CN202393293U - Device for improving cooling effect of cooling tower by means of reducing air moisture - Google Patents

Device for improving cooling effect of cooling tower by means of reducing air moisture Download PDF

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Publication number
CN202393293U
CN202393293U CN2011205252246U CN201120525224U CN202393293U CN 202393293 U CN202393293 U CN 202393293U CN 2011205252246 U CN2011205252246 U CN 2011205252246U CN 201120525224 U CN201120525224 U CN 201120525224U CN 202393293 U CN202393293 U CN 202393293U
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solution
heat exchanger
outlet
inlet
lean
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CN2011205252246U
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李舒宏
丁一
张小松
李阳
冯义康
程德园
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Southeast University
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Southeast University
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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
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2

Abstract

The utility model relates to a device for improving the cooling effect of a cooling tower by means of reducing air moisture. The device is characterized by comprising a cooling water subsystem of a power plant, a CO2 trapping subsystem and a liquid desiccant subsystem, wherein the cooling water subsystem of the power plant and the CO2 trapping subsystem are integrated by the liquid desiccant subsystem, the cooling water subsystem of the power plant comprises the cooling tower (18), the CO2 trapping subsystem comprises an absorption tower (1), a rich liquor pump (2), a rich and barren liquor heat exchanger (3), a regenerating tower (4), a regenerative gas cooler (5), a gas-liquid separator (6), a barren liquor pump (7), a barren liquor heat exchanger (8), a reboiler (9), a barren liquor water-cooling heat exchanger (19) and a regenerative gas water-cooling cooler (20), and the liquid desiccant subsystem comprises a dehumidifier inlet fan (10). The vacuum degree of a condenser is improved, generating efficiency is increased, coal consumption is reduced, and the influence of a CO2 trapping system on power plant efficiency is decreased.

Description

A kind ofly reduce the device that the air water capacity improves the cooling tower cooling effect
Technical field
The utility model relates to a kind of solution dehumidification that utilizes and reclaims chemical method CO 2The energy of capturing device improves the system of cooling tower cooling effect, belongs to CO 2Trapping technique energy recovery energy-saving field.
Background technology
The thermal power plant is as CO 2Maximum emission source, the control CO of thermal power plant 2Discharging is the important component part of global reduction of discharging work.Existing C O 2The capturing device energy consumption is higher, causes the reduction of discharging cost too high, and this is the major obstacle that CCS (collecting carbonic anhydride and storage) technology does not have large-scale application so far.
Be currently applied to CO 2What capture mainly is chemical absorption method, in the absorption tower, absorbs CO through chemical absorbent 2, the rich solution after absorbing then returns the regenerator thermal regeneration, gets into compressor compresses liquefaction after the regeneration gas process cooling condensation, is delivered to burial ground and stores, and the lean solution after the regeneration gets into the absorption tower continuation and absorbs CO after cooling 2In regenerator, need solution to be heated to more than 110 ℃ CO 2Gas just can be separated sucking-off.Regenerative process needs a large amount of heats, and the heat part of input is used to heated solution to desorption temperature, and another part is used to make CO 2From rich solution, desorb, some is taken away by water evaporation and regeneration gas.In lean solution cooling and regeneration gas condensation process, this part heat water that is cooled is taken away not utilization.
Cooling tower is the capital equipment of power plant s cold end system, and the quality of its operation directly influences the heat-economy of unit and power plant.There is document to show, for middle press group, 1 ℃ of the every decline of cooling water temperature, efficient can improve 0.47%; To the high pressure unit, can improve 0.35%.In addition, because the difference of cooling tower design conditions and actual operating mode under some meteorological condition in 1 year, may cause the cooling tower performance decrease, make the power plant lotus of having to lighten the burden move.
The utility model adopts the heat of lean solution and regeneration gas to come the weak solution of solution dehumidification system is regenerated; And the low water capacity air after will dehumidifying is sent into power plant's cooling tower; Improve cooling tower efficient; Reduce condenser inlet coolant water temperature, when improving power generator group efficient, the heat that has effectively utilized the water that is cooled originally to take away.
