CN1693778A - Heat recovery type fresh air treatment system of using hygroscopic solution as circulating working medium - Google Patents
Heat recovery type fresh air treatment system of using hygroscopic solution as circulating working medium Download PDFInfo
- Publication number
- CN1693778A CN1693778A CN 200510011826 CN200510011826A CN1693778A CN 1693778 A CN1693778 A CN 1693778A CN 200510011826 CN200510011826 CN 200510011826 CN 200510011826 A CN200510011826 A CN 200510011826A CN 1693778 A CN1693778 A CN 1693778A
- Authority
- CN
- China
- Prior art keywords
- solution
- module
- gas
- liquid
- direct contact
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000011084 recovery Methods 0.000 title claims description 17
- 239000007788 liquid Substances 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000007921 spray Substances 0.000 claims abstract description 8
- 230000004087 circulation Effects 0.000 claims description 5
- 239000012530 fluid Substances 0.000 claims description 5
- 230000001839 systemic circulation Effects 0.000 claims description 5
- 238000000034 method Methods 0.000 abstract description 7
- 238000005516 engineering process Methods 0.000 abstract description 3
- 239000000428 dust Substances 0.000 abstract description 2
- 230000001954 sterilising effect Effects 0.000 abstract description 2
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 2
- 238000010792 warming Methods 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 10
- 238000007791 dehumidification Methods 0.000 description 6
- 238000005265 energy consumption Methods 0.000 description 4
- 239000000945 filler Substances 0.000 description 4
- 238000005057 refrigeration Methods 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000009938 salting Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Landscapes
- Central Air Conditioning (AREA)
- Drying Of Gases (AREA)
Abstract
The invention relates to a warming air condition used heat recycle new type wind process system that belongs to energy source technology field. The system contains heat recycle device and temperature adjustable unit spray module. The heat recycle device is made up of gas-liquid directly contact module, board type heat exchanger, solution self-circulating pump, system circulating pump and water compensation valve. The unit spray module is made up of board type heat exchange, gas-liquid directly contact module, and solution self-circulating pump. The system uses solution that has hygroscopic feature as working medium. It could adopt hot water as the driving energy source. It has the function of sterilization, dust separation, and purifying air.
Description
Technical field
The present invention relates to the hygroscopic solution that utilizes that a kind of HVAC uses is the heat recovery type fresh air treatment system of cycle fluid, belongs to energy technology field.
Background technology
New wind is having incomparable advantage aspect removal indoor pollution material, the raising indoor air quality, but the increase of resh air requirement can make that handling energy consumption increases considerably, and how reducing the novel wind energy consumption, to improve indoor air quality simultaneously be the major issue that air conditioner industry faces.Adopt the recuperation of heat mode, the energy that reclaims indoor exhaust wind is to reduce the effective measures that new wind is handled energy consumption.
New blower fan group need realize the cool-down dehumidification process of summer to new wind, and winter is to the warming and humidifying processing procedure of new wind.At present, the dehumidification by condensation method is adopted in dehumidifying in the conventional new blower fan, promptly uses 7 ℃ chilled water by surface cooler the temperature of air to be reduced to the moisture that freeze-outs below the dew point, thereby plays the effect of dehumidifying.The problem of being brought is: refrigeration machine is operated under the low evaporating temperature situation, causes the refrigeration machine coefficient of performance lower; Temperature is low excessively though the air humidity behind the dehumidification by condensation meets the demands, thereby also needs heat to cause the waste of the energy sometimes again; Coil pipe that condensate water is arranged etc. grows mould, contaminated air easily.The humidification function in winter also needs other humidification apparatus to realize.
Because hygroscopic solution obtains everybody concern gradually in the superiority of removing on the indoor latent heat load.Liquid desiccant air conditioning is compared with conventional air-conditioning, saves a large amount of electric energy thereby can adopt low-temperature heat source to drive; Can remove airborne dust, bacterium, mould and some other nuisances by the sprinkling of solution; Avoid using the coil pipe of condensate water, can obviously improve indoor air quality.
Summary of the invention
The purpose of this invention is to provide a kind of heat recovery type fresh air treatment system that utilizes hygroscopic solution for cycle fluid.
