CN113998751A - A system for flash extraction of desulfurized slurry to extract hot water - Google Patents

A system for flash extraction of desulfurized slurry to extract hot water Download PDF

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Publication number
CN113998751A
CN113998751A CN202111447491.0A CN202111447491A CN113998751A CN 113998751 A CN113998751 A CN 113998751A CN 202111447491 A CN202111447491 A CN 202111447491A CN 113998751 A CN113998751 A CN 113998751A
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water
outlet
inlet
pump
heat pump
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CN202111447491.0A
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Chinese (zh)
Inventor
徐世明
彭烁
蔡洪波
周贤
刘新宇
钟迪
姚国鹏
黄永琪
安航
白烨
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Huaneng Clean Energy Research Institute
Huaneng Yingkou Thermal Power Co Ltd
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Huaneng Clean Energy Research Institute
Huaneng Yingkou Thermal Power Co Ltd
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Priority to CN202111447491.0A priority Critical patent/CN113998751A/en
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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/06—Flash evaporation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/16—Treatment of water, waste water, or sewage by heating by distillation or evaporation using waste heat from other processes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/18—Nature of the water, waste water, sewage or sludge to be treated from the purification of gaseous effluents

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention relates to the technical field of flue gas treatment, in particular to a system for extracting hot water by desulfurization slurry flash evaporation, which comprises a desulfurization tower, a flash tank, an absorption heat pump, heat source equipment and water treatment equipment, wherein a slurry outlet of the desulfurization tower is connected with a slurry inlet of the flash tank, a steam outlet of the flash tank is connected with a low-temperature heat source inlet of the absorption heat pump, and a high-temperature heat source inlet of the absorption heat pump is connected with an outlet of the heat source equipment; the inlet of the water treatment equipment is connected with the low-temperature heat source outlet of the absorption heat pump, and the outlet of the water treatment equipment is connected with the water replenishing inlet of the absorption heat pump. According to the system for extracting heat and water from the desulfurization slurry through flash evaporation, a large amount of water vapor is extracted from the desulfurization slurry through a flash evaporation mode, and the water vapor is condensed in the absorption heat pump and then mixed with the demineralized water replenishing water of a power plant and then conveyed to a thermodynamic system, so that the recovery and utilization rate of heat energy in the flue gas are improved, and the water consumption of the power plant is reduced.

