CN111154516A - Cooling and deslagging system for coal ash - Google Patents
Cooling and deslagging system for coal ash Download PDFInfo
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- CN111154516A CN111154516A CN201910138543.2A CN201910138543A CN111154516A CN 111154516 A CN111154516 A CN 111154516A CN 201910138543 A CN201910138543 A CN 201910138543A CN 111154516 A CN111154516 A CN 111154516A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/54—Gasification of granular or pulverulent fuels by the Winkler technique, i.e. by fluidisation
- C10J3/56—Apparatus; Plants
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/80—Other features with arrangements for preheating the blast or the water vapour
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1625—Integration of gasification processes with another plant or parts within the plant with solids treatment
- C10J2300/1628—Ash post-treatment
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1687—Integration of gasification processes with another plant or parts within the plant with steam generation
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
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- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
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- Gasification And Melting Of Waste (AREA)
Abstract
The invention discloses a coal ash cooling and deslagging system which comprises a cold slag tank, a slag collecting tank and a slag discharging tank, wherein an outlet of a slag pipe extends to the inner bottom of the cold slag tank, an ash temperature sensor is arranged inside the top end of the ash pipe, a cooling water pipe is communicated with a water inlet pipe of the cold slag tank, a water inlet control valve is arranged on the water inlet pipe, an inflation pipe is communicated with the upper part of the ash pipe inside the cold slag tank, the cooling air pipe is communicated with the inflation pipe, an inflation control valve is arranged on the inflation pipe, and a cold slag tank pressure sensor and a cold slag tank temperature sensor are arranged at the top of the cold slag tank. The invention has the advantages that carbon dioxide is introduced into the ash residue pipe instead of steam to control the slag discharge speed, the ash residue is cooled for one time, the use amount of the steam is reduced, the investment cost of steam manufacturing equipment and raw material coal is reduced, and the carbon dioxide can inhibit the carbon in the fluidized bed gasification furnace from reacting with oxygen to generate the carbon dioxide after entering the fluidized bed gasification furnace, thereby promoting the reaction of the carbon and the water vapor.
Description
The technical field is as follows:
the invention relates to a slag discharging device, in particular to a cooling slag discharging system for coal ash.
Background art:
the coal powder and the gasifying agent are gasified in the fluidized bed gasifier to generate crude gas, and high-temperature ash is generated after the coal powder is gasified. In order to discharge ash in the fluidized bed gasification furnace, a chilling chamber and a slag discharge tank are generally communicated with a slag discharge port of the fluidized bed gasification furnace in sequence, and the slag discharge process comprises the following steps: ash in the fluidized bed gasifier enters a slag discharging channel through a slag discharging port, steam is introduced into the slag discharging channel to control the slag discharging speed, cooling water is introduced into the slag discharging channel to cool the ash in the descending process, the ash and the cooling water fall into a chilling chamber from the slag discharging channel, and the cooled ash in the chilling chamber is discharged through a slag discharging tank; in the process, the slag discharge speed is generally controlled by adding hot steam into the slag discharge channel, the ash slag is cooled by introducing cooling water into the slag discharge channel, 90% of heat in the ash slag is transferred to the cooling water in a sensible heat mode, the cooling water is forcibly circulated by a circulating pump, and the heat is removed by a heat exchanger.
The slag discharge device has the following problems in the use process: 1. ash slag needs to be cooled in the chilling chamber for a period of time, the chilling chamber continuously feeds the slag, when the liquid level of cooling water in the chilling chamber exceeds a water outlet, a circulating pump needs to be used for forced circulation, the cooling water contains part of the ash slag, the circulating pump and a heat exchanger are blocked in the circulating cooling process, the operation of a slag discharging device is interrupted, and the slag discharging efficiency is influenced; 2. ash in the slag discharging tank falls into the slag storage device through self weight, the slag storage device can only be placed below the slag discharging tank, the placement position of equipment is limited, the overall height of the slag discharging equipment is high, and the maintenance is inconvenient; 3. the steam is introduced into the deslagging channel to control the deslagging speed, so that the use amount of the steam is increased, the steam needs to be produced by a steam boiler, and the investment cost of equipment and raw material coal is increased; 4. the slag discharging channel is internally provided with cooling water to cool the slag, the slag can not be completely immersed in the cooling water, and the cooling effect is poor.
The invention content is as follows:
the invention aims to provide a coal ash cooling and deslagging system which can reduce the amount of steam supplied from the outside of a fluidized bed gasification furnace, inhibit the generation of carbon dioxide in gasification reaction by adding normal-temperature carbon dioxide gas into an ash tube and improve the gasification efficiency of raw coal.
The invention is implemented by the following technical scheme: a cooling and deslagging system for coal ash and slag comprises a cold slag tank, a slag collecting tank and a slag discharging tank, wherein an outlet of a slag pipe extends to the inner bottom of the cold slag tank, a slag temperature sensor is arranged inside the top end of the slag pipe, a cooling water pipe is communicated with a water inlet pipe of the cold slag tank, a water inlet control valve is arranged on the water inlet pipe, an inflation pipe is communicated with the upper part of the slag pipe inside the cold slag tank, a cooling air pipe is communicated with the inflation pipe, an inflation control valve is arranged on the inflation pipe, and a cold slag tank pressure sensor and a cold slag tank temperature sensor are arranged at the top of the cold slag tank;
a slag discharge port at the bottom of the cold slag tank is communicated with a slag inlet at the top of the slag collecting tank, and the top of the slag collecting tank is provided with a water balance valve; receive the row's cinder notch of sediment jar bottom through first sediment valve with arrange the slag inlet intercommunication at sediment tank deck the relief valve and arrange sediment jar pressure sensor have been installed at the top of sediment jar arrange the lateral part of sediment jar and have installed sediment level sensor arrange the second sediment valve of arranging the bottom of sediment jar, the second is arranged sediment valve and is arranged sediment house steward intercommunication the second is arranged sediment valve top arrange sediment jar facial make-up and be equipped with the water injection valve.