Summary of the invention
Technical problem:The purpose of the utility model provides a kind of device that improves the cooling tower cooling effect.This system is with solution dehumidification technology and chemical method CO 2Trapping technique is the basis, recycles CO 2Script lean solution and the regeneration gas heat that water is taken away that need be cooled in the capture process; Be used for the regeneration of solution dehumidification system; And the low water capacity air after solution dehumidification system handled is sent into power plant's cooling tower; Improve the cooling tower effect, reduce the condenser cooling water inlet temperature, improve generating set efficient.
Technical scheme:For solving the problems of the technologies described above, the utility model provides a kind of device that the air water capacity improves the cooling tower cooling effect that reduces, and it comprises power plant cooling water subsystem, CO 2Capture subsystem, with power plant's cooling subsystem and CO 2Capture the solution dehumidification subsystem that subsystem combines;
The power plant cooling water subsystem comprises cooling tower;
CO 2Capture subsystem and comprise absorption tower, rich solution pump, poor rich liquid heat exchanger, regenerator, regeneration gas cooler, gas-liquid separator, lean pump, lean solution heat exchanger, reboiler, lean solution water cooling heat exchanger, regeneration gas water-cooled cooler;
The solution dehumidification subsystem comprises dehumidifier inlet blower fan, solution moisture removing device, weak solution pump, water cooling heat exchanger, concentrated solution pump, solution regenerator, regenerator inlet blower fan, concentrated solution weak solution heat exchanger, air water cooler;
In the described solution dehumidification subsystem; The outlet of dehumidifier inlet blower fan links to each other with the blast entrance of solution moisture removing device through airduct; The air intake of the air outlet slit of solution moisture removing device and air water cooler joins, and the air outlet slit of air water cooler communicates with the cooling tower air intake; Weak solution pump intake and the outlet of solution moisture removing device weak solution are joined, and the weak solution pump discharge links to each other with the weak solution inlet of concentrated solution weak solution heat exchanger; The weak solution outlet of concentrated solution weak solution heat exchanger communicates with the weak solution inlet of lean solution heat exchanger; The weak solution outlet of lean solution heat exchanger links to each other with the weak solution inlet of regeneration gas cooler; The weak solution outlet of regeneration gas cooler communicates with the weak solution inlet of solution regenerator; The concentrated solution outlet of solution regenerator links to each other with the import of concentrated solution pump; The concentrated solution inlet of concentrated solution delivery side of pump and concentrated solution weak solution heat exchanger joins; The concentrated solution outlet of concentrated solution weak solution heat exchanger links to each other with the concentrated solution inlet of water cooling heat exchanger; The concentrated solution outlet of water cooling heat exchanger is connected with the concentrated solution inlet of solution moisture removing device; The outlet of regenerator inlet blower fan links to each other with the blast entrance of solution regenerator;
Described CO 2Capture in the subsystem, flue gas gets into the absorption tower gas feed; Absorption tower rich solution outlet is joined with the rich solution pump; The rich solution pump discharge communicates with the rich solution inlet of poor rich liquid heat exchanger; The outlet of poor rich liquid heat exchanger rich solution links to each other with regenerator rich solution inlet; The outlet of regenerator lean solution communicates with the lean pump inlet; The lean pump outlet links to each other with the lean solution inlet of poor rich liquid heat exchanger; The lean solution outlet of poor rich liquid heat exchanger is joined with the lean solution inlet of lean solution heat exchanger; The lean solution outlet of lean solution heat exchanger communicates with the lean solution inlet of lean solution water cooling heat exchanger; The lean solution outlet of lean solution water cooling heat exchanger links to each other with the lean solution inlet on absorption tower; The outlet of regenerator regeneration gas is joined with regeneration gas cooler regeneration gas inlet; The regeneration gas outlet of regeneration gas cooler communicates with the regeneration gas inlet of regeneration gas water-cooled cooler; The regeneration gas outlet of regeneration gas water-cooled cooler communicates with the gas access of gas-liquid separator;
In the described power plant cooling water subsystem, the solution moisture removing device air outlet slit links to each other with the import of air water cooler air, and the outlet of air water cooler air is joined with the cooling tower air intake.
Beneficial effect:
(1) the utility model provides a kind of solution dehumidification that utilizes to reclaim chemical method CO 2The method and apparatus of capturing device energy is recycled lean solution and regeneration gas heat that the water that originally is cooled is taken away, is used for the weak solution regeneration of solution dehumidification system.