The present invention proposes utilizes the heat recovery type fresh air treatment system of hygroscopic solution for cycle fluid, it is characterized in that, but described fresh air treatment system contains the unit spray module of heat reclamation device and temperature adjustment; Described heat reclamation device is made up of the direct contact modules of gas-liquid (1), plate type heat exchanger (2), solution self-circulating pump (3), systemic circulation pump (4), water compensating valve (5); But the unit spray module of described temperature adjustment is made up of plate type heat exchanger (2), the direct contact modules G of gas-liquid, solution self-circulating pump (3); Described fresh air treatment system is divided into upper and lower two-layer passage, and the upper strata passage is the return air treatment channel, and lower floor is new wind treatment channel; Described upper strata passage is made up of the direct contact modules A of gas-liquid, C, E, and lower floor's passage is made up of the direct contact modules B of gas-liquid, D, F, G; The direct contact modules A of described gas-liquid, B, C, D, E, F and corresponding plate type heat exchanger (2) are formed three grades of heat recovery systems, utilize summer the transpiration-cooled cold of air draft to reduce the solution temperature that enters module B, D, E, be circulation solution in six modules winter, become solution full heat recovery device, directly reclaim the heat and the wet amount of air draft; Through the new wind of heat recovery system, after the further processing of module G, send into air-conditioned room; Described plate type heat exchanger (2) carries out exchange heat with the solution that enters the direct contact modules G of gas-liquid, enters the solution temperature of this module in order to adjusting.
The course of work of this fresh air processor group is as follows:
In heat recovery system, six solution self-circulating pumps flow of the spray solution of control module A～F inside is respectively arranged, there is a systemic circulation pump to be controlled at circulation solution flow between modules A～F.In each module, solution is under the driving of self-circulating pump 3, flow into plate type heat exchanger 2 from module bottom, flow down through liquid distributor then and soak filler, solution carries out the exchange of heat and quality with new wind (or return air) in filler, last solution is got back in the bottom liquid bath of module, finishes cyclic process.In summer, directly the water spray evaporative cooling effect that utilizes moisture passes to the solution of opposite side with cold by plate type heat exchanger 2 in modules A, C, E, enters the solution temperature of module B, D, F liquid distributor with reduction, thereby improves its dehumidifying effect; Hygroscopic solution directly contacts with new wind in module B, D, F, new wind is by cool-down dehumidification, have between module B, D, the F with the solution of new wind counter-current flow taking away the moisture that from air, absorbs, the solution concentration that intermodule flows constantly reduces to be needed to concentrate regeneration and just can reuse.In summer, utilize the evaporative cooling effect of air draft like this, realized the abundant recovery of air draft cold.Winter, what circulate in modules A～F is hygroscopic solution, extracts solution by the effect of self-circulating pump 3 from module bottom, through entering the liquid distributor of module after the plate type heat exchanger temperature adjustment, solution spraying and soak into down filler, and carry out with the incoming flow air that heat is wet to be exchanged.The exchange of sensible heat (temperature) is to be that the plate type heat exchanger that media passes through (A and B, C and D, E and F) in the respective stages carries out with solution between new wind and the air draft, and the exchange of moisture (humidity) is the solution concentration variation realization of flowing between modules A～F under 4 effects of systemic circulation pump.So in the winter time, be circulation vector with solution, by the solution that plate type heat exchanger in the level and inter-stage circulate, realized the full recuperation of heat of air draft heat and moisture, new wind is heated humidification in this process.
Through the new wind after heat reclamation device (module B, D, F), need be in module G further processing just can reach the requirement of air supply parameter.In summer, what flow in the corresponding plate type heat exchanger 2 of module G is 15～18 ℃ cold water.The extraneous concentrated solution that flows into flow through in turn module G, F, D, B, opposite with new wind flow direction, constantly reduce along the concentration of journey solution.The weak solution that flows out from module B need concentrate regeneration and just can reuse, and the hot water that can adopt 60～70 ℃ is as the regeneration thermal source.Solution among the module G the effect of solution pump 3 dirty go into board-like heat exchanger 2 by cooling after, behind the liquid distributor at module top, soak into filler again, and carry out the exchange of heat and quality with new wind.In this process, the reduction that act as of cold water enters the solution temperature of module G liquid distributor, thereby improves its dehumidifying effect; No longer be in order to dehumidify, thus the supply water temperature of cold water can be under the conventional dehumidification by condensation situation about 7 ℃ bring up to 15～18 ℃.The cold water of this temperature provides condition for the use of natural cold sources such as underground water, even adopt the mechanical refrigeration mode, the coefficient of performance of refrigeration machine also is improved largely.In module G, new wind is further sent into air-conditioned room after the cool-down dehumidification processing.In winter, what flow in the corresponding plate type heat exchanger 2 of module G is hot water about 40 ℃, thereby acting as of hot water improves the solution temperature that enters module G liquid distributor and improve its humidification ability.In module G, new wind is further heated humidification, and solution is concentrated, and opens water compensating valve 5 amount of makeup water to keep the concentration of solution among the module G.
