CN111302424A - Low-energy-consumption desulfurization wastewater treatment system and working method thereof - Google Patents
Low-energy-consumption desulfurization wastewater treatment system and working method thereof Download PDFInfo
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- CN111302424A CN111302424A CN202010231667.8A CN202010231667A CN111302424A CN 111302424 A CN111302424 A CN 111302424A CN 202010231667 A CN202010231667 A CN 202010231667A CN 111302424 A CN111302424 A CN 111302424A
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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
- C02F1/16—Treatment of water, waste water, or sewage by heating by distillation or evaporation using waste heat from other processes
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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
- C02F1/10—Treatment of water, waste water, or sewage by heating by distillation or evaporation by direct contact with a particulate solid or with a fluid, as a heat transfer medium
- C02F1/12—Spray evaporation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/006—Layout of treatment plant
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
- F23J15/025—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using filters
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
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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
- 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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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2215/00—Preventing emissions
- F23J2215/20—Sulfur; Compounds thereof
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2217/00—Intercepting solids
- F23J2217/10—Intercepting solids by filters
- F23J2217/102—Intercepting solids by filters electrostatic
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
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- Treating Waste Gases (AREA)
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Abstract
The invention discloses a low-energy-consumption desulfurization wastewater treatment system and a working method thereof, and belongs to the technical field of flue gas waste heat utilization and desulfurization wastewater treatment. For a boiler, an economizer, an air preheater, an electrostatic dust collector, a wet desulphurization tower and a chimney which are connected in sequence, a smoke cooler is arranged between the electrostatic dust collector and the wet desulphurization tower, a smoke outlet of the electrostatic dust collector is connected with a smoke inlet of the smoke cooler, a smoke outlet of the smoke cooler is connected with a smoke inlet of the wet desulphurization tower, a waste water outlet of the wet desulphurization tower is connected with a waste water preprocessor, the waste water preprocessor is connected with a waste water inlet of the smoke cooler, and a waste water outlet of the smoke cooler is connected with a waste water rotary evaporator. The system is simple to operate, low in energy consumption, low in operation cost and high in operation reliability, can remove the fly ash in the flue gas while removing the sulfur oxides in the desulfurization wastewater, and the fly ash cannot be blocked and hardened.
Description
Technical Field
The invention belongs to the technical field of flue gas waste heat utilization and desulfurization wastewater treatment, and particularly relates to a low-energy-consumption desulfurization wastewater treatment system and a working method thereof.
Background
The energy structure of China is continuously improved, and the coal accounts for about 60% of the energy structure of China from 70% ten years ago to 2019. Nevertheless, coal remains the main fuel in energy consumption in china. The sulfur oxides produced in the coal combustion process are major atmospheric pollutants and also one of the important precursors of particulate matters and acid rain. In recent years, the pollution control strength of China is continuously increased, coal-fired power stations with large coal consumption are comprehensively transformed by ultra-low emission technology, and the overall quality of the environment is improved year by year.
The limestone gypsum wet flue gas desulfurization process in the desulfurization method of the coal-fired power plant is most widely applied due to the characteristics of mature technology, wide absorbent source, strong coal adaptability, low calcium-sulfur ratio, recyclable byproducts and the like. With the development of the technology in recent years, the removal efficiency of sulfur dioxide in the wet flue gas desulfurization process reaches 98 percent, but the removal rate of sulfur trioxide is lower.
The wet flue gas desulfurization process produces a large amount of highly polluted wastewater, and the desulfurization wastewater has the characteristics of high suspended matter, high corrosion, high salt content, various heavy metals and the like. The existing desulfurization wastewater treatment process generally adopts evaporative crystallization and high-temperature flue gas evaporation. The evaporative crystallization process has large equipment investment and high operating cost, and desulfurization wastewater treatment factories using the technology are few. Compared with an evaporative crystallization technology, the high-temperature flue gas evaporation technology has low investment and certain technical advantages, but has the defects of high energy consumption and poor equipment reliability, the power generation coal consumption in the high-temperature flue gas evaporation process is increased by about more than 1.5g/kW.h, and the equipment of the high-temperature flue gas evaporation technology is frequently hardened and blocked by fly ash.
Disclosure of Invention
In order to solve the defects in the prior art, the invention aims to provide a low-energy-consumption desulfurization wastewater treatment system and a working method thereof, which have the advantages of good sulfur oxide removal effect, capability of simultaneously removing fly ash in flue gas, low energy consumption, no blockage and hardening of the fly ash and high reliability.