(2) the low water capacity air after the solution dehumidification system dehumidifying is sent into power plant's cooling tower, improve cooling tower efficient, reduce the condenser cooling water inflow temperature, improve generating set efficient.
(3) the utility model has made full use of the heat that the water that originally directly is cooled is taken away, and improves generating set efficient, reduces and installs CO additional 2Behind the trapping system to the adverse effect of power plant efficiency.
Description of drawings
Fig. 1 is a kind of installation drawing that improves the cooling tower cooling effect;
Wherein: absorption tower 1; Rich solution pump 2; Poor rich liquid heat exchanger 3; Regenerator 4; Regeneration gas cooler 5; Gas-liquid separator 6; Lean pump 7; Lean solution heat exchanger 8; Reboiler 9; Dehumidifier inlet blower fan 10; Solution moisture removing device 11; Weak solution pump 12; Water cooling heat exchanger 13; Concentrated solution pump 14; Solution regenerator 15; Regenerator inlet blower fan 16; Concentrated solution weak solution heat exchanger 17; Cooling tower 18; Lean solution water cooling heat exchanger 19; Regeneration gas water-cooled cooler 20; Air water cooler 21; Boiler 22, steam turbine 23; Generator 24; Condenser 25; Water pump 26.
The specific embodiment
Below with reference to accompanying drawings the utility model is described.
Utilize solution dehumidification to reclaim chemical method CO 2The system of capturing device energy is based upon solution dehumidification technology and chemical method CO 2On the trapping technique, solution dehumidification agent commonly used has lithium-bromide solution, lithium chloride solution and calcium chloride solution etc.; Commonly used be used to capture CO 2Solution MEA solution, MDEA solution etc. are arranged.
In the power plant cooling water subsystem, the solution moisture removing device air outlet slit links to each other with the cooling tower air intake after reducing to room temperature through the air water cooler, and the air after the dehumidifying is sent into cooling tower through pipeline.
Invention provides a kind of system that improves the cooling tower cooling effect, and it comprises power plant cooling water subsystem, CO 2Capture subsystem, with power plant's cooling subsystem and CO 2Capture the solution dehumidification subsystem that subsystem combines;
The power plant cooling water subsystem comprises cooling tower;
CO 2Capture subsystem and comprise absorption tower, rich solution pump, poor rich liquid heat exchanger, regenerator, regeneration gas cooler, gas-liquid separator, lean pump, lean solution heat exchanger, reboiler, lean solution water cooling heat exchanger, regeneration gas water-cooled cooler;
The solution dehumidification subsystem comprises dehumidifier inlet blower fan, solution moisture removing device, weak solution pump, water cooling heat exchanger, concentrated solution pump, solution regenerator, regenerator inlet blower fan, concentrated solution weak solution heat exchanger, air water cooler;
In the described solution dehumidification subsystem; Outdoor air is admitted in the solution moisture removing device 11 through dehumidifier inlet blower fan 10 and contacts dehumidifying with concentrated solution; Dry air after the dehumidifying is admitted to earlier and is cooled to outdoor dry-bulb temperature in the air water cooler 21; And then be admitted in the cooling tower 18 of power plant cooling water subsystem, strengthen the heat and mass in the cooling tower, to improve the cooling tower cooling effect; In dehumidifier 11, absorbed the weak solution that obtains after water in air is divided by weak solution pump 12 send in the concentrated solution weak solution heat exchanger 17 with regeneration after the concentrated solution heat-shift that obtains, the weak solution after the heat exchange then is admitted in the lean solution heat exchanger 8 and CO 2Capture the lean solution heat exchange in the subsystem, be sent to CO then again 2Capture in the regeneration cooler 5 in the subsystem and export regeneration CO with regenerator 4 2Gas converting heat makes weak solution be heated to regeneration temperature, and then weak solution is admitted in the solution regenerator 15 contact with outdoor air and obtains regenerating; Regeneration air is introduced by regenerator inlet blower fan 16; The concentrated solution that obtains after the regeneration is sent in the concentrated solution weak solution heat exchanger 17 and the weak solution heat exchange by concentrated solution pump 14, then is admitted to water cooling heat exchanger 13, sends into solution moisture removing device 11 after further being cooled to the solution moisture removing device inlet temperature;