Description

System for desulfurization slurry flash distillation is carried hot water intaking
Technical Field
The invention relates to the field of flue gas treatment technology, in particular to a system for extracting hot water by desulfurization slurry flash evaporation.
Background
The utility boiler, as the first large energy consumption equipment in China, consumes about 15 million tons of standard coal each year, accounting for nearly 50% of the total coal consumption in China. At present, the thermal efficiency of large-scale power station boilers is generally about 90-94%, and the heat loss of exhaust smoke accounts for more than half of the total heat loss, so that huge waste heat resources are stored. And a large amount of moisture contained in the boiler exhaust gas is discharged to the atmosphere.
At present, most coal-fired cogeneration units adopt a plurality of energy-saving measures, and the reduction of smoke discharge loss becomes one part of the units with the largest energy-saving potential after the loss of a cold end is basically eliminated. The waste heat of the flue gas is recycled to reduce the temperature of the discharged flue gas, the loss of the discharged flue gas is reduced, and the energy utilization efficiency of the unit can be effectively improved.
If the waste heat of the boiler flue gas can be deeply utilized, the thermal power generating unit can save a large amount of coal consumption, thereby reducing pollutant emission and saving water, and having great significance to the strategy of energy conservation and emission reduction in China.
Disclosure of Invention
Aiming at the problems of low heat utilization rate and high water consumption of a power plant in the prior art, the invention provides a system for extracting hot water by desulfurization slurry flash evaporation.
The invention is realized by the following technical scheme:
a system for extracting hot water by desulfurization slurry flash evaporation comprises a desulfurization tower, a flash tank, an absorption heat pump, heat source equipment and water treatment equipment, wherein a slurry outlet of the desulfurization tower is connected with a slurry inlet of the flash tank, a steam outlet of the flash tank is connected with a low-temperature heat source inlet of the absorption heat pump, and a high-temperature heat source inlet of the absorption heat pump is connected with an outlet of the heat source equipment; the inlet of the water treatment equipment is connected with the low-temperature heat source outlet of the absorption heat pump, and the outlet of the water treatment equipment is connected with the water replenishing inlet of the absorption heat pump.
Preferably, the heat source equipment comprises a steam turbine and a condenser, a steam exhaust outlet of the steam turbine is connected with a steam inlet of the condenser, a steam extraction outlet of the steam turbine is connected with a high-temperature heat source inlet of the absorption heat pump, and the condenser is connected with the absorption heat pump.
Preferably, a first mixer is further arranged between the condenser and the absorption heat pump, a condensed water inlet of the first mixer is connected with a condensed water outlet of the condenser, and a water supplement outlet of the absorption heat pump is connected with a water supplement inlet of the first mixer.
Preferably, a circulating pump is further arranged between the first mixer and the condenser, a condensed water inlet of the circulating pump is connected with a condensed water outlet of the condenser, and a condensed water outlet of the circulating pump is connected with a condensed water inlet of the first mixer.
Preferably, a control device is arranged between the water treatment device and the absorption heat pump, the control device comprises a water pump and a second mixer which are sequentially arranged, an outlet of the water treatment device is connected with an inlet of the water pump, an outlet of the water pump is connected with an inlet of the second mixer, and an outlet of the second mixer is connected with a water supplementing inlet of the absorption heat pump.
Preferably, a booster pump is arranged between the second mixer and the absorption heat pump, an outlet of the second mixer is connected with an inlet of the booster pump, and an outlet of the booster pump is connected with a water replenishing inlet of the absorption heat pump.
Preferably, the slurry outlet of the flash tank is connected with the slurry spraying inlet of the desulfurization tower.
Preferably, the slurry spraying inlet of the desulfurization tower is positioned at the top end of the desulfurization tower.
Compared with the prior art, the invention has the following beneficial effects:
the system for extracting heat and water from the desulfurization slurry through flash evaporation not only extracts a large amount of water vapor from the desulfurization slurry in a flash evaporation mode, the water vapor is condensed in the absorption heat pump, then is conveyed to a thermodynamic system through water treatment equipment, and is mixed with the steam in the heat source equipment in the absorption heat pump, so that the process of extracting heat and water is realized, the recovery and utilization rate of heat energy in flue gas are improved, and the water consumption of a power plant is reduced.
The system for extracting hot water by desulfurization slurry flash evaporation reduces the temperature of the desulfurization slurry in a flash evaporation mode, thereby reducing the temperature of flue gas, reducing the water content of the flue gas and achieving the effect of eliminating white smoke.