The invention is realized by the following technical scheme:
the invention discloses a low-energy-consumption desulfurization wastewater treatment system, which comprises a boiler, an economizer, an air preheater, an electrostatic dust collector, a wet desulfurization tower and a chimney which are sequentially connected, and is characterized in that a flue gas cooler is arranged between the electrostatic dust collector and the wet desulfurization tower, a flue gas outlet of the electrostatic dust collector is connected with a flue gas inlet of the flue gas cooler, a flue gas outlet of the flue gas cooler is connected with a flue gas inlet of the wet desulfurization tower, a wastewater outlet of the wet desulfurization tower is connected with a wastewater preprocessor, the wastewater preprocessor is connected with a wastewater inlet of the flue gas cooler, and a wastewater outlet of the flue gas cooler is connected with a wastewater rotary evaporator;
the waste water rotary evaporator comprises an upper straight cylinder section and a lower conical section, a horizontal inlet is formed in the upper side wall of the upper straight cylinder section, the horizontal inlet is connected with a waste water outlet of a smoke cooler and an outlet of an economizer, a center cylinder is arranged at the top of the upper straight cylinder section, one end of the center cylinder is located inside the upper straight cylinder section and is communicated with the inside of the upper straight cylinder section, the other end of the center cylinder is connected with an inlet of an electrostatic dust collector, the lower conical section is connected with a vertical pipe, and the vertical pipe is connected with an ash bin.
Preferably, the lower conical sections of the vertical pipe and the wastewater rotary evaporator are provided with purging ports, the purging ports are respectively connected with purging valves, and the purging valves are connected with air compressors.
Preferably, rappers are arranged on the lower conical sections of the stand pipe and the wastewater rotary evaporator.
Preferably, the ash bin is connected with a pneumatic conveying pipeline, and the pneumatic conveying pipeline is connected with the ash bin.
Preferably, the horizontal inlet is arranged in the tangential direction of the upper straight cylinder section of the wastewater rotary evaporator.
Preferably, the central cylinder is arranged in the center of the upper straight cylinder section of the wastewater rotary evaporator, and the length of the part of the central cylinder positioned inside the upper straight cylinder section is adjustable.
Preferably, the central cartridge opening is lower than the horizontal inlet.
Preferably, a high-pressure waste water pump is arranged between the waste water preprocessor and the waste water inlet of the smoke cooler.
The invention discloses a working method of the low-energy-consumption desulfurization wastewater treatment system, which comprises the following steps:
flue gas discharged by the boiler sequentially enters an air preheater, an electrostatic dust collector and a flue gas cooler through the rear part of the economizer, enters a wet desulfurization tower after exchanging heat with wastewater from a wastewater preprocessor and cooling in the flue gas cooler, and is discharged through a chimney after desulfurization;
waste water from the waste water preprocessor exchanges heat with flue gas in a flue gas cooler and is heated up, and then is atomized at a horizontal inlet of a waste water rotary evaporator to form liquid drops, residual flue gas from an economizer carries the liquid drops formed by the waste water to adhere to the wall at the horizontal inlet and enters the waste water rotary evaporator, the liquid drops are rotationally mixed and evaporated in an upper straight cylinder section, and salts in the waste water are separated out and then are discharged to an ash bin along a lower conical section after falling behind; and the cooled flue gas enters the electrostatic dust collector through the central cylinder for subsequent treatment.
Compared with the prior art, the invention has the following beneficial technical effects:
according to the low-energy-consumption desulfurization wastewater treatment system disclosed by the invention, desulfurization wastewater is atomized and then is mixed with high-temperature flue gas in a rotating manner, the residence time in a wastewater rotary evaporator is long, the heat exchange between wastewater droplets and the flue gas is sufficient, salts and fly ash are discharged through a lower conical section after being attached to walls, rotate, fall and collected, and are not easy to harden and block; a small amount of fly ash and salts enter the electrostatic dust collector along with the flue gas by taking static pressure difference as driving force, the temperature of the mixed flue gas is reduced, partial sulfur oxide in the flue gas is condensed into acid mist due to temperature reduction, and the sulfuric acid mist is easy to adhere to the surface of the fly ash and is removed by collecting dust through electrostatic dust collection. Desulfurization waste water gets into the smoke cooler and preheats, has reduced the smoke temperature that gets into the wet flue gas desulfurization tower simultaneously, risees desulfurization waste water temperature before getting into waste water rotary evaporator, can reduce the quantity of evaporating high temperature flue gas by a wide margin, reduces waste water treatment's coal consumption, and is more energy-conserving. Simultaneously, the smoke cooler has reduced flue gas side smoke temperature for sulfur trioxide is changeed the condensation and is obtained the desorption in the wet flue gas desulfurization tower, and low smoke temperature does benefit to and reduces calcium-sulfur ratio, has improved desulfurization efficiency. The low-temperature flue gas discharged by the central cylinder reduces the temperature and the flow velocity of the flue gas entering the electrostatic dust removal, so that sulfur trioxide is more easily adhered to fly ash, and the removal effect of the electrostatic dust removal on the sulfur trioxide and smoke dust is improved.
