CN202452608U - Solution-humidity-regulating all-air unit with total-heat recovery device - Google Patents
Solution-humidity-regulating all-air unit with total-heat recovery device Download PDFInfo
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- CN202452608U CN202452608U CN2012200423267U CN201220042326U CN202452608U CN 202452608 U CN202452608 U CN 202452608U CN 2012200423267 U CN2012200423267 U CN 2012200423267U CN 201220042326 U CN201220042326 U CN 201220042326U CN 202452608 U CN202452608 U CN 202452608U
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Abstract
The utility model provides a solution-humidity-regulating all-air unit with a total-heat recovery device. The solution-humidity-regulating all-air unit comprises a solution total-heat recovery module, a plurality of solution-humidity-regulating modules, a plurality of solution regenerating modules, a surface cooler, an air-returning duct, a fresh air duct, a plurality of first heat exchangers and a plurality of second heat exchangers, wherein humidity regulating solutions inside the solution total-heat recovery module, the plurality of solution-humidity-regulating modules and the plurality of solution regenerating modules form up-down solution cycle and are in contact with gas, the air-returning duct penetrates through the upper portion of the total-heat recovery module and the solution regenerating modules sequentially and is communicated with an exterior of a room, the fresh air duct penetrates through the lower portion of the total-heat recovery module, the solution-humidity-regulating modules and the surface cooler sequentially and is communicated with an interior of the room, the first heat exchangers are connected with all the solution-humidity-regulating modules, the second heat exchangers are connected with all the solution regenerating modules, the first heat exchangers and the second heat exchangers are connected through compressors and expansion valves respectively and form a refrigerant cycle, and bottoms of the solution-humidity-regulating modules are in communication with bottoms of the solution regenerating modules so as to form a solution regenerating cycle. The all-air unit has the advantages that solution humidity regulation is performed through gas-liquid total-heat exchange modules and the problem that the temperate after dehumidification is low is solved.
Description
Technical field
The utility model relates to the air processor field, the full air unit of particularly a kind of solution damping with full heat recovery device.
Background technology
For large space places such as megastore, supermarket, meeting room, auditorium, gymnasium, adopt centralized all-air system usually.Traditional full air unit, generally be with indoor return air with after new wind mixes, through the surface cooler cool-down dehumidification with realization to indoor Temperature and Humidity Control.
The full air unit that is applied to field of air conditioning at present generally adopts the mode of dehumidification by condensation, utilizes refrigeration unit to produce low-temperature cold water, to dew point, makes the water in air steam be condensed into aqueous water air freezing, thereby realizes dehumidifying.There is following problem in this kind air-treatment mode: the refrigeration unit evaporating temperature is low, and refrigerating efficiency is low; Air themperature is too low behind the dehumidification by condensation, needs heat just can reach the wind pushing temperature