Furthermore, a communicating pipe is connected between the cooling water pipe and the water injection valve, and a control valve is arranged on the communicating pipe.
Furthermore, the communicating pipe at the outlet end of the control valve is communicated with the slag discharge main pipe through a slag flushing valve, and the outlet end of the pressure release valve is communicated with the inlet of the slag discharge main pipe.
Furthermore, the outlet end of the water balance valve is communicated with the communicating pipe at the outlet end of the control valve, and the communicating pipe at the inlet end of the control valve is communicated with the inlet end of the water balance valve through a slag collecting tank flushing valve.
Furthermore, ash temperature sensor cold sediment jar pressure sensor arrange sediment jar pressure sensor, arrange sediment level sensor and all be connected with the input electricity of controller, the output of controller respectively with advance the water control valve fill the control valve, the relief valve electricity is connected.
Further, the cold slag tank comprises a tank body, the ash pipe is vertically arranged in the middle of the tank body, the top end of the ash pipe extends to the outside of the top end of the tank body, and a channel is formed between the bottom end of the ash pipe and the bottom end of the tank body; a high liquid level sensor is arranged in the tank body below the inflation tube; a plurality of balance holes are formed in the ash pipe below the high liquid level sensor along the circumferential direction, a low liquid level sensor is arranged in the tank body below the balance holes, and the high liquid level sensor and the low liquid level sensor are electrically connected with the water inlet control valve and the water balance valve; the side part of the tank body is communicated with the water inlet pipe, the outer part of the ash residue pipe is sleeved with an annular water distribution pipe communicated with the water inlet pipe, and the pipe wall of the annular water distribution pipe is provided with a plurality of water distribution holes.
Furthermore, the ash pipe comprises a straight pipe heat exchange section, an expanding pipe vaporization section and a straight pipe deslagging section which are sequentially communicated from top to bottom, the inflation pipe is arranged on the straight pipe heat exchange section, and the balance hole is formed in the upper portion of the expanding pipe vaporization section.
Further, an air distribution pipe is embedded and mounted on the ash pipe above the high liquid level sensor, and the inflation pipe is communicated with the ash pipe through the air distribution pipe; the gas distribution pipe comprises an annular sintered metal filter element and a split sleeve, wherein the sintered metal filter element is arranged on the outer pipe body, the pipe body is embedded in the ash pipe, the top end and the bottom end of the pipe body are respectively connected with the ash pipe through flanges, and the gas filling pipe is communicated with the inside of the pipe body.
Furthermore, a fire-resistant layer is arranged on the inner wall of the ash slag pipe outside the tank body.
Furthermore, a grate plate is fixed between the outer wall of the lower part of the ash pipe and the inner wall of the tank body, and a manhole is arranged on the side wall of the tank body.
Further, the gas filling pipe is a carbon dioxide gas filling pipe.
The invention has the advantages that: 1. the cooling water at the liquid level in the ash pipe is continuously evaporated into steam, the steam carries out secondary cooling on the ash, and the steam enters the fluidized bed gasification furnace through the ash pipe for utilization, so that the external steam supply amount is reduced by 5%, and the input cost of the steam is reduced; the low-temperature cooling water is supplemented after the cooling water is evaporated, and forced circulation cooling of the cooling water is not needed, so that the blockage of a circulating pump and a heat exchanger in the circulation cooling process is avoided, the smooth operation of a slag discharging device is ensured, and the slag discharging efficiency is ensured; 2. ash in the slag discharging main pipe is conveyed by high-pressure water and can be conveyed into the slag storage device at the tail end of the slag discharging main pipe along the slag discharging main pipe, so that the placement position of the slag storage device is not limited, the overall height of slag discharging equipment is reduced, and the maintenance is convenient; 3. carbon dioxide is introduced into the ash residue pipe to replace steam to control the deslagging speed, the ash residue is cooled for the first time, the using amount of the steam is reduced, the input cost of steam manufacturing equipment and raw material coal is reduced, and the carbon dioxide enters the fluidized bed gasification furnace, so that the concentration of the carbon dioxide in the fluidized bed gasification furnace is increased, the carbon in the fluidized bed gasification furnace can be inhibited from reacting with oxygen to generate the carbon dioxide, the reaction of the carbon and water vapor is promoted, and the effective gas component content of the crude gas is improved; 4. after entering the tank body, the ash falls into and is immersed in cooling water, and the cooling water can fully cool the ash, so that the cooling effect is ensured; 5. a plurality of balance holes are formed in the middle of the ash residue pipe in the circumferential direction, so that the pressure of the upper part of the tank body and the pressure in the ash residue pipe can be balanced, the cooling water is prevented from being pressed into the fluidized bed gasification furnace when the pressure of the upper part of the tank body is greater than the pressure in the ash residue pipe, and the safety production is ensured; 6. the ash pipe comprises a straight pipe heat exchange section, an expanding pipe vaporization section and a straight pipe deslagging section which are sequentially communicated from top to bottom, wherein the diameters of the expanding pipe vaporization section and the straight pipe deslagging section are larger than that of the straight pipe heat exchange section, so that the diffusion of high-temperature ash in cooling water can be limited, the diffusion of fly ash which is not easy to dissolve in water in the ash can be limited, and the fly ash is forced to be wet; and the steam generated by the heat absorption of the cooling water is fully collected and enters the fluidized bed gasification furnace through the ash pipe to be used as a gasification agent, so that the investment cost of the gasification agent is reduced.
Description of the drawings:
FIG. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a schematic structural diagram of a cold slag tank;
fig. 3 is a schematic structural view of the gas distribution pipe.
The slag cooling system comprises a cold slag tank 1, a slag collecting tank 2, a slag discharging tank 3, a slag pipe 4, a slag temperature sensor 5, a cooling water pipe 6, a water inlet pipe 7, a water inlet control valve 8, a cooling air pipe 9, an inflation pipe 10, an inflation control valve 11, a cold slag tank pressure sensor 12, a water balance valve 13, a first slag discharging valve 14, a pressure release valve 15, a slag discharging tank pressure sensor 16, a slag discharging liquid level sensor 17, a water injection valve 18, a second slag discharging valve 19, a slag discharging main pipe 20, a communicating pipe 21, a control valve 22, a slag flushing valve 23, a slag collecting tank flushing valve 24, a controller 25, a tank body 26, a gas distribution pipe 27, a high liquid level sensor 28, a balance hole 29, a low liquid level sensor 30, a manhole 31, an annular water distribution pipe 32, a water distribution hole 33, a straight pipe heat exchange section 34, an expanding pipe section 35, a straight pipe slag discharging section 36, a sintered metal filter element 37, a pipe body 38.
The specific implementation mode is as follows:
example 1:
as shown in fig. 1-3, a cooling and deslagging system for coal ash includes a cold slag tank 1, a slag collecting tank 2 and a deslagging tank 3,
the cold slag tank 1 comprises a tank body 26, a slag pipe 4 is vertically arranged in the middle of the tank body 26, the top end of the slag pipe 4 extends to the outside of the top end of the tank body 26, an outlet of the slag pipe 4 extends to the inner bottom of the cold slag tank 1, a channel is formed between the bottom end of the slag pipe 4 and the bottom end of the tank body 26, and slag falls into the tank body 26 through the slag pipe 4 to be cooled.
The ash pipe 4 comprises a straight pipe heat exchange section 34, an expanding pipe vaporization section 35 and a straight pipe deslagging section 36 which are sequentially communicated from top to bottom, the diameters of the expanding pipe vaporization section 35 and the straight pipe deslagging section 36 are larger than the diameter of the straight pipe heat exchange section 34, the diffusion of high-temperature ash in cooling water can be limited, the diffusion of fly ash which is not easy to dissolve in water in the ash can be limited, and the fly ash is forced to be wet.
The upper part of an ash residue pipe 4 in the cold residue tank 1 is communicated with an inflation pipe 10, the inflation pipe 10 is arranged on a straight pipe heat exchange section 34, a cooling air pipe 9 is communicated with the inflation pipe 10, and when ash residues flow through the straight pipe heat exchange section 34, the inflation pipe 10 introduces cooling air into the ash residue pipe 4 to carry out primary cooling on the ash residues. The lime-ash after once cooling continues down along lime-ash pipe 4, when the cooling water contact in with lime-ash pipe 4, the cooling water heat absorption evaporation produces a large amount of steam, steam carries out the secondary cooling to the lime-ash in lime-ash pipe 4, steam after carrying out the secondary cooling to the lime-ash gets into the fluidized bed gasifier through lime-ash pipe 4 and utilizes, 5% external steam supply volume has been reduced, the input cost of gasifying agent has been reduced, there is microthermal cooling water to mend after the cooling water evaporation, need not carry out the forced circulation cooling to the cooling water, avoided causing the jam of circulating pump and heat exchanger in the circulative cooling process, guaranteed going on smoothly of sediment device work, guaranteed row's sediment efficiency.
The gas distribution pipe 27 is embedded in the ash pipe 4, the inflation pipe 10 is communicated with the ash pipe 4 through the gas distribution pipe 27, the gas distribution pipe 27 comprises an annular sintered metal filter element 37 and a pipe body 38 which is sleeved outside the sintered metal filter element 37 in a split mode, the sintered metal filter element 37 can prevent ash from entering the pipe body 38 to avoid blocking the inflation pipe 10, the pipe body 38 is embedded in the ash pipe 4, the top end and the bottom end of the pipe body 38 are connected with the ash pipe 4 through flanges respectively, and the inflation pipe 10 is communicated with the inside of the pipe body 38. An inflation control valve 11 is arranged on the inflation pipe 10, an ash temperature sensor 5 is arranged in the top end of the ash pipe 4, the ash temperature sensor 5 detects the temperature of ash discharged by the fluidized bed gasification furnace, and when the temperature is higher than the preset value of the controller 25, an opening degree increasing signal is sent to the inflation control valve 11 to increase the entering amount of cooling gas. The gas-filled pipe 10 is a carbon dioxide gas-filled pipe, carbon dioxide gas is used for replacing steam as cooling gas, the using amount of steam is reduced, the input cost of steam manufacturing equipment and raw material coal is reduced, and after the carbon dioxide enters the fluidized bed gasification furnace, the concentration of the carbon dioxide in the fluidized bed gasification furnace is increased, the carbon in the fluidized bed gasification furnace can be inhibited from reacting with oxygen to generate carbon dioxide, the reaction of the carbon and water vapor is promoted, and the effective gas component content of the raw gas is improved.