Furthermore, the purging ports arranged on the vertical pipe and the lower conical section of the wastewater rotary evaporator can prevent fly ash from being blocked and hardened, and the operation reliability of the system is improved.
Furthermore, the rappers are arranged at the lower conical sections of the vertical pipe and the wastewater rotary evaporator, so that the fly ash can be prevented from being blocked, hardened or adhered to the wall surface, and the running reliability of the system is improved.
Furthermore, the fly ash in the ash bin is transported to the ash bin through a pneumatic conveying pipeline, and the pneumatic conveying device is simple in structure, large in conveying capacity and long in conveying distance.
Further, horizontal import is established on the tangential direction of the straight section of thick bamboo in waste water rotary evaporator upper portion, makes flue gas and the waste water droplet that get into can adhere to the wall and rotate and intensive mixing, prevents to produce the turbulent flow and influences the mixing effect.
Furthermore, the central cylinder is arranged at the center of the upper straight cylinder section of the wastewater rotary evaporator, and the length of the part of the central cylinder positioned in the upper straight cylinder section is adjustable, so that a small amount of fly ash and salts can quickly enter the electrostatic dust collector along with flue gas by taking static pressure difference as driving force, and the efficiency of the device is improved.
Further, the opening of the central cylinder is lower than the horizontal inlet, so that high-temperature flue gas entering the horizontal inlet is prevented from being short-circuited, and the mixing and rotating effect of the flue gas is ensured.
The working method of the low-energy-consumption desulfurization wastewater treatment system disclosed by the invention is simple to operate and low in energy consumption, has the function of removing fly ash in flue gas while removing sulfur oxides in the desulfurization wastewater, and is low in operation cost and high in operation reliability.
Drawings
FIG. 1 is a schematic diagram of the overall structure of a low-energy desulfurization wastewater treatment system of the present invention;
FIG. 2 is a top view of a wastewater rotary evaporator of the present invention.
In the figure: 1-boiler, 2-economizer, 3-air preheater, 4-electrostatic precipitator, 5-smoke cooler, 6-wet desulphurization tower, 7-chimney, 8-waste water preprocessor, 9-high pressure waste water pump, 10-waste water rotary evaporator, 11-horizontal inlet, 12-central cylinder, 13-vertical pipe, 14-ash bin, 15-pneumatic conveying pipeline, 16-ash bin, 17-air compressor, 18-purging port, 19-purging valve and 20-vibrator.
Detailed Description
The invention will now be described in further detail with reference to the following drawings and specific examples, which are intended to be illustrative and not limiting:
the invention discloses a low-energy-consumption desulfurization wastewater treatment system, which is shown in figure 1, and comprises the following components in part by weight: the system comprises a boiler 1, an economizer 2, an air preheater 3, an electrostatic dust collector 4, a wet desulphurization tower 6 and a chimney 7 which are sequentially connected, wherein a smoke cooler 5 is arranged between the electrostatic dust collector 4 and the wet desulphurization tower 6, a smoke outlet of the electrostatic dust collector 4 is connected with a smoke inlet of the smoke cooler 5, a smoke outlet of the smoke cooler 5 is connected with a smoke inlet of the wet desulphurization tower 6, a waste water outlet of the wet desulphurization tower 6 is connected with a waste water preprocessor 8, the waste water preprocessor 8 is connected with a waste water inlet of the smoke cooler 5, a high-pressure waste water pump 9 is arranged between the waste water preprocessor 8 and the waste water inlet of the smoke cooler 5, and a waste water outlet of the smoke cooler 5 is connected with a waste water;
the wastewater rotary evaporator 10 comprises an upper straight cylinder section and a lower conical section, wherein the upper side wall of the upper straight cylinder section is provided with a horizontal inlet 11, and preferably, the horizontal inlet 11 is arranged in the tangential direction of the upper straight cylinder section of the wastewater rotary evaporator (10). The horizontal inlet 11 is connected with a wastewater outlet of the smoke cooler 5 and an outlet of the economizer 2, a central cylinder 12 is arranged at the top of the upper straight cylinder section, one end of the central cylinder 12 is positioned inside the upper straight cylinder section and communicated with the inside of the upper straight cylinder section, the other end of the central cylinder is connected with an inlet of the electrostatic dust collector 4, preferably, the central cylinder 12 is arranged at the center of the upper straight cylinder section of the wastewater rotary evaporator 10, the length of the part of the central cylinder 12 positioned inside the upper straight cylinder section is adjustable, and the opening of the central cylinder 12 is lower than the horizontal inlet 11. The lower conical section is connected with a vertical pipe 13, the vertical pipe 13 is connected with an ash bin 14, the ash bin 14 is connected with a pneumatic conveying pipeline 15, the pneumatic conveying pipeline 15 is connected with an ash bin 16, and the pneumatic conveying pipeline 15 can be connected with an air compressor 17 to obtain power. The lower conical sections of the vertical pipe 13 and the wastewater rotary evaporator 10 are uniformly provided with a purging port 18 and a vibrator 20, the purging port 18 is respectively connected with a purging valve 19, and the purging valve 19 is connected with an air compressor 17.