Described CO 2Capture in the subsystem, the lean solution reaction of flue gas through obtaining after getting into absorption tower 1 after the desulfurization and regenerating is removed CO in the boiler of power plant 2After purified gas enter atmosphere, the rich solution that obtains is sent into poor rich liquid heat exchanger 3 and lean solution heat-shift through rich solution pump 2 after the reaction, rich solution is admitted to regenerator 4 regeneration then, in regenerator 4, rich solution is heated to regeneration temperature by reboiler 9, with CO wherein 2Desorb; The lean solution that obtains after the regeneration is sent into poor rich liquid heat exchanger 3 and rich solution heat exchange through lean pump 7; Lean solution behind the heat-shift then is admitted in the lean solution heat exchanger 8 the weak solution heat exchange with the solution dehumidification subsystem; And then be admitted in the lean solution water cooling heat exchanger 19, lean solution is admitted to absorption tower 1 after reducing to absorption temperature; The CO that desorbs in the regenerator 4 2Get into the weak solution in the further heated solution dehumidifying subsystem in the regeneration gas cooler 5 with steam, make weak solution obtain regeneration, the CO after the cooling 2Be admitted to further cooling in the regeneration gas water-cooled cooler 20 with condensate, so that the CO of outlet 2Further be compressed and liquefy, condensate is back to regenerator 4 from gas-liquid separator 6;
In the described power plant cooling water subsystem; Dry air through after the solution dehumidification system dehumidifying is admitted to cooling tower 18, has strengthened the heat and mass in the cooling tower, has reduced the outlet water temperature of cooling tower 18; Low cooling water temperature has improved the vacuum of condenser, makes unit efficiency be improved.
Referring to Fig. 1, improve the system of cooling tower cooling effect, it comprises power plant cooling water subsystem, CO 2Capture subsystem, with power plant's cooling subsystem and CO 2Capture the solution dehumidification subsystem that subsystem combines;
The power plant cooling water subsystem comprises cooling tower 18;
CO 2Capture subsystem and comprise absorption tower 1, rich solution pump 2, poor rich liquid heat exchanger 3, regenerator 4, regeneration gas cooler 5, gas-liquid separator 6, lean pump 7, lean solution heat exchanger 8, reboiler 9, lean solution water cooling heat exchanger 19, regeneration gas water-cooled cooler 20;
The solution dehumidification subsystem comprises dehumidifier inlet blower fan 10, solution moisture removing device 11, weak solution pump 12, water cooling heat exchanger 13, concentrated solution pump 14, solution regenerator 15, regenerator inlet blower fan 16, concentrated solution weak solution heat exchanger 17, air water cooler 21;
In the described solution dehumidification subsystem; The outlet of dehumidifier inlet blower fan 10 links to each other with the blast entrance of solution moisture removing device 11 through airduct; The air intake of the air outlet slit of solution moisture removing device 11 and air water cooler 21 joins, and the air outlet slit of air water cooler 21 communicates with cooling tower 18 air intakes; Weak solution pump 12 inlets join with the outlet of solution moisture removing device 11 weak solutions, and 12 outlets of weak solution pump link to each other with the weak solution inlet of concentrated solution weak solution heat exchanger 17; The weak solution outlet of concentrated solution weak solution heat exchanger 17 communicates with the weak solution inlet of lean solution heat exchanger 8; The weak solution outlet of lean solution heat exchanger 8 links to each other with the weak solution inlet of regeneration gas cooler 5; The weak solution outlet of regeneration gas cooler 5 communicates with the weak solution inlet of solution regenerator 15; The concentrated solution outlet of solution regenerator 15 links to each other with the import of concentrated solution pump 14; The concentrated solution inlet of the outlet of concentrated solution pump 14 and concentrated solution weak solution heat exchanger 17 joins; The concentrated solution outlet of concentrated solution weak solution heat exchanger 17 links to each other with the concentrated solution inlet of water cooling heat exchanger 13; The concentrated solution outlet of water cooling heat exchanger 13 is connected with the concentrated solution inlet of solution moisture removing device 11; The outlet of regenerator inlet blower fan 16 links to each other with the blast entrance of solution regenerator 15;
Described CO 2Capture in the subsystem, flue gas links to each other with absorption tower 1 gas feed; Absorption tower 1 rich solution outlet is joined with rich solution pump 2; 2 outlets of rich solution pump communicate with the rich solution inlet of poor rich liquid heat exchanger 3; The outlet of poor rich liquid heat exchanger 3 rich solutions links to each other with regenerator 4 rich solutions inlet; The outlet of regenerator 4 lean solutions communicates with lean pump 7 inlets; Lean pump 7 outlets link to each other with the lean solution inlet of poor rich liquid heat exchanger 3; The lean solution outlet of poor rich liquid heat exchanger 3 is joined with the lean solution inlet of lean solution heat exchanger 8; The lean solution outlet of lean solution heat exchanger 8 communicates with the lean solution inlet of lean solution water cooling heat exchanger 19; The lean solution outlet of lean solution water cooling heat exchanger 19 links to each other with the lean solution inlet on absorption tower 1; The outlet of regenerator 4 regeneration gases is joined with regeneration gas cooler 5 regeneration gases inlet; The regeneration gas outlet of regeneration gas cooler 5 communicates with the regeneration gas inlet of regeneration gas water-cooled cooler 20; The regeneration gas outlet of regeneration gas water-cooled cooler 20 communicates with the gas access of gas-liquid separator 6;
In the described power plant cooling water subsystem, solution moisture removing device 11 air outlet slits link to each other with air water cooler 21 air intlets, and air water cooler 21 air outlet slits and cooling tower 18 air intakes join.
The utility model utilizes the weak solution after the solution dehumidification system dehumidifying to pass through heat exchanger elder generation and the lower lean solution heat exchange of temperature, and higher with temperature then regeneration gas heat exchange makes weak solution obtain regeneration; And the low water capacity air after solution dehumidification system handled is sent into power plant's cooling tower; Improve cooling effectiveness, reduce condenser cooling inflow temperature, improve generating set efficient; Make the heat of taking away through cooling water originally obtain utilizing, reduced energy loss.
Having CO 2Be provided with a cover solution dehumidification subsystem in the power plant of capturing device, with the same CO of power plant cooling water subsystem 2The capture subsystem integrates: principal character is to send into the air intake of cooling tower 18 the solution dehumidification subsystem dehumidifies air in solution moisture removing device 11 after; Strengthen the heat and mass transfer process in the cooling tower; Improve the efficient of cooling tower, reduce condenser recirculated water inflow temperature;
The outlet weak solution of solution moisture removing device 11 is earlier in the lower lean solution heat exchange of lean solution heat exchanger 8 neutral temperatures simultaneously; The regeneration gas heat exchange higher in regeneration gas cooler 5 again with temperature; Make weak solution obtain regeneration, the weak solution after the regeneration is used to reduce the water capacity of cooling tower 18 inlet airs.
Lean solution water cooling heat exchanger 19 is used for lean solution heat exchanger 8 outlet lean solutions are cooled to absorption temperature, and regeneration gas water-cooled cooler 20 is used for that regeneration gas cooler 5 outlet regeneration gases are cooled to the suction port of compressor and requires temperature.
Every relating to reclaimed the CO of power plant 2Trapping system lean solution heat and regeneration gas heat; The heat that this is partially recycled is used for the weak solution regeneration of solution dehumidification system; And the air after the solution dehumidification system dehumidifying is sent into power plant's cooling tower; Strengthen the system of cooling tower heat and mass effect, comprise and use follow-on solution dehumidification system or follow-on CO 2Trapping system is as long as principle is consistent, all within the claim scope.