The side part of the tank body 26 is communicated with a water inlet pipe 7, a cooling water pipe 6 is communicated with the water inlet pipe 7, cooling water is introduced into the cold slag tank 1, and the ash slag after secondary cooling falls into the tank body 26 and is immersed in the cooling water for tertiary cooling. The water inlet pipe 7 is provided with a water inlet control valve 8, the top of the cold slag tank 1 is provided with a cold slag tank temperature sensor 41, the cold slag tank temperature sensor 41 is used for detecting the temperature of cooling water and ash in the cold slag tank 1, and when the temperature is higher than the preset value of the controller 25, an opening degree increasing signal is sent to the water inlet control valve 8 to increase the entering amount of the cooling water.
The annular water distribution pipe 32 communicated with the water inlet pipe 7 is sleeved outside the ash pipe 4, and a plurality of water distribution holes 33 are formed in the pipe wall of the annular water distribution pipe 32, so that cooling water can be uniformly added into the tank 26, the liquid level and the ambient temperature of each part of the tank 26 are uniform, and the regulation and control of the temperature and the pressure of a cooling system are facilitated. The water distribution holes 33 are arranged in all directions of the annular water distribution pipe 32, and when cooling water is sprayed on the side wall of the tank 26, the side wall of the tank 26 can be cooled.
A high liquid level sensor 28 is arranged inside the tank body 26 below the air distribution pipe 27 and the gas charging pipe 10, the high liquid level sensor 28 is arranged below the gas charging pipe 10, the liquid level inside the ash slag pipe 4 is prevented from exceeding the gas charging pipe 10, and the cooling air is ensured to normally enter the ash slag pipe 4; a plurality of balance holes 29 are arranged on the ash pipe 4 below the high liquid level sensor 28 along the circumferential direction, and the balance holes 29 are arranged at the upper part of the vaporizing section 35 of the expanding tube. The pressure at the upper part of the tank body 26 and the pressure in the ash pipe 4 are balanced, so that the cooling water is prevented from being pressed into the fluidized bed gasification furnace through the ash pipe 4 when the pressure at the upper part of the tank body 26 is greater than the pressure in the ash pipe 4, and the safety production is ensured; a low liquid level sensor 30 is arranged in the tank body 26 below the balance hole 29, the high liquid level sensor 28 and the low liquid level sensor 30 are both electrically connected with the water inlet control valve 8 and the water balance valve 13 on the slag collecting tank 2, the high liquid level sensor 28 is used for detecting whether the liquid level in the tank body 26 reaches the upper limit value of the liquid level, and the low liquid level sensor 30 is used for detecting whether the liquid level in the tank body 26 reaches the lower limit value of the liquid level; when the low liquid level sensor 30 detects that the liquid level of the cooling water in the cold slag tank 1 reaches a preset liquid level lower limit value, the opening degree of the water inlet control valve 8 is increased, the opening degree of the water balance valve 13 is decreased, and water is supplemented to the tank body 26; when the high liquid level sensor 28 detects that the liquid level of the cooling water reaches the preset upper limit value of the liquid level, the opening degree of the water inlet control valve 8 is reduced, and the opening degree of the water balance valve 13 is increased, so that the liquid level of the cooling water in the tank body 26 is always kept between the lowest liquid level and the highest liquid level, the coal cinder can be immersed in the cooling water, and a good cooling effect is ensured. The high level sensor 28 and the low level sensor 30 in this embodiment function to detect the level of the liquid, and are conventional functions of level sensors, and are of the type MC1151/3351 DP.
A grate plate 40 is fixed between the outer wall of the lower part of the ash pipe 4 and the inner wall of the tank body 26, so that ash in cooling water can be prevented from floating upwards to block the balance hole 29 on the ash pipe 4, and the pressure balance between the upper part of the tank body 26 and the inner part of the ash pipe 4 is ensured. The manhole 31 is arranged on the side wall of the tank body 26, so that the inside of the tank body 26 can be conveniently overhauled. The top of the cold slag tank 1 is provided with a cold slag tank pressure sensor 12, and the cold slag tank pressure sensor 12 is used for detecting the air pressure inside the cold slag tank 1.
A slag discharge port at the bottom of the cold slag tank 1 is communicated with a slag inlet at the top of the slag collecting tank 2, a water balance valve 13 is arranged at the top of the slag collecting tank 2, cooling water and ash slag in the cold slag tank 1 enter the slag collecting tank 2, the ash slag is deposited to the bottom in the slag collecting tank 2, and the water balance valve 13 is opened to discharge redundant water at the upper part of the slag collecting tank 2; the water discharged by the water balance valve 13 is divided into two paths, one path is used as a water replenishing source of the slag discharging tank 3, and the other path is used as a slag discharging source of the slag discharging main pipe 20 for utilization.
A slag discharge port at the bottom of the slag collection tank 2 is communicated with a slag inlet at the top of the slag discharge tank 3 through a first slag discharge valve 14, the top of the slag discharge tank 3 is provided with a pressure release valve 15 and a slag discharge tank pressure sensor 16, the side part of the slag discharge tank 3 is provided with a slag discharge liquid level sensor 17, the bottom of the slag discharge tank 3 is provided with a second slag discharge valve 19, the second slag discharge valve 19 is communicated with a slag discharge main pipe 20, and the slag discharge tank 3 above the second slag discharge valve 19 is provided with a water injection valve 18; supplying water into the slag discharging tank 3 through a water injection valve 18 to balance the pressure in the slag discharging tank 3 and the slag collecting tank 2, detecting the air pressure in the slag discharging tank 3 through a slag discharging tank pressure sensor 16, when the slag discharging tank 3 is filled with water, if the detection value of the slag discharging tank pressure sensor 16 is larger than the detection value of a cold slag tank pressure sensor 12, a controller 25 controls a pressure release valve 15 to be opened, releasing the pressure of the slag discharging tank 3 until the detection value of the slag discharging tank pressure sensor 16 is equal to the cold slag tank pressure sensor 12, and closing the pressure release valve 15, at the moment, a high-pressure gas phase space is formed at the top of the slag discharging tank 3, a slag discharging liquid level sensor 17 is used for detecting the liquid level in the slag discharging tank 3 during water injection, and when the detection value of the slag discharging liquid level sensor 17 reaches the preset value; after the water injection is finished, the first slag discharging valve 14 is opened periodically, and the ash slag at the bottom in the slag collecting tank 2 falls into the slag discharging tank 3; when the slag discharging tank 3 discharges slag, the pressure release valve 15 is opened firstly to release the pressure of the slag discharging tank 3, so that the pipeline is prevented from being impacted too much due to overhigh pressure, the safe slag discharging is ensured, the pressure in the slag discharging pipe 3 can be detected by the slag discharging tank pressure sensor 16, when the pressure in the slag discharging pipe 3 is released to the normal pressure of the system, the pressure release valve 15 is closed, the second slag discharging valve 19 and the slag flushing valve 23 are opened, and the ash slag in the slag discharging tank 3 enters the slag discharging main pipe 20 through the second slag discharging valve 19; when the slag discharging of the slag discharging tank 3 is not smooth, the water injection valve 18 is opened, and water is injected into the slag discharging tank 3 for blockage removal until the slag discharging is finished.
A communicating pipe 21 is connected between the cooling water pipe 6 and the water injection valve 18, a control valve 22 is arranged on the communicating pipe 21, the control valve 22 and the water injection valve 18 are opened, part of cooling water sent by the cooling water pipe 6 is used as a water replenishing source of the slag discharging tank 3, the communicating pipe 21 at the outlet end of the control valve 22 is communicated with a slag discharging main pipe 20 through the slag flushing valve 23, the slag flushing valve 23 is opened, part of cooling water sent by the cooling water pipe 6 flushes ash through a pipeline or uses the cooling water as slag discharging water of the slag discharging main pipe 20, the outlet end of the pressure relief valve 15 is communicated with an inlet of the slag discharging main pipe 20, gas discharged from the slag discharging tank 3 is discharged into the slag discharging main pipe 20 to disturb the ash, and good fluidity of the ash in the slag.
The outlet end of the water balance valve 13 is communicated with a communicating pipe 21 at the outlet end of a control valve 22, the water balance valve 13 and a slag flushing valve 23 are opened, and cooling water after heat exchange discharged by the slag collecting tank 2 can be used as slag discharging water of the slag discharging main pipe 20; opening water balance valve 13 and water injection valve 18, can using the cooling water after receiving the discharged heat transfer of sediment jar 2 as the moisturizing water source of row sediment jar 3, communicating pipe 21 of control valve 22 entrance point communicates with the entrance point of water balance valve 13 through receiving sediment jar flushometer 24, opens and receives sediment jar flushometer 24, can use the partial cooling water that condenser tube 6 sent to wash the inlet pipeline of water balance valve 13.
The ash temperature sensor 5, the cold slag tank temperature sensor 41, the cold slag tank pressure sensor 12, the slag discharging tank pressure sensor 16 and the slag discharging liquid level sensor 17 are all electrically connected with the input end of the controller 25, and the output end of the controller 25 is respectively electrically connected with the water inlet control valve 8, the air charging control valve 11 and the pressure release valve 15. The functions of the cold slag pot temperature sensor 41 and the ash slag temperature sensor 5 in the embodiment are temperature detection, and are the conventional functions of the temperature sensors, and the models of the temperature sensors are MCT 80Y; the cold slag tank pressure sensor 12 and the slag discharge tank pressure sensor 16 in the present embodiment have the functions of detecting the internal pressure of the tank, and are conventional functions of pressure sensors, and the models thereof are MC1151/3351 GP; the function of the slag discharge liquid level sensor 17 in the present embodiment is to detect the liquid level height, which is the conventional function of a liquid level sensor, and the model number thereof is MC1151/3351 DP; the controller 25 in this embodiment functions to control the corresponding valve according to the received detection value, and is a type S7-400 siemens PLC controller. The ash residue temperature sensor 5, the cold slag tank temperature sensor 41, the cold slag tank pressure sensor 12, the slag discharging tank pressure sensor 16 and the slag discharging liquid level sensor 17 transmit detection values to the controller 25, and the controller 25 correspondingly adjusts the water inlet control valve 8, the inflation control valve 11 and the pressure release valve 15, so that the temperature and the pressure of the slag discharging system are controlled, the labor intensity is reduced, and the working efficiency is improved.
The working process is as follows:
the ash in the fluidized bed gasification furnace enters the tank body 26 of the cold slag tank 1 through the ash pipe 4, the ash is cooled for the first time in the straight pipe heat exchange section 34 of the ash pipe 4 through carbon dioxide cooling gas discharged from the sintered metal filter element 37, and the cooling gas cools the ash for the first time and then moves upwards along the ash pipe 4 to enter the fluidized bed gasification furnace. The ash residue after primary cooling continues to move downwards along the ash residue pipe 4, after the ash residue is contacted with cooling water, the cooling water is evaporated to generate a large amount of steam, the expansion pipe vaporization section 35 and the straight pipe residue discharging section 36 limit the high-temperature ash residue from diffusing in the cooling water, the steam generated by the heat absorption of the cooling water is fully collected, the steam moves upwards along the ash residue pipe 4 to carry out secondary cooling on the ash residue, and the steam carries out secondary cooling on the ash residue and then moves upwards along the ash residue pipe 4 to enter the fluidized bed gasification furnace. After the ash falls into the cooling water, the cooling water cools the ash for three times. The cooling water is sprayed out through the water distribution holes 33 on the annular water distribution pipe 32 to supplement the cooling water in the tank 26, and meanwhile, part of the cooling water is sprayed onto the inner wall of the tank 26 and slides down along the inner wall to cool the inner wall of the tank 26.
The upper space of the tank body 26 is communicated with the ash pipe 4 through the balance hole 29, thereby ensuring the pressure balance between the tank body 1 and the ash pipe 2, and the grate plate 40 between the lower outer wall of the ash pipe 4 and the inner wall of the tank body 26 can prevent the ash in the cooling water from floating upwards to block the balance hole 29.
The ash slag after being cooled for three times directly enters the slag collecting tank 2 through the slag discharging port, after the ash slag in the slag discharging tank 3 is discharged, the second slag discharging valve 19 is closed, the water injection valve 18 is opened to start water injection, when the detection value of the slag discharging liquid level sensor 17 reaches the preset value of the controller 25, the water injection valve 18 is closed, when the detection value of the slag discharging tank pressure sensor 16 is greater than the detection value of the cold slag tank pressure sensor 12, the controller 25 sends an opening signal to the pressure release valve 15 to release the pressure of the slag discharging tank 3, and when the detection value of the slag discharging tank pressure sensor 16 is equal to the cold slag tank pressure sensor 12, the pressure release valve 15 is closed;
after the liquid level and the pressure in the slag discharging tank 3 are adjusted according to the steps, the first slag discharging valve 14 is opened, high-pressure gas at the top of the slag discharging tank 3 moves upwards to enter the slag collecting tank 2, and ash residues at the lower part of the slag collecting tank 2 are disturbed and move downwards to enter the slag discharging tank 3; after the feeding of the slag discharging tank 3 is finished, the first slag discharging valve 14 is closed, the pressure release valve 15 is opened, after the slag discharging tank 3 is discharged to normal pressure, the second slag discharging valve 19 and the slag flushing valve 23 are opened, ash slag is smoothly taken away by high-pressure injection water and flows to the slag storage device along the slag discharging main pipe 20, the ash slag in the slag discharging main pipe 20 is conveyed by the high-pressure injection water and can be conveyed into the slag storage device at the tail end of the slag discharging main pipe 20 along the slag discharging main pipe 20, and the placing position of the slag storage device is not limited; in the slag feeding and discharging process of the slag discharging tank 3, the water balance valve 13 is always in an open state, water injected into the slag discharging tank 3 and conveying water of the slag discharging main pipe 20 are water discharged from the slag collecting tank 2 through the water balance valve 13, water discharged from the slag collecting tank 2 is fully utilized, and the using amount of purified water resources is reduced.
The water injected into the slag discharging tank 3 and the conveying water of the slag discharging main pipe 20 are provided by the slag collecting tank 2 through the water discharged by the water balance valve 13, the water discharged by the water balance valve 13 contains certain ash, the slag collecting tank flushing valve 24 and the control valve 22 need to be opened at regular time to flush the pipeline through which the slag water flows, the pipeline through which the slag water flows is prevented from being blocked, and the flushing period is determined according to the actual working condition of the system operation.
When the low liquid level sensor 30 detects that the liquid level of the cooling water in the cold slag tank 1 reaches a preset liquid level lower limit value, the opening degree of the water inlet control valve 8 is increased, the opening degree of the water balance valve 13 is decreased, and water is supplemented to the tank body 26; when the high liquid level sensor 28 detects that the liquid level of the cooling water reaches the preset upper limit value of the liquid level, the opening degree of the water inlet control valve 8 is reduced, and the opening degree of the water balance valve 13 is increased, so that the liquid level of the cooling water in the tank body 26 is always kept between the lowest liquid level and the highest liquid level, the coal cinder can be immersed in the cooling water, and a good cooling effect is ensured.
When the controller 25 receives that the detection value of the cold slag tank temperature sensor 41 exceeds the preset value, the controller 25 sends an opening degree increasing signal to the water inlet control valve 8 to increase the entering amount of cooling water; when the controller 25 receives that the detection value of the ash temperature sensor 5 exceeds the preset value, the controller 25 sends an opening degree increase signal to the air inflation control valve 11 to increase the entering amount of the cooling air.
Example 2:
a cooling slag-discharging method for cooling the coal ash using the cooling slag-discharging system for the coal ash in embodiment 1, comprising the steps of: (1) cooling gas primary cooling, (2) steam secondary cooling, (3) cooling water tertiary cooling, and (4) slag feeding and discharging of a slag discharging tank; wherein the content of the first and second substances,
(1) primary cooling of cooling gas: ash residue at 850-900 ℃ discharged from the fluidized bed gasification furnace enters the ash residue pipe 4, carbon dioxide of cooling gas enters the pipe body 38 of the gas distribution pipe 27 through the gas filling pipe 10 and is uniformly sprayed out through the sintered metal filter element 37, the ash residue in the ash residue pipe 4 is cooled for one time, the ash residue cooled to 450-550 ℃ moves downwards along the ash residue pipe 4, and the carbon dioxide after heat exchange with the ash residue moves upwards along the ash residue pipe 4 and enters the fluidized bed gasification furnace; carbon dioxide is used for replacing steam to control the slag discharge speed, so that on one hand, the use amount of the steam is reduced, the input cost of steam manufacturing equipment and raw material coal is reduced, on the other hand, the carbon dioxide and residual carbon in high-temperature ash slag generate endothermic reduction reaction to further cool the ash slag, on the other hand, the carbon dioxide can inhibit the carbon in the fluidized bed gasification furnace from reacting with oxygen to generate carbon dioxide after entering the fluidized bed gasification furnace, the generation of the carbon dioxide is reduced, the reaction of the carbon and water vapor is promoted, and the effective gas components of crude gas are improved;
when the controller 25 receives that the detection value of the ash temperature sensor 5 is more than 500 ℃, the controller 25 sends an opening degree increase signal to the aeration control valve 11 to increase the introduction amount of carbon dioxide of the cooling gas, so as to reduce the temperature of the ash;
(2) secondary cooling by steam: the ash after primary cooling moves downwards along the ash pipe 4 and contacts with cooling water, the cooling water at the liquid level of the cooling water absorbs the heat of the ash to evaporate, the steam generated by evaporation moves upwards along the ash pipe 4 to cool the ash for the second time, the temperature of the ash after secondary cooling is 200-300 ℃, and the steam after heat exchange with the ash moves upwards along the ash pipe 4 and enters a gasification furnace to be used as a gasification agent, so that the external supply amount of the steam is reduced, and the input cost of the steam is reduced; the low-temperature cooling water is supplemented after the cooling water is evaporated, and forced circulation cooling of the cooling water is not needed, so that the blockage of a circulating pump and a heat exchanger in the circulating cooling process is avoided, the smooth operation of a slag discharging device is ensured, and the slag discharging efficiency is ensured;
(3) cooling water for three times: the ash slag is immersed in cooling water after entering the cooling water, the cooling water can fully cool the ash slag, the cooling effect is ensured, and the cooling water cools the ash slag for three times to be cooled to below 150 ℃;
when the controller 25 receives that the detection value of the cold slag pot temperature sensor 41 is more than 150 ℃, the controller 25 sends an opening degree increasing signal to the water inlet control valve 8 to increase the entering amount of cooling water, so that the temperature of the cooling water in the cold slag pot 1 is reduced, and the temperature of ash and slag is further reduced;
(4) slag feeding and discharging of the slag discharging tank: the ash cooled for three times moves downwards to enter the slag collecting tank 2 for temporary storage, when the ash in the slag discharging tank 3 is exhausted, the second slag discharging valve 19 is closed, the water injection valve 18 is opened to start water injection, when the detection value of the slag discharging liquid level sensor 17 reaches the preset value of the controller 25, the controller 25 sends a closing signal to the water injection valve 18, the water injection valve 18 is closed, when the detection value of the slag discharging tank pressure sensor 16 is greater than the detection value of the cold slag tank pressure sensor 12, the controller 25 sends an opening signal to the pressure release valve 15 to release the pressure of the slag discharging tank 3, and when the detection value of the slag discharging tank pressure sensor 16 is equal to the cold slag tank pressure sensor 12, the pressure release valve 15 is closed;
after the liquid level and the pressure in the slag discharging tank 3 are adjusted according to the steps, the first slag discharging valve 14 is opened, high-pressure gas at the top of the slag discharging tank 3 moves upwards to enter the slag collecting tank 2, and ash residues at the lower part of the slag collecting tank 2 are disturbed and move downwards to enter the slag discharging tank 3; after the feed of slag discharging tank 3, close first slag discharging valve 14, open relief valve 15, after the detected value of slag discharging tank pressure sensor 16 equals zero, open second slag discharging valve 19 and slag flushing valve 23, the lime-ash is drawn the injection water by the high pressure and is taken away smoothly, flow direction slag storage device along slag discharging main pipe 20, at the slag feeding and the slag discharging in-process of slag discharging tank 3, water balance valve 13 is the open mode all the time, the water that slag discharging tank 3 injected and the delivery water of slag discharging main pipe 20 are the water of receiving slag tank 2 through water balance valve 13 discharge, carry out make full use of to the water of receiving slag tank 2 discharge, reduce the use amount of pure water resource.
The ash in the main ash discharge pipe 20 is conveyed by high-pressure water, so that the ash can be conveyed into the ash storage device at the tail end of the main ash discharge pipe 20 along the main ash discharge pipe 20 without limiting the position of the ash storage device, the flexibility of the placement position of equipment is improved, high-pressure gas in the ash discharge tank 3 is discharged outside through the main ash discharge pipe 20, certain pressure is provided for conveying the ash, and smooth conveying of the ash is guaranteed.
The water injected into the slag discharging tank 3 and the conveying water of the slag discharging main pipe 20 are provided by the slag collecting tank 2 through the water discharged by the water balance valve 13, the slag collecting tank flushing valve 24 and the control valve 22 are opened at regular time, the cooling water discharged by the cooling water pipe is used for flushing pipelines through which the slag water flows, the pipelines through which the slag water flows are prevented from being blocked, and the flushing period is determined according to the actual working condition of the system operation.
When the low liquid level sensor 30 detects that the liquid level of the cooling water in the cold slag tank 1 reaches a preset liquid level lower limit value, the opening degree of the water inlet control valve 8 is increased, the opening degree of the water balance valve 13 is decreased, and water is supplemented to the tank body 26; when the high liquid level sensor 28 detects that the liquid level of the cooling water reaches the preset upper limit value of the liquid level, the opening degree of the water inlet control valve 8 is reduced, and the opening degree of the water balance valve 13 is increased, so that the liquid level of the cooling water in the tank body 26 is always kept between the lowest liquid level and the highest liquid level, the coal cinder can be immersed in the cooling water, and a good cooling effect is ensured.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.
Claims (11)
1. A cooling and deslagging system for coal ash and slag is characterized by comprising a cold slag tank, a slag collecting tank and a slag discharging tank, wherein an outlet of a slag pipe extends to the inner bottom of the cold slag tank, a slag temperature sensor is arranged inside the top end of the slag pipe, a cooling water pipe is communicated with a water inlet pipe of the cold slag tank, a water inlet control valve is arranged on the water inlet pipe, an inflation pipe is communicated with the upper part of the slag pipe inside the cold slag tank, the cooling air pipe is communicated with the inflation pipe, an inflation control valve is arranged on the inflation pipe, and a cold slag tank pressure sensor and a cold slag tank temperature sensor are arranged at the top of the cold slag tank;
a slag discharge port at the bottom of the cold slag tank is communicated with a slag inlet at the top of the slag collecting tank, and the top of the slag collecting tank is provided with a water balance valve; receive the row's cinder notch of sediment jar bottom through first sediment valve with arrange the slag inlet intercommunication at sediment tank deck the relief valve and arrange sediment jar pressure sensor have been installed at the top of sediment jar arrange the lateral part of sediment jar and have installed sediment level sensor arrange the second sediment valve of arranging the bottom of sediment jar, the second is arranged sediment valve and is arranged sediment house steward intercommunication the second is arranged sediment valve top arrange sediment jar facial make-up and be equipped with the water injection valve.
2. The system of claim 1, wherein a communication pipe is connected between the cooling water pipe and the water injection valve, and a control valve is installed on the communication pipe.
3. The cooling and deslagging system of coal ash slag according to claim 2, characterized in that the communicating pipe at the outlet end of the control valve is communicated with the deslagging header pipe through a slag flushing valve, and the outlet end of the pressure relief valve is communicated with the inlet of the deslagging header pipe.
4. The cooling and deslagging system for coal ash and slag according to claim 3, characterized in that the outlet end of said water balance valve is communicated with said communicating pipe at the outlet end of said control valve, and said communicating pipe at the inlet end of said control valve is communicated with the inlet end of said water balance valve through a slag collecting tank flushing valve.
5. The coal ash cooling and deslagging system of claim 4, wherein the ash temperature sensor, the cold slag tank pressure sensor, the deslagging tank pressure sensor and the deslagging liquid level sensor are all electrically connected with an input end of a controller, and an output end of the controller is respectively electrically connected with the water inlet control valve, the air charging control valve and the pressure relief valve.
6. The coal ash cooling and deslagging system of any one of claims 1 to 5, wherein the cold slag tank comprises a tank body, the middle part of the tank body is vertically provided with the ash pipe, the top end of the ash pipe extends to the outside of the top end of the tank body, and a channel is formed between the bottom end of the ash pipe and the bottom end of the tank body; a high liquid level sensor is arranged in the tank body below the inflation tube; a plurality of balance holes are formed in the ash pipe below the high liquid level sensor along the circumferential direction, a low liquid level sensor is arranged in the tank body below the balance holes, and the high liquid level sensor and the low liquid level sensor are electrically connected with the water inlet control valve and the water balance valve; the side part of the tank body is communicated with the water inlet pipe, the outer part of the ash residue pipe is sleeved with an annular water distribution pipe communicated with the water inlet pipe, and the pipe wall of the annular water distribution pipe is provided with a plurality of water distribution holes.
7. The cooling and deslagging system for coal ash and slag according to claim 6, wherein said ash pipe includes a straight pipe heat exchange section, an expanded diameter pipe vaporization section and a straight pipe deslagging section which are sequentially communicated from top to bottom, said gas charging pipe is disposed on said straight pipe heat exchange section, and said balance hole is opened on the upper portion of said expanded diameter pipe vaporization section.
8. The cooling and deslagging system for coal ash according to claim 6, characterized in that a gas distribution pipe is embedded in said ash pipe above said high level sensor, and said gas charging pipe is communicated with said ash pipe through said gas distribution pipe; the gas distribution pipe comprises an annular sintered metal filter element and a split sleeve, wherein the sintered metal filter element is arranged on the outer pipe body, the pipe body is embedded in the ash pipe, the top end and the bottom end of the pipe body are respectively connected with the ash pipe through flanges, and the gas filling pipe is communicated with the inside of the pipe body.
9. The system of claim 6, wherein a refractory layer is disposed on an inner wall of the ash pipe outside the tank.
10. The cooling and deslagging system of the coal ash according to claim 6, characterized in that a grate plate is fixed between the outer wall of the lower part of the ash pipe and the inner wall of the tank body, and a manhole is arranged on the side wall of the tank body.
11. The system of claim 6, wherein the gas-filled tube is a carbon dioxide gas-filled tube.
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| CN201910138543.2A CN111154516A (en) | 2019-02-25 | 2019-02-25 | Cooling and deslagging system for coal ash |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114479944A (en) * | 2021-12-21 | 2022-05-13 | 中国科学院工程热物理研究所 | Slag cooling device and fluidized bed gasification furnace |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114479944A (en) * | 2021-12-21 | 2022-05-13 | 中国科学院工程热物理研究所 | Slag cooling device and fluidized bed gasification furnace |
| CN114479944B (en) * | 2021-12-21 | 2023-10-27 | 中国科学院工程热物理研究所 | Slag cooling device and fluidized bed gasifier |
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