The working method of the low-energy-consumption desulfurization wastewater treatment system comprises the following steps:
step 1: waste water generated by the wet desulphurization tower 6 is pretreated by a waste water preprocessor 8 and then is conveyed to a waste water rotary evaporator 10 by a high-pressure waste water pump 9 through a smoke cooler 5;
step 2: the flue gas is cooled by 10-20 ℃ through a flue gas cooler 5 and then enters a wet desulphurization tower 6, the reduction of the flue gas temperature increases the physical and chemical properties of sulfur trioxide, more sulfur trioxide is condensed and removed, and meanwhile, the reduction of the flue gas temperature is beneficial to gas-liquid mass transfer in the desulphurization process, the desulphurization efficiency is improved, and the calcium-sulfur ratio is reduced;
and step 3: the preheated wastewater is atomized at a horizontal inlet 11, high-temperature flue gas from the front of an air preheater 3 carries wastewater liquid drops to enter a wastewater rotary evaporator 10 at a speed of 10m/s, the wastewater liquid drops are rotationally mixed and evaporated at a high speed in the wastewater rotary evaporator 10, salts in the wastewater are separated out and fall, and the flue gas is discharged from a central cylinder 12 after heat exchange;
and 4, step 4: the cooled flue gas enters a front flue of the electrostatic dust collector 4 through the central cylinder 12, the temperature of the mixed flue gas is reduced, part of sulfur oxide in the flue gas is condensed into acid mist due to temperature reduction, and the sulfuric acid mist is easy to adhere to the surface of fly ash and is removed by collecting dust through electrostatic dust collection;
and 5: the salt separated out from the wastewater rotary evaporator 10 and the fly ash fall into a vertical pipe 13 and enter an ash bin 14, and the salt and the fly ash are conveyed to an ash bin 16 by compressed air through a pneumatic conveying pipeline 15;
step 6: compressed air is introduced into the lower conical section of the wastewater rotary evaporator 10 and the blowing openings 18 on the vertical pipe 13 at regular time for blowing, so that fly ash is prevented from falling and blocking; the vibrator 20 performs mechanical vibration on the conical section and the vertical pipe 13 of the wastewater rotary evaporator 10 at regular time to prevent fly ash from adhering to the pipe wall and hardening;
and 7: the pretreated desulfurization wastewater is heated by a high-pressure wastewater pump 9 through a smoke cooler 5 and enters a wastewater rotary evaporator 10 for atomization, so that the consumption of high-temperature smoke for evaporation is greatly reduced, and the coal consumption for wastewater treatment is reduced;
the 'zero emission' treatment of the desulfurization wastewater is realized by repeating the steps 1-7, the temperature of the flue gas entering the electrostatic dust collector 4 and the wet desulfurization tower 6 is reduced, the removal efficiency of the electrostatic dust collector 4 and the wet desulfurization tower 6 to sulfur trioxide is improved, and the calcium-sulfur ratio is reduced.
It should be noted that the above description is only one embodiment of the present invention, and all equivalent changes of the system described in the present invention are included in the protection scope of the present invention. Persons skilled in the art to which this invention pertains may substitute similar alternatives for the specific embodiments described, all without departing from the scope of the invention as defined by the claims.