Referring to Fig. 1; In the solution dehumidification subsystem; The outlet of blower fan 10 links to each other with the blast entrance of solution moisture removing device 11 through airduct, and the air intake of the air outlet slit of dehumidifier 11 and air water cooler 21 joins, and the air outlet slit of air water cooler 21 communicates with power plant cooling tower 18 air intakes; Weak solution pump 12 inlets join with the outlet of dehumidifier 11 weak solutions, and outlet links to each other with the weak solution inlet of concentrated solution weak solution heat exchanger 17; The weak solution outlet of concentrated solution weak solution heat exchanger 17 communicates with the weak solution inlet of lean solution heat exchanger 8; The weak solution outlet of lean solution heat exchanger 8 links to each other with the weak solution inlet of regeneration gas cooler 5; The weak solution outlet of regeneration gas cooler 5 communicates with the weak solution inlet of solution regenerator 15; The concentrated solution outlet of solution regenerator 15 links to each other with the import of concentrated solution pump 14; The concentrated solution inlet of the outlet of concentrated solution pump 14 and concentrated solution weak solution heat exchanger 17 joins; The concentrated solution outlet of concentrated solution weak solution heat exchanger 17 links to each other with the concentrated solution inlet of water cooling heat exchanger 13; The concentrated solution outlet of water cooling heat exchanger 13 is connected with the concentrated solution inlet of solution moisture removing device 11; The outlet of blower fan 16 links to each other with the blast entrance of solution regenerator 15.
At CO 2Capture in the subsystem, flue gas links to each other with the absorption tower gas feed; Absorption tower 1 rich solution outlet is joined with rich solution pump 2; 2 outlets of rich solution pump communicate with the rich solution inlet of poor rich liquid heat exchanger 3; The outlet of poor rich liquid heat exchanger 3 rich solutions links to each other with regenerator 4 rich solutions inlet; The outlet of regenerator 4 lean solutions communicates with lean pump 7 inlets; Lean pump 7 outlets link to each other with the lean solution inlet of poor rich liquid heat exchanger 3; The lean solution outlet of poor rich liquid heat exchanger 3 is joined with the lean solution inlet of lean solution heat exchanger 8; The lean solution outlet of lean solution heat exchanger 8 communicates with the lean solution inlet of lean solution water cooling heat exchanger 19; The lean solution outlet of lean solution water-cooled heat exchange 19 links to each other with the lean solution inlet on absorption tower 1; The outlet of regenerator 4 regeneration gases is joined with regeneration gas cooler 5 regeneration gases inlet; The regeneration gas outlet of regeneration gas cooler 5 communicates with the regeneration gas inlet of regeneration gas water-cooled cooler 20; The regeneration gas outlet of regeneration gas water-cooled cooler 20 communicates with the gas access of gas-liquid separator 6.
In the power plant cooling water subsystem, solution moisture removing device 11 air outlet slits link to each other with the empty 18 gas inlet of cooling tower after reducing to room temperature through air water cooler 21, and the air after the dehumidifying is sent into cooling tower 18 through pipeline.
The above is merely the preferred embodiments of the utility model; The protection domain of the utility model does not exceed with above-mentioned embodiment; As long as the equivalence that those of ordinary skills do according to the utility model institute disclosure is modified or changed, all should include in the protection domain of putting down in writing in claims.

Claims (1)

1. one kind is reduced the device that the air water capacity improves the cooling tower cooling effect, it is characterized in that: it comprises power plant cooling water subsystem, CO 2Capture subsystem, with power plant's cooling subsystem and CO 2Capture the solution dehumidification subsystem that subsystem combines;
The power plant cooling water subsystem comprises cooling tower (18);
CO 2Capture subsystem and comprise absorption tower (1), rich solution pump (2), poor rich liquid heat exchanger (3), regenerator (4), regeneration gas cooler (5), gas-liquid separator (6), lean pump (7), lean solution heat exchanger (8), reboiler (9), lean solution water cooling heat exchanger (19) and regeneration gas water-cooled cooler (20);
The solution dehumidification subsystem comprises dehumidifier inlet blower fan (10), solution moisture removing device (11), weak solution pump (12), water cooling heat exchanger (13), concentrated solution pump (14), solution regenerator (15), regenerator inlet blower fan (16), concentrated solution weak solution heat exchanger (17) and air water cooler (21);