The system for extracting heat and water by desulfurization slurry flash evaporation provided by the invention uses the desulfurization slurry extracted heat as a low-temperature heat source of the absorption heat pump, uses the steam extracted by the steam turbine as a high-temperature heat source, and jointly drives the absorption heat pump for preheating and supplementing water, thereby achieving the effect of reducing the heat loss of exhaust smoke.
The slurry outlet of the flash tank is connected with the slurry spraying inlet of the desulfurizing tower so as to recycle the cold slurry, the slurry in the desulfurizing tower can be cooled, the water balance problem in the desulfurizing tower can be solved, and the possibility of equipment failure caused by the expansion tank of the desulfurizing tower is reduced.
Drawings
FIG. 1 is a schematic diagram of a system for extracting hot water by desulfurization slurry flash evaporation.
In the figure, 1, a steam turbine; 2. a condenser; 3. a circulation pump; 4. a first mixer; 5. a desulfurizing tower; 6. a slurry pump; 7. a flash tank; 8. an absorption heat pump; 9. a water treatment device; 10. a water pump; 11. a second mixer; 12. a booster pump.
Detailed Description
The present invention will now be described in further detail with reference to specific examples, which are intended to be illustrative, but not limiting, of the invention.
A system for extracting hot water by desulfurization slurry flash evaporation refers to fig. 1, and comprises a desulfurization tower 5, a flash tank 7, an absorption heat pump 8, heat source equipment and water treatment equipment 9, wherein a slurry outlet of the desulfurization tower 5 is connected with a slurry inlet of the flash tank 7 and is controlled by a slurry pump 6. The slurry outlet of the flash tank 7 is connected with the slurry spraying inlet of the desulfurizing tower 5, and the slurry spraying inlet of the desulfurizing tower 5 is positioned at the top of the desulfurizing tower 5.
The heat source equipment comprises a steam turbine 1 and a condenser 2, and a steam outlet of the flash tank 7 is connected with an absorption heat pump 8; an exhaust steam outlet of the steam turbine 1 is connected with a steam inlet of the condenser 2, an exhaust steam outlet of the steam turbine 1 is connected with a high-temperature heat source inlet of the absorption heat pump 8, and the condenser 2 is connected with the absorption heat pump 8; the low-temperature heat source inlet of the absorption heat pump 8 is connected with the steam outlet of the flash tank 7.
Still be equipped with first blender 4 and circulating pump 3 between condenser 2 and the absorption heat pump 8, the condensate inlet of circulating pump 3 and the condensate outlet connection of condenser 2, the condensate outlet of circulating pump 3 and the condensate inlet connection of first blender 4, the condensate inlet of first blender 4 and the condensate outlet connection of condenser 2, the moisturizing export of absorption heat pump 8 and the moisturizing entry linkage of first blender 4.
The inlet of the water treatment device 9 is connected with the low-temperature heat source outlet of the absorption heat pump 8, and the outlet of the water treatment device 9 is connected with the water replenishing inlet of the absorption heat pump 8.
A control device is arranged between the water treatment device 9 and the absorption heat pump 8, the control device comprises a water pump 10 and a second mixer 11 which are arranged in sequence, an outlet of the water treatment device 9 is connected with an inlet of the water pump 10, and an outlet of the water pump 10 is connected with an inlet of the second mixer 11.
A booster pump 12 is arranged between the second mixer 11 and the absorption heat pump 8, the outlet of the second mixer 11 is connected with the inlet of the booster pump 12, and the outlet of the booster pump 12 is connected with the water replenishing inlet of the absorption heat pump 8.
The invention discloses an implementation principle of a system for extracting hot water by desulfurization slurry flash evaporation, which comprises the following steps: the desulfurization slurry enters a flash tank 7 from a desulfurization tower 5 under the action of a slurry pump 6, is subjected to an evaporative cooling process in the flash tank 7, is flashed to generate steam, is cooled to become cold slurry, is sent to the desulfurization tower 5, and is sprayed into the tower from the top.
The steam flashed out from the flash tank 7 is used as a low-temperature heat source of the absorption heat pump, the extracted steam from the steam turbine 1 is used as a high-temperature heat source of the collecting device, heat is released in the collecting device and condensed into water, the collecting device is used for preheating and supplementing water, and the preheated and supplemented water is sent into a thermodynamic system, so that water recovery is realized.
According to the system for extracting heat and water from the desulfurization slurry through flash evaporation, a large amount of water vapor is extracted from the desulfurization slurry through a flash evaporation mode, and the water vapor is condensed in the absorption heat pump and then mixed with the demineralized water replenishing water of a power plant and then conveyed to a thermodynamic system, so that the recovery and utilization rate of heat energy in the flue gas are improved, and the water consumption of the power plant is reduced. The cold slurry in the flash tank 7 is conveyed back to the desulfurizing tower 5, and the slurry in the desulfurizing tower 5 can be cooled, so that the problem of water balance in the desulfurizing tower 5 can be solved, and the equipment failure caused by the expansion tank of the desulfurizing tower 5 is avoided.