Claims (9)
1. A low-energy-consumption desulfurization wastewater treatment system comprises a boiler (1), an economizer (2), an air preheater (3), an electrostatic dust collector (4), a wet desulfurization tower (6) and a chimney (7) which are connected in sequence, and is characterized in that a smoke cooler (5) is arranged between the electrostatic dust collector (4) and the wet desulfurization tower (6), a smoke outlet of the electrostatic dust collector (4) is connected with a smoke inlet of the smoke cooler (5), a smoke outlet of the smoke cooler (5) is connected with a smoke inlet of the wet desulfurization tower (6), a wastewater outlet of the wet desulfurization tower (6) is connected with a wastewater preprocessor (8), the wastewater preprocessor (8) is connected with a wastewater inlet of the smoke cooler (5), and a wastewater outlet of the smoke cooler (5) is connected with a wastewater rotary evaporator (10);
waste water rotary evaporator (10) includes upper portion straight section of thick bamboo section and lower part conic section, the upper portion lateral wall of upper portion straight section of thick bamboo section is equipped with horizontal import (11), horizontal import (11) and the waste water export of cigarette cooler (5) and the exit linkage of economizer (2), the top of upper portion straight section of thick bamboo section is equipped with center tube (12), the one end of center tube (12) is located the inside and with the inside intercommunication of upper portion straight section of thick bamboo section, the other end and the access connection of electrostatic precipitator (4), the lower part conic section is connected with riser (13), riser (13) are connected with ash bin (14).
2. The low-energy-consumption desulfurization waste water treatment system according to claim 1, characterized in that the lower conical sections of the vertical pipe (13) and the waste water rotary evaporator (10) are provided with purging ports (18), the purging ports (18) are respectively connected with a purging valve (19), and the purging valve (19) is connected with an air compressor (17).
3. Low energy consumption desulfurization waste water treatment system according to claim 1, characterized in that rappers (20) are provided on the lower conical sections of the stand pipe (13) and the waste water rotary evaporator (10).
4. The low-energy-consumption desulfurization wastewater treatment system according to claim 1, characterized in that the ash bin (14) is connected with a pneumatic conveying pipeline (15), and the pneumatic conveying pipeline (15) is connected with an ash bin (16).
5. The low energy consumption desulfurization waste water treatment system according to claim 1, wherein the horizontal inlet (11) is provided in a tangential direction of the upper straight section of the rotary evaporator (10) for waste water.
6. The low-energy desulfurization waste water treatment system according to claim 1, wherein the central cylinder (12) is provided at the center of the upper straight cylinder section of the waste water rotary evaporator (10), and the length of the portion of the central cylinder (12) located inside the upper straight cylinder section is adjustable.
7. Low energy desulfurization waste water treatment system according to claim 1, characterized in that the central cartridge (12) is opened lower than the horizontal inlet (11).
8. A low energy consumption desulfurization wastewater treatment system according to claim 1, characterized in that a high pressure wastewater pump (9) is provided between the wastewater pre-processor (8) and the wastewater inlet of the flue gas cooler (5).
9. The working method of the low-energy-consumption desulfurization waste water treatment system according to any one of claims 1 to 8, characterized by comprising the following steps:
flue gas discharged by a boiler (1) enters an air preheater (3), an electrostatic dust collector (4) and a flue gas cooler (5) in sequence through the rear part of an economizer (2), exchanges heat with wastewater from a wastewater preprocessor (8) in the flue gas cooler (5) to reduce the temperature, enters a wet desulphurization tower (6), and is discharged through a chimney (7) after being desulfurized;
waste water from the waste water preprocessor (8) exchanges heat with flue gas in the flue gas cooler (5) and is heated up, then the waste water is atomized at a horizontal inlet (11) of the waste water rotary evaporator (10) to form liquid drops, residual flue gas from the economizer (2) carries the liquid drops formed by the waste water at the horizontal inlet (11) to adhere to the wall and enters the waste water rotary evaporator (10), the residual flue gas is rotationally mixed and evaporated at an upper straight cylinder section, and salts in the waste water are separated out and then are discharged to an ash bin (14) along a lower conical section and after falling down; the cooled flue gas enters the electrostatic dust collector (4) through the central cylinder (12) for subsequent treatment.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN112047413A (en) * | 2020-08-12 | 2020-12-08 | 国家电投集团电站运营技术（北京）有限公司 | Power plant desulfurization wastewater treatment system and method |
| CN112604497A (en) * | 2020-12-30 | 2021-04-06 | 广东电网有限责任公司电力科学研究院 | System for desulfurization waste water desorption flue gas fine particle and sulfur trioxide in coordination |
| WO2022033512A1 (en) * | 2020-08-14 | 2022-02-17 | 中国华能集团清洁能源技术研究院有限公司 | Near-zero emission type flue gas multi-pollutant integrated removal system and method |
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