 203 stored in the slag lock hopper 111 becomes slurry 204 by the slurry cooling water 202, and is sucked from the slurry suction pipe 123 by the operation of the slurry pump 122, and is put into the separation tank 113 by the slurry pipe 121. Pumped. In this case, since the separation tank 113 includes the first and second separation tanks 113a and 113b, the first and second separation tanks 113a and 113b selectively receive the slurry 204 from the slag lock hopper 111. Accept.

  Here, the first and second shutoff valves 131a and 131b, the first and second drain valves 134a and 134b, the first and second discharge valves 135a and 135b, the first and second pressure reducing valves 137a and 137b by the control device 152. The opening / closing control of the first and second water supply valves 139a and 139b will be described in detail with reference to the time chart of FIG.

  In the opening / closing control of each valve by the control device 152, as shown in FIG. 3, first, the first shut-off valve 131a and the first drain valve 134a are opened, while the second shut-off valve 131b, the second drain valve 134b, The first and second discharge valves 135a and 135b, the first and second pressure reducing valves 137a and 137b, and the first and second water supply valves 139a and 139b are closed. In this state, the slurry 204 in the slag lock hopper 111 is supplied only from the slurry pipe 121 to the first separation tank 113a via the first branch pipe 121a by the slurry conveying device 112. The first separation tank 113a separates the supplied slurry 204 into the slag cooling water 202 and the granulated slag 203. The separated slag cooling water 202 is used as the circulating water 206 from the first drain pipe 132a to the drain pipe. The water is discharged to the cooling tank 102 through 132.

  At time t1, the controller 152 determines that the slag storage amount in the first separation tank 113a detected by the weight sensor 151a is a predetermined slag storage amount, that is, the granulated slag 203 in the first separation tank 113a is almost equal. When full, the first shut-off valve 131a and the first drain valve 134a are opened, while the second shut-off valve 131b and the second drain valve 134b are opened, thereby accepting the slurry 204 from the first separation tank 113a. Switch to 2 separation tank 113b. Moreover, the internal pressure of the 1st separation tank 113a is reduced to a normal pressure by opening the 1st pressure-reduction valve 137a. At this time, a part of the slag cooling water 202 in the first separation tank 113a is discharged from the first drainage pipe 132a to the water storage tank 145 through the first decompression pipe 136a and the decompression pipe 136.

  When the pressure reduction of the first separation tank 113a is completed at the time t2, the control device 152 opens the first discharge valve 135a, so that the separated granulated slag 203 and the slag cooling water 202 are removed from the first discharge pipe 133a. Discharge into the slag storage tank 114. In this case, the internal pressure of the first separation tank 113a may be measured by a pressure sensor (not shown), or may wait for a predetermined time set in advance. Then, at time t3, when all the slurry 204 in the first separation tank 113a is discharged, the control device 152 closes the first discharge valve 135a, while opening the first water supply valve 139a and turns the water supply pump 140 on. By operating, the slag cooling water 202 in the water storage tank 145 is supplied as circulating water 207 to the first separation tank 113a from the water supply pipe 138, the first water supply pipe 138a, and the first branch pipe 121a to fill the water, and the remaining air Is discharged from the first decompression pipe 136a.

  When the first separation tank 113a becomes full at time t4 and all the air is discharged, the control device 152 closes the first water supply valve 139a and the first pressure reducing valve 137a and enters a standby state. That is, the first separation tank 113a enters a standby state corresponding to the storage state of the slurry 204 in the second separation tank 113b.

  That is, at this time, the slurry 204 in the slag lock hopper 111 is supplied only from the slurry pipe 121 to the second separation tank 113b via the second branch pipe 121b by the slurry conveying device 112. The second separation tank 113b separates the supplied slurry 204 into the slag cooling water 202 and the granulated slag 203, and uses the separated slag cooling water 202 as the circulating water 206 from the second drain pipe 132b to the drain pipe. The water is discharged to the cooling tank 102 through 132.

  At time t5, the control device 152 determines that the slag storage amount in the second separation tank 113b detected by the weight sensor 151b is a predetermined slag storage amount, that is, the granulated slag 203 in the second separation tank 113b is almost equal. When it is full, the second shutoff valve 131b and the second drain valve 134b are closed, while the first shutoff valve 131a and the first drain valve 134a are opened, thereby accepting the slurry 204 from the second separation tank 113b. Switch to 1 separation tank 113a. Hereinafter, similarly to the above description, the control device 152 controls the opening and closing of the valves on the second separation tank 113b side so as to be in a standby state.

  Thereafter, as shown in FIG. 2, the granulated slag 203 discharged to the slag storage tank 114 is discharged from the filter 142 as slag cooling water 202 and is collected as discharged water 205 by the water receiver 143, and is stored in the water storage tank 145. Stored.

  As described above, in the slag discharge system of the first embodiment, the cooling tank 102 that cools the high-temperature granulated slag 203 with the slag cooling water 202, the granulated slag 203 discharged from the lower portion of the cooling tank 102, and the slag cooling. A slag lock hopper 111 that stores water 202, a slurry transport device 112 that transports a slurry 204 of granulated slag 203 and slag cooling water 202 stored in the slag lock hopper 111, and a slurry transported by the slurry transport device 112 204, a separation tank 113 (113a, 113b), pressure reducing valves 137a, 137b for reducing the pressure of the separation tank 113, and a slag storage tank 114 for storing the granulated slag 203 discharged from the lower part of the pressure-reduced separation tank 113. And are provided.

  Accordingly, when the high-temperature granulated slag 203 is cooled by water in the cooling tank 102, the granulated slag 203 and the slag cooling water 202 are discharged from the lower part and stored in the slag lock hopper 111 and stored in the slag lock hopper 111. The slurry 204 of the granulated slag 203 and the slag cooling water 202 is transferred and stored in the separation tanks 113a and 113b by the slurry transfer device 112, and the separation tanks 113a and 137b are opened by opening the pressure reducing valves 137a and 137b. After 113b is depressurized, the granulated slag 203 is discharged from the lower part of the separation tanks 113a and 113b to the slag storage tank 114. Therefore, the slurry 204 of the granulated slag 203 and the slag cooling water 202 is generated by the slag lock hopper 111, and the pressure difference between the slurry conveyance area and the slag discharge area is absorbed by the separation tanks 113a and 113b. It is only necessary to arrange the slag lock hopper 111 below the tank 102, and the apparatus can be simplified and the construction cost can be reduced.

  In the slag discharge system of the first embodiment, the shutoff valves 131a and 131b that can open and close the slurry pipe 121 (branch pipes 121a and 121a), and the discharge valves 135a that open and close the discharge pipes 133a and 133b of the separation tanks 113a and 113b, 135b, weight sensors 151a and 151b for detecting the amount of slag stored in the separation tanks 113a and 113b, pressure reducing valves 137a and 137b, shut-off valves 131a and 131b, and discharge valves 135a and 135b based on the detection results of the weight sensors 151a and 151b. When the slag storage amount in the separation tanks 113a and 113b reaches a predetermined slag storage amount, the control device 152 closes the shut-off valves 131a and 131b and reduces the pressure reducing valve. 137a and 137b are opened, and the separation tanks 113a and 11 b of Once decompression is complete dispensing valve 135a, is open the 135b. Therefore, the control device 152 closes the shutoff valves 131a and 131b and opens the pressure reducing valves 137a and 137b when the slag storage amount in the separation tanks 113a and 113b reaches a predetermined slag storage amount, that is, full load. By making the inside of the separation tanks 113a and 113b normal pressure and opening the discharge valves 135a and 135b, the granulated slag 203 is discharged to the slag storage tank 114, and the granulated slag 203 can be discharged safely.

  In the slag discharge system according to the first embodiment, the separation tanks 113 a and 113 b have a separation function of centrifuging the granulated slag 203 and the slag cooling water 202, and the slag cooling water 202 separated from the granulated slag 203. Drainage pipes 132a and 132b are provided. Therefore, the separation tanks 113a and 113b separate the conveyed slurry 204 into the granulated slag 203 and the slag cooling water 202, and discharge the granulated slag 203 from the lower part of the separation tanks 113a and 113b to the slag storage tank 114. The slag cooling water 202 is drained from the drain pipes 132a and 132b, and by mainly discharging only the granulated slag 203 to the slag storage tank 114, the enlargement of the slag storage tank 114 can be suppressed. .

  In the slag discharge system according to the first embodiment, the slag cooling water 202 separated from the granulated slag 203 by the separation tanks 113a and 113b is returned to the cooling tank 102 from the drain pipes 132a and 132b. Therefore, the separation tanks 113a and 113b separate the conveyed slurry 204 into the granulated slag 203 and the slag cooling water 202, and return the slag cooling water 202 to the cooling tank 102 from the drain pipes 132a and 132b. By reusing 202 as the circulating water 206, the processing cost can be reduced.

  In the slag discharge system of the first embodiment, water supply pipes 138a and 138b for supplying water to the separation tanks 113a and 113b and water supply valves 139a and 139b that can open and close the water supply pipes 138a and 138b are provided. When the slurry 204 in the separation tanks 113a and 113b is discharged, the discharge valves 135a and 135b are closed to open the water supply valves 139a and 139b, and when the air in the separation tanks 113a and 113b is discharged, the water supply valves 139a, 139b and pressure reducing valves 137a and 137b are closed. Therefore, when the slurry 204 in the separation tanks 113a and 113b is discharged, the control device 152 closes the discharge valves 135a and 135b and opens the water supply valves 139a and 139b, thereby removing the air in the separation tanks 113a and 113b. By discharging and eliminating the air in the separation tanks 113a and 113b, it is possible to prevent air from entering the cooling tank 102 and to facilitate the slurry conveyance.

  Moreover, in the slag discharge system of Example 1, the water tank 145 which stores the slag cooling water 202 separated from the slag storage tank 114 is provided, and the water supply pipes 138a and 138b separate the water in the water tank 145 into the separation tanks 113a and 113b. To supply. Therefore, by supplying the slag cooling water 202 separated from the slag storage tank 114 to the separation tanks 113a and 113b, the processing cost can be reduced by reusing the water as circulating water.

  In the slag discharge system of the first embodiment, a plurality of separation tanks 113a and 113b are provided and selectively used according to the amount of slag stored. Therefore, by selectively using the plurality of separation tanks 113a and 113b according to the amount of slag stored, it becomes possible to perform slag processing continuously and improve processing efficiency.

  FIG. 4 is a schematic configuration diagram of a slag discharge system according to Embodiment 2 of the present invention. In addition, the same code | symbol is attached | subjected to the member which has the function similar to the Example mentioned above, and detailed description is abbreviate | omitted.

  In the slag discharge system 160 of the second embodiment, as shown in FIG. 4, the coal gasification furnace 14 is provided with a slag hole 101 for dropping the molten slag 201 at the bottom, and the slag hole 101 is provided below the slag hole 101. A cooling tank 102 for storing the molten slag 201 dropped from the inside is integrally provided, and the cooling tank 102 is provided with a slag hopper 103 therein. The slag hopper 103 is provided with an on-off valve 104 with a lower small-diameter opening passing through the bottom of the cooling tank 102 downward.

  The slag discharge system 160 includes a slurry conveying device 112, a slurry tank 161, and a slag storage tank 114 in addition to the slag lock hopper 111 located below the coal gasification furnace 14.

  The slag lock hopper 111 is a storage unit that temporarily stores the slag cooling water 202 including the granulated slag 203, and is disposed below the slag hopper 103 in the coal gasification furnace 14. The slurry conveying device 112 conveys the slurry 204 of the slag cooling water 202 and the granulated slag 203 stored in the slag lock hopper 111 to the slurry tank 161, and includes a slurry pipe (slurry conveying path) 121, a slurry A pump 122 and a slurry suction pipe 123 are provided.

  The slurry tank 161 includes a first slurry tank 161a and a second slurry tank 161b. In the slurry pipe 121, the first branch pipe 121a is connected to the first slurry tank 161a, and the second branch pipe 121b is connected to the second slurry tank 161b. A first cutoff valve 131a is attached to the first branch pipe 121a, and a second cutoff valve 131b is attached to the second branch pipe 121b. The first and second slurry tanks 161a and 161b are connected to the first and second discharge pipes 133a and 133b at the lower part, and the first and second discharge pipes 133a and 133b are connected to the first and second discharge pipes 133a and 133b. Valves 135a and 135b are mounted. The lower ends of the first and second delivery pipes 133 a and 133 b are inserted into the slag storage tank 114.

  Accordingly, the slurry 204 of the slag cooling water 202 and the granulated slag 203 in the slag lock hopper 111 is transferred from the slurry pipe 121 to the first and second branch pipes 121a and 121b by the slurry transfer device 112. The slurry is supplied to the slurry tanks 161a and 161b. At this time, the slurry 204 can be selectively supplied to the slurry tanks 161a and 161b by alternately opening and closing the first and second shut-off valves 131a and 131b. . Each of the slurry tanks 161a and 161b discharges the supplied slurry 204 to the slag storage tank 114 through the first and second discharge pipes 133a and 133b by opening the first and second discharge valves 135a and 135b. can do.

  The first and second slurry tanks 161a and 161b are connected to the first and second pressure reducing pipes 136a and 136b, and are equipped with first and second pressure reducing valves 137a and 137b. The first and second decompression pipes 136a and 136b join in the middle to form the decompression pipe 136 and are connected to the water storage tank 145. Accordingly, the first and second pressure reducing valves 137a and 137b are opened to reduce the internal pressure of the first and second slurry tanks 161a and 161b to normal pressure, and then the slurry 204 is supplied to the first and second discharge pipes 133a and 133b. To the slag storage tank 114. Here, by opening the first and second pressure reducing valves 137a and 137b, a part of the slag cooling water 202 in the first and second slurry tanks 161a and 161b becomes the first and second pressure reducing pipes 136a and 136b and It is discharged to the water storage tank 145 through the decompression pipe 136.

  The slag storage tank 114 is a tank that stores the slurry 204 (granulated slag 203) discharged from the slurry tank 161 (first and second slurry tanks 161a and 161b).

  The slag discharge system 48 is provided with weight sensors (such as load cells) 151a and 151b for detecting the amount of slag stored in the slurry tank 161 (first and second slurry tanks 161a and 161b), and controls the detection results. To the device 152. The control device 152 controls the first and second shutoff valves 131a and 131b, the first and second discharge valves 135a and 135b, the first and second pressure reducing valves 137a and 137b based on the detection results of the weight sensors 151a and 151b. Open / close control is possible.

  Specifically, the control device 152 closes the first and second shutoff valves 131a and 131b when the slag storage amount in the first and second slurry tanks 161a and 161b reaches a predetermined slag storage amount. Then, the first and second pressure reducing valves 137a and 137b are opened, and when the pressure reduction of the first and second slurry tanks 161a and 161b is completed, the first and second discharge valves 135a and 135b are opened.

  Here, the discharge process of the molten slag 201 by the slag discharge system 160 configured as described above will be described in detail.

  In the slag discharge system 160, the molten slag 201 generated at the bottom of the coal gasification furnace 14 is cooled by the slag cooling water 202 in the cooling tank 102 and is recovered by the slag hopper 103 as the granulated slag 203. At this time, in the cooling tank 102, the liquid level is maintained within a certain range by the liquid level adjusting device 105. In the slag hopper 103, the slag cooling water 202 including the granulated slag 203 is discharged and stored in the slag lock hopper 111 by opening the lower end on-off valve 104. The granulated slag 203 stored in the slag lock hopper 111 is sent to the slurry tank 161 by the slurry conveying device 112.

  That is, the granulated slag 203 stored in the slag lock hopper 111 becomes slurry 204 by the slurry cooling water 202, and is sucked from the slurry suction pipe 123 by operating the slurry pump 122, and is put into the slurry tank 161 by the slurry pipe 121. Pumped. In this case, since the slurry tank 161 includes the first and second slurry tanks 161a and 161b, the first and second slurry tanks 161a and 161b selectively receive the slurry 204 from the slag lock hopper 111. Accept.

  First, the first shut-off valve 131a is opened, while the second shut-off valve 131b, the first and second discharge valves 135a and 135b, and the first and second pressure reducing valves 137a and 137b are closed. In this state, the slurry 204 in the slag lock hopper 111 is supplied only from the slurry pipe 121 to the first slurry tank 161a via the first branch pipe 121a by the slurry conveying device 112. The first slurry tank 161a stores the supplied slurry 204 up to a predetermined amount.

  Then, when the slag storage amount in the first slurry tank 161a detected by the weight sensor 151a is a predetermined slag storage amount, that is, the slurry 204 in the first slurry tank 161a is almost full, the control device 152 performs the first shutoff. While the valve 131a is opened, the second shutoff valve 131b is opened to switch the acceptance of the slurry 204 from the first slurry tank 161a to the second slurry tank 161b. Further, by opening the first pressure reducing valve 137a, the internal pressure of the first slurry tank 161a is reduced to normal pressure. At this time, a part of the slag cooling water 202 in the first slurry tank 161a is discharged from the first drain pipe 132a to the water storage tank 145 through the first decompression pipe 136a and the decompression pipe 136.

  When the pressure reduction of the first slurry tank 161a is completed, the control device 152 opens the first discharge valve 135a, and discharges the slurry 204 that has become normal pressure from the first discharge pipe 133a to the slag storage tank 114. When all the slurry 204 in the first slurry tank 161a is discharged, the control device 152 closes the first discharge valve 135a and closes the first pressure reducing valve 137a, and enters a standby state. That is, the first slurry tank 161a is in a standby state according to the storage state of the slurry 204 in the second slurry tank 161b. The control device 152 operates the water supply pump 140 to return the slag cooling water 202 in the water storage tank 145 as the circulating water 207 from the water supply pipe 138 to the cooling tank 102.

  At this time, the slurry 204 in the slag lock hopper 111 is supplied only from the slurry pipe 121 to the second slurry tank 161b via the second branch pipe 121b by the slurry conveying device 112. The second slurry tank 161b stores the supplied slurry 204 up to a predetermined amount. When the slag storage amount in the second slurry tank 161b detected by the weight sensor 151b is a predetermined slag storage amount, that is, the slurry 204 in the second slurry tank 161b is almost full, the control device 152 detects the second shutoff valve 131b. While the first shutoff valve 131a is opened, the acceptance of the slurry 204 is switched from the second slurry tank 161b to the first slurry tank 161a. Hereinafter, in the same manner as described above, the control device 152 controls the opening and closing of each valve on the second slurry tank 161b side to enter a standby state.

  Thereafter, the granulated slag 203 discharged to the slag storage tank 114 is discharged with the slag cooling water 202 from the filter 142, recovered as discharged water 205 by the water receiver 143, and stored in the water storage tank 145.

  As described above, in the slag discharge system of the second embodiment, the cooling tank 102 that cools the high-temperature granulated slag 203 with the slag cooling water 202, the granulated slag 203 discharged from the lower portion of the cooling tank 102, and the slag cooling. A slag lock hopper 111 that stores water 202, a slurry transport device 112 that transports a slurry 204 of granulated slag 203 and slag cooling water 202 stored in the slag lock hopper 111, and a slurry transported by the slurry transport device 112 204, a slurry tank 161 (161a, 161b), pressure reducing valves 137a, 137b for reducing the pressure of the slurry tank 161, and a slag storage tank 114 for storing the granulated slag 203 discharged from the lower part of the slurry tank 161 after the pressure reduction. And are provided.

  Accordingly, when the high-temperature granulated slag 203 is cooled by water in the cooling tank 102, the granulated slag 203 and the slag cooling water 202 are discharged from the lower part and stored in the slag lock hopper 111 and stored in the slag lock hopper 111. The slurry 204 of the granulated slag 203 and the slag cooling water 202 is transferred and stored in the slurry tanks 161a and 161b by the slurry transfer device 112. Here, the slurry tanks 161a and 161b are opened by opening the pressure reducing valves 137a and 137b. After 161b is depressurized, the granulated slag 203 is discharged to the slag storage tank 114 from the lower part of the slurry tanks 161a and 161b. Therefore, the slurry 204 of the granulated slag 203 and the slag cooling water 202 is generated by the slag lock hopper 111, and the pressure difference between the slurry conveying area and the slag discharge area is absorbed by the slurry tanks 161a and 161b. It is only necessary to arrange the slag lock hopper 111 below the tank 102, and the apparatus can be simplified and the construction cost can be reduced.

  In the slag discharge system of the second embodiment, a water storage tank 145 for storing the slag cooling water 202 separated from the slag storage tank 114 is provided, and the cooling tank is provided by the water supply pipe 138 using the slag cooling water 202 of the water storage tank 145 as circulating water. 102. Accordingly, by supplying the slag cooling water 202 separated from the slag storage tank 114 to the cooling tank 102, the processing cost can be reduced by reusing the water as the circulating water 207.

  In the first embodiment described above, the separation tanks 113a and 113b separate the supplied slurry 204 into the slag cooling water 202 and the granulated slag 203, and use the separated slag cooling water 202 as the circulating water 206 for the first, The second drain pipes 132 a and 132 b are configured to drain to the cooling tank 102 through the drain pipe 132, but may be supplied to the slag lock hopper 111.

  In each of the above-described embodiments, the slag discharge system of the present invention has been described as applied to a coal gasification furnace in a coal gasification combined power generation facility. However, the present invention is not limited to this field. The present invention can also be applied to a melt processing plant.

DESCRIPTION OF SYMBOLS 10 Coal gasification combined cycle power generation equipment 11 Coal supply apparatus 12 Fluidized bed drying apparatus 13 Pulverized coal machine 14 Coal gasification furnace 15 Char recovery apparatus 16 Gas refinement apparatus 17 Gas turbine equipment 18 Steam turbine equipment 19 Generator 20 Exhaust heat recovery boiler 48 , 160 Slag discharge system 102 Cooling tank 103 Slag hopper 111 Slag lock hopper (slag tank)
112 Slurry transfer device 113, 113a, 113b Separation tank (slurry tank)
114 Slag storage tank 131a, 131b Shut-off valve 133a, 133b Discharge piping 134a, 134b Drain valve 135a, 135b Discharge valve 136, 136a, 136b Pressure reduction piping 137a, 137b Pressure reduction valve 138, 138a, 138b Water supply piping 139a, 139b Water supply valve Weight supply valve Sensor (slag storage amount detection unit)
152 Control Device 201 Molten Slag 202 Slag Cooling Water 203 Granulated Slag 204 Slurry 205 Drained Water 206, 207 Circulating Water 161, 161a, 161b Slurry Tank

Claims (7)

A cooling tank that cools the hot slag with water;
Slag discharged from the lower part of the cooling tank and slag tank for storing water;
A slurry transport path for transporting slurry of slag and water stored in the slag tank;
A slurry tank for storing the high-pressure slurry conveyed by the slurry conveyance path;
A pressure reducing valve for reducing the internal pressure of the slurry tank to normal pressure ;
A slag storage tank for storing slag discharged from the lower part of the slurry tank after decompression;
A slag discharge system comprising:   A shutoff valve capable of opening and closing the slurry conveyance path, a discharge valve for opening and closing a discharge portion of the slurry tank, a slag storage amount detection unit for detecting a slag storage amount in the slurry tank, and a slag storage amount detection unit A control device capable of opening and closing the pressure reducing valve, the shut-off valve, and the discharge valve based on a detection result is provided, and the control device sets the slag storage amount in the slurry tank to a predetermined slag storage amount set in advance. The slag discharge system according to claim 1, wherein the shutoff valve is closed and the pressure reducing valve is opened, and the discharge valve is opened when the pressure reduction of the slurry tank is completed.   The slag discharge system according to claim 1 or 2, wherein the slurry tank has a separation function of separating slag and water, and is provided with a drainage path for discharging water separated from the slag.   The slag discharge system according to claim 3, wherein the water separated from the slag in the slurry tank is returned to the cooling tank or the slag tank through the drainage path. A water supply path for supplying water to the slurry tank and a water supply valve capable of opening and closing the water supply path are provided, and the controller closes the discharge valve when the slurry in the slurry tank is discharged, and supplies the water supply The slag discharge system according to claim 2 , wherein when the valve is opened and the air in the slurry tank is discharged, the water supply valve and the pressure reducing valve are closed. Reservoir is provided for storing the water separated from the slag storage tank, the water supply path, according to claim 5, characterized in that the supply water of the water tank to the slurry tank or the cooling tank Slag discharge system.   The slag discharge system according to any one of claims 1 to 6, wherein a plurality of the slurry tanks are provided and selectively used according to a slag storage amount.

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