In the described solution dehumidification subsystem; The outlet of dehumidifier inlet blower fan (10) links to each other with the blast entrance of solution moisture removing device (11) through airduct; The air intake of the air outlet slit of solution moisture removing device (11) and air water cooler (21) joins, and the air outlet slit of air water cooler (21) communicates with cooling tower (18) air intake; Weak solution pump (12) inlet joins with the outlet of solution moisture removing device (11) weak solution, and weak solution pump (12) outlet links to each other with the weak solution inlet of concentrated solution weak solution heat exchanger (17); The weak solution outlet of concentrated solution weak solution heat exchanger (17) communicates with the weak solution inlet of lean solution heat exchanger (8); The weak solution outlet of lean solution heat exchanger (8) links to each other with the weak solution inlet of regeneration gas cooler (5); The weak solution outlet of regeneration gas cooler (5) communicates with the weak solution inlet of solution regenerator (15); The concentrated solution outlet of solution regenerator (15) links to each other with the import of concentrated solution pump (14); The concentrated solution inlet of the outlet of concentrated solution pump (14) and concentrated solution weak solution heat exchanger (17) joins; The concentrated solution outlet of concentrated solution weak solution heat exchanger (17) links to each other with the concentrated solution inlet of water cooling heat exchanger (13); The concentrated solution outlet of water cooling heat exchanger (13) is connected with the concentrated solution inlet of solution moisture removing device (11); The outlet of regenerator inlet blower fan (16) links to each other with the blast entrance of solution regenerator (15);
Described CO 2Capture in the subsystem, flue gas gets into absorption tower (1) gas feed; Absorption tower (1) rich solution outlet is joined with rich solution pump (2); Rich solution pump (2) outlet communicates with the rich solution inlet of poor rich liquid heat exchanger (3); The outlet of poor rich liquid heat exchanger (3) rich solution links to each other with regenerator (4) rich solution inlet; The outlet of regenerator (4) lean solution communicates with lean pump (7) inlet; Lean pump (7) outlet links to each other with the lean solution inlet of poor rich liquid heat exchanger (3); The lean solution outlet of poor rich liquid heat exchanger (3) is joined with the lean solution inlet of lean solution heat exchanger (8); The lean solution outlet of lean solution heat exchanger (8) communicates with the lean solution inlet of lean solution water cooling heat exchanger (19); The lean solution outlet of lean solution water cooling heat exchanger (19) links to each other with the lean solution inlet of absorption tower (1); The outlet of regenerator (4) regeneration gas is joined with regeneration gas cooler (5) regeneration gas inlet; The regeneration gas outlet of regeneration gas cooler (5) communicates with the regeneration gas inlet of regeneration gas water-cooled cooler (20); The regeneration gas outlet of regeneration gas water-cooled cooler (20) communicates with the gas access of gas-liquid separator (6);
In the described power plant cooling water subsystem, solution moisture removing device (11) air outlet slit links to each other with air water cooler (21) air intlet, and air water cooler (21) air outlet slit and cooling tower (18) air intake join.
CN2011205252246U 2011-12-15 2011-12-15 Device for improving cooling effect of cooling tower by means of reducing air moisture Expired - Fee Related CN202393293U (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102519299A (en) * 2011-12-15 2012-06-27 东南大学 System capable of improving cooling effect of cooling tower by means of reducing moisture content of air
US9021810B2 (en) * 2012-01-27 2015-05-05 The University Of Kentucky Research Foundation Fossil-fuel-fired power plant
CN110701922A (en) * 2019-10-22 2020-01-17 常州和余环保科技有限公司 Mechanical ventilation cooling tower
CN114923233A (en) * 2022-04-01 2022-08-19 东南大学 Light stimulation response ionic liquid dehumidification air conditioning system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102519299A (en) * 2011-12-15 2012-06-27 东南大学 System capable of improving cooling effect of cooling tower by means of reducing moisture content of air
CN102519299B (en) * 2011-12-15 2013-05-01 东南大学 System capable of improving cooling effect of cooling tower by means of reducing moisture content of air
US9021810B2 (en) * 2012-01-27 2015-05-05 The University Of Kentucky Research Foundation Fossil-fuel-fired power plant
CN110701922A (en) * 2019-10-22 2020-01-17 常州和余环保科技有限公司 Mechanical ventilation cooling tower
CN114923233A (en) * 2022-04-01 2022-08-19 东南大学 Light stimulation response ionic liquid dehumidification air conditioning system
CN114923233B (en) * 2022-04-01 2023-10-24 东南大学 Light stimulus response ionic liquid dehumidification air conditioning system

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