The solution that this new blower fan group system utilization has moisture pick-up properties is working media, utilize the transpiration-cooled energy of air draft summer, directly carry out full recuperation of heat to air draft winter, reduces greatly thereby make new wind handle energy consumption, can adopt low grade heat energy such as hot water as drive energy.Salting liquid has sterilization, dedusting effect, can purify air, improve indoor air quality.
Description of drawings
Fig. 1 is fresh air processor group work structuring in a summer schematic diagram of the present invention.
Fig. 2 is a fresh air processor unit in winter work structuring schematic diagram of the present invention.
The specific embodiment
The present invention will be further described below in conjunction with accompanying drawing:
Referring to Fig. 1 and Fig. 2, this fresh air processor comprises: parts such as the direct contact modules 1 of gas-liquid, plate type heat exchanger 2, solution self-circulating pump 3, systemic circulation pump 4, water compensating valve 5.This new blower fan is divided into upper and lower two-layer passage, and the upper strata passage is the return air treatment channel, and lower floor is new wind treatment channel.The upper strata passage is made up of the direct contact modules A of gas-liquid, C, E, and lower floor's passage is made up of the direct contact modules B of gas-liquid, D, F, G.The direct contact modules A of gas-liquid, B, C, D, E, F and corresponding plate type heat exchanger 2 are formed three grades of heat recovery systems, and summer, (see figure 1) utilized the transpiration-cooled cold reduction of air draft to enter the solution temperature of module B, D, E, thereby improved its dehumidifying effect; Be circulation solution in six modules of (see figure 2) in winter, become solution full heat recovery device, directly reclaim the heat and the wet amount of air draft.Through the new wind of heat recovery system, after the further processing of module G, send into air-conditioned room.There are plate type heat exchanger 2 and the solution that enters the direct contact modules G of gas-liquid to carry out exchange heat, enter the solution temperature of this module in order to adjusting, thereby strengthen its dehumidifying (or humidification) ability.
Claims (1)
1, utilize the heat recovery type fresh air treatment system of hygroscopic solution, it is characterized in that, but described fresh air treatment system contains the unit spray module of heat reclamation device and temperature adjustment for cycle fluid; Described heat reclamation device is made up of the direct contact modules of gas-liquid (1), plate type heat exchanger (2), solution self-circulating pump (3), systemic circulation pump (4), water compensating valve (5); But the unit spray module of described temperature adjustment is made up of plate type heat exchanger (2), the direct contact modules G of gas-liquid, solution self-circulating pump (3); Described fresh air treatment system is divided into upper and lower two-layer passage, and the upper strata passage is the return air treatment channel, and lower floor is new wind treatment channel; Described upper strata passage is made up of the direct contact modules A of gas-liquid, C, E, and lower floor's passage is made up of the direct contact modules B of gas-liquid, D, F, G; The direct contact modules A of described gas-liquid, B, C, D, E, F and corresponding plate type heat exchanger (2) are formed three grades of heat recovery systems, utilize summer the transpiration-cooled cold of air draft to reduce the solution temperature that enters module B, D, E, be circulation solution in six modules winter, become solution full heat recovery device, directly reclaim the heat and the wet amount of air draft; Through the new wind of heat recovery system, after the further processing of module G, send into air-conditioned room; Described plate type heat exchanger (2) carries out exchange heat with the solution that enters the direct contact modules G of gas-liquid, enters the solution temperature of this module in order to adjusting.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100118269A CN100439805C (en) | 2005-05-31 | 2005-05-31 | Heat recovery type fresh air treatment system of using hygroscopic solution as circulating working medium |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100118269A CN100439805C (en) | 2005-05-31 | 2005-05-31 | Heat recovery type fresh air treatment system of using hygroscopic solution as circulating working medium |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1693778A true CN1693778A (en) | 2005-11-09 |
| CN100439805C CN100439805C (en) | 2008-12-03 |
Family
ID=35352855
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100118269A Expired - Fee Related CN100439805C (en) | 2005-05-31 | 2005-05-31 | Heat recovery type fresh air treatment system of using hygroscopic solution as circulating working medium |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100439805C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100427841C (en) * | 2006-06-15 | 2008-10-22 | 清华大学 | Whole-thermal reclaiming type thermal-drive solution ventilation processor set by using evaporative cooling of return air |