Claims (8)

1.一种脱硫浆液闪蒸提热取水的系统，其特征在于，包括脱硫塔(5)、闪蒸罐(7)、吸收式热泵(8)、热源设备和水处理设备(9)，所述脱硫塔(5)的浆液出口与闪蒸罐(7)的浆液入口连接，所述闪蒸罐(7)的蒸汽出口与吸收式热泵(8)的低温热源入口连接，所述吸收式热泵(8)的高温热源入口与热源设备的出口连接；所述水处理设备(9)的入口与吸收式热泵(8)的低温热源出口连接，所述水处理设备(9)的出口与吸收式热泵(8)的补水入口连接。1. a system of desulfurization slurry flash extraction hot water, is characterized in that, comprises desulfurization tower (5), flash tank (7), absorption heat pump (8), heat source equipment and water treatment equipment (9), so The slurry outlet of the desulfurization tower (5) is connected with the slurry inlet of the flash tank (7), and the steam outlet of the flash tank (7) is connected with the low-temperature heat source inlet of the absorption heat pump (8). The high temperature heat source inlet of (8) is connected to the outlet of the heat source equipment; the inlet of the water treatment equipment (9) is connected to the low temperature heat source outlet of the absorption heat pump (8), and the outlet of the water treatment equipment (9) is connected to the absorption type heat source outlet. The make-up water inlet of the heat pump (8) is connected. 2.根据权利要求1所述的脱硫浆液闪蒸提热取水的系统，其特征在于，所述热源设备包括汽轮机(1)和凝汽器(2)，所述汽轮机(1)的排汽出口与凝汽器(2)的蒸汽入口连接，所述汽轮机(1)的抽汽出口与吸收式热泵(8)的高温热源入口连接，所述凝汽器(2)与吸收式热泵(8)连接。2 . The system for extracting hot water by flash distillation of desulfurization slurry according to claim 1 , wherein the heat source equipment comprises a steam turbine (1) and a condenser (2), and the exhaust steam outlet of the steam turbine (1) Connected to the steam inlet of the condenser (2), the extraction steam outlet of the steam turbine (1) is connected to the high temperature heat source inlet of the absorption heat pump (8), and the condenser (2) is connected to the absorption heat pump (8) connect. 3.根据权利要求2所述的脱硫浆液闪蒸提热取水的系统，其特征在于，所述凝汽器(2)和吸收式热泵(8)之间还设有第一混合器(4)，所述第一混合器(4)的凝结水入口与凝汽器(2)的凝结水出口连接，所述吸收式热泵(8)的补水出口与第一混合器(4)的补水入口连接。3. The system for extracting hot water by flash distillation of desulfurization slurry according to claim 2, wherein a first mixer (4) is also provided between the condenser (2) and the absorption heat pump (8). , the condensed water inlet of the first mixer (4) is connected to the condensed water outlet of the condenser (2), and the water replenishment outlet of the absorption heat pump (8) is connected to the water replenishment inlet of the first mixer (4) . 4.根据权利要求3所述的脱硫浆液闪蒸提热取水的系统，其特征在于，所述第一混合器(4)与凝汽器(2)之间还设有循环泵(3)，所述循环泵(3)的凝结水入口与凝汽器(2)的凝结水出口连接，所述循环泵(3)的凝结水出口与第一混合器(4)的凝结水入口连接。4. The system for extracting hot water by flash evaporation of desulfurization slurry according to claim 3, wherein a circulating pump (3) is also provided between the first mixer (4) and the condenser (2), The condensed water inlet of the circulating pump (3) is connected with the condensed water outlet of the condenser (2), and the condensed water outlet of the circulating pump (3) is connected with the condensed water inlet of the first mixer (4). 5.根据权利要求1所述的脱硫浆液闪蒸提热取水的系统，其特征在于，所述水处理设备(9)与吸收式热泵(8)之间设有控制设备，所述控制设备包括依次设置的水泵(10)和第二混合器(11)，所述水处理设备(9)的出口与水泵(10)的入口连接，所述水泵(10)的出口与第二混合器(11)入口连接，所述第二混合器(11)的出口与吸收式热泵(8)的补水入口连接。5. The system for extracting hot water by flash evaporation of desulfurization slurry according to claim 1, characterized in that, a control device is provided between the water treatment device (9) and the absorption heat pump (8), and the control device comprises: A water pump (10) and a second mixer (11) are arranged in sequence, the outlet of the water treatment device (9) is connected to the inlet of the water pump (10), and the outlet of the water pump (10) is connected to the second mixer (11) ) is connected to the inlet, and the outlet of the second mixer (11) is connected to the water supply inlet of the absorption heat pump (8). 6.根据权利要求5所述的脱硫浆液闪蒸提热取水的系统，其特征在于，所述第二混合器(11)和吸收式热泵(8)之间设有加压泵(12)，所述第二混合器(11)的出口与加压泵(12)的入口连接，所述加压泵(12)的出口与吸收式热泵(8)的补水入口连接。6. The system for flashing and extracting hot water from desulfurization slurry according to claim 5, wherein a pressurizing pump (12) is provided between the second mixer (11) and the absorption heat pump (8), The outlet of the second mixer (11) is connected to the inlet of the pressurizing pump (12), and the outlet of the pressurizing pump (12) is connected to the water supply inlet of the absorption heat pump (8). 7.根据权利要求1所述的脱硫浆液闪蒸提热取水的系统，其特征在于，所述闪蒸罐(7)的浆液出口与脱硫塔(5)的浆液喷淋入口连接。7. The system for flashing and extracting hot water from desulfurization slurry according to claim 1, wherein the slurry outlet of the flash tank (7) is connected to the slurry spray inlet of the desulfurization tower (5). 8.根据权利要求7所述的脱硫浆液闪蒸提热取水的系统，其特征在于，所述脱硫塔(5)的浆液喷淋入口位于脱硫塔(5)顶端。8 . The system for extracting hot water by flash distillation of desulfurization slurry according to claim 7 , wherein the slurry spray inlet of the desulfurization tower ( 5 ) is located at the top of the desulfurization tower ( 5 ). 9 .
CN202111447491.0A 2021-11-30 2021-11-30 A system for flash extraction of desulfurized slurry to extract hot water Pending CN113998751A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114797387A (en) * 2022-05-31 2022-07-29 华能营口热电有限责任公司 Flue gas deep carbon capture device and method for recovering waste heat
CN114988512A (en) * 2022-05-31 2022-09-02 华能营口热电有限责任公司 Geothermal energy driven desulfurization slurry flash evaporation heat supply system and method
CN115143438A (en) * 2022-05-31 2022-10-04 华能营口热电有限责任公司 A system and method for generating electricity by recovering flue gas waste heat by flashing of desulfurization slurry
CN115183306A (en) * 2022-05-31 2022-10-14 华能营口热电有限责任公司 System and method for supplying heat by virtue of desulfurization slurry flash evaporation and solar energy complementation

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3064841A1 (en) * 2015-01-08 2016-09-07 Tsinghua University Gas steam combined cycle central heating device and heating method
CN110425902A (en) * 2019-08-26 2019-11-08 华能国际电力股份有限公司 Flue gas waste heat recycling system and method after wet desulphurization
CN111396913A (en) * 2020-04-29 2020-07-10 华能国际电力股份有限公司 A system and method for recovering waste heat and moisture from flue gas of coal-fired units
CN212057351U (en) * 2020-04-29 2020-12-01 华能国际电力股份有限公司 A recovery system for waste heat and moisture in flue gas of coal-fired units
CN216273194U (en) * 2021-11-30 2022-04-12 华能营口热电有限责任公司 A system for flash extraction of desulfurized slurry to extract hot water

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3064841A1 (en) * 2015-01-08 2016-09-07 Tsinghua University Gas steam combined cycle central heating device and heating method
CN110425902A (en) * 2019-08-26 2019-11-08 华能国际电力股份有限公司 Flue gas waste heat recycling system and method after wet desulphurization
CN111396913A (en) * 2020-04-29 2020-07-10 华能国际电力股份有限公司 A system and method for recovering waste heat and moisture from flue gas of coal-fired units
CN212057351U (en) * 2020-04-29 2020-12-01 华能国际电力股份有限公司 A recovery system for waste heat and moisture in flue gas of coal-fired units
CN216273194U (en) * 2021-11-30 2022-04-12 华能营口热电有限责任公司 A system for flash extraction of desulfurized slurry to extract hot water

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114797387A (en) * 2022-05-31 2022-07-29 华能营口热电有限责任公司 Flue gas deep carbon capture device and method for recovering waste heat
CN114988512A (en) * 2022-05-31 2022-09-02 华能营口热电有限责任公司 Geothermal energy driven desulfurization slurry flash evaporation heat supply system and method
CN115143438A (en) * 2022-05-31 2022-10-04 华能营口热电有限责任公司 A system and method for generating electricity by recovering flue gas waste heat by flashing of desulfurization slurry
CN115183306A (en) * 2022-05-31 2022-10-14 华能营口热电有限责任公司 System and method for supplying heat by virtue of desulfurization slurry flash evaporation and solar energy complementation

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