| CN104456875A (en) * | 2014-11-18 | 2015-03-25 | 东南大学 | Fresh air treatment device for indirect evaporative cooling return air total heat recovery |
| CN105737302A (en) * | 2016-02-26 | 2016-07-06 | 无锡市天兴净化空调设备有限公司 | Central air-conditioning based on dry air energy |
| CN107388430A (en) * | 2017-09-01 | 2017-11-24 | 江苏紫东建筑科技股份有限公司 | A kind of solar energy evacuated liquid desiccant air conditioning and its method of work |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002054838A (en) * | 2000-08-10 | 2002-02-20 | Seibu Giken Co Ltd | Dehumidifying air conditioning apparatus |
| JP4015351B2 (en) * | 2000-08-25 | 2007-11-28 | 三機工業株式会社 | Total heat exchanger |
| CN1231723C (en) * | 2003-04-30 | 2005-12-14 | 清华大学 | Complete heat exchange method by using solvent as medium and apparatus thereof |
| CN1220007C (en) * | 2003-05-08 | 2005-09-21 | 清华大学 | Fresh air air-conditioner with solution heat recoverer |
| CN2811816Y (en) * | 2005-05-31 | 2006-08-30 | 清华大学 | Heat recovery type fresh air processing unit utilizing moisture absorption solution as circulating medium |
-
2005
- 2005-05-31 CN CNB2005100118269A patent/CN100439805C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100427841C (en) * | 2006-06-15 | 2008-10-22 | 清华大学 | Whole-thermal reclaiming type thermal-drive solution ventilation processor set by using evaporative cooling of return air |
| CN104456875A (en) * | 2014-11-18 | 2015-03-25 | 东南大学 | Fresh air treatment device for indirect evaporative cooling return air total heat recovery |
| CN104456875B (en) * | 2014-11-18 | 2017-05-31 | 东南大学 | A kind of Fresh air handing device of indirect evaporating-cooling return air total heat recovery |
| CN105737302A (en) * | 2016-02-26 | 2016-07-06 | 无锡市天兴净化空调设备有限公司 | Central air-conditioning based on dry air energy |
| CN107388430A (en) * | 2017-09-01 | 2017-11-24 | 江苏紫东建筑科技股份有限公司 | A kind of solar energy evacuated liquid desiccant air conditioning and its method of work |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100439805C (en) | 2008-12-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100404967C (en) | Air treater set with moisture-absorbing solution as circulation work medium and driven by hot pump | |
| CN100494793C (en) | Two-stage rotating wheel dehumidification air conditioner device capable of using low-grade heat source | |
| CN101876469B (en) | Heat pump coupling contraflow type liquid-desiccant central ventilation system and control method thereof | |
| CN100510558C (en) | Single runner two stage dehumidify air-conditioner driven by solar | |
| CN206055832U (en) | The solar energy solution dehumidification system of unit is cooled down for double flash evaporation | |
| CN201582927U (en) | Coupling counterflow-type solution dehumidification fresh air system of heat pump | |
| CN101701738B (en) | Fresh air handling unit for regulating humidity and controlling temperature by adopting solution and control method thereof | |
| CN1862121A (en) | Temp and moisture independent control type air-conditioning system using solution as auxiliary working substance | |
| CN1862123A (en) | Multi-stage solution dehumidifying and regenerating fresh air set driven by heat pump | |
| CN106907809B (en) | Air conditioning system combining hollow fiber membrane liquid dehumidification and evaporative cooling | |
| CN202719696U (en) | Dehumidification and regeneration type air treating machine set with rotating wheel driven by heat pump | |
| CN2896090Y (en) | Multi-stage solution dehumidifying and fresh-air regenerating device driven by heat pump | |
| CN104676782B (en) | A kind of solution humidifying air processor of multistage distributary | |
| CN102519096A (en) | Heat pump type total heat recovering fresh air treating machine | |
| CN101294755A (en) | Air-conditioning unit with constant temperature and humidity | |
| CN100417865C (en) | Thermal-drive solution ventilation processor set by using cooling water as cooling source | |
| CN104235973B (en) | Rotating wheel energy recovery type solution dehumidification air-conditioning system | |
| CN2811816Y (en) | Heat recovery type fresh air processing unit utilizing moisture absorption solution as circulating medium | |
| CN102563770A (en) | Fresh air handling unit with integrated functions of dehumidification and evaporative cooling and air treatment method of fresh air handling unit | |
| CN104456875A (en) | Fresh air treatment device for indirect evaporative cooling return air total heat recovery | |
| CN1916512A (en) | Air condition system by using latent energy of exhaustion to retrieve liquid and extract moisture | |
| CN106765685A (en) | A kind of heat pump driven indirect evaporating-cooling return air full heat recovery fresh air processing unit | |
| CN100439805C (en) | Heat recovery type fresh air treatment system of using hygroscopic solution as circulating working medium | |
| CN202494181U (en) | Double-effect heat pump type total heat recovery and fresh air processor | |
| CN201582926U (en) | Solution moisture-temperature control fresh air air-conditioning unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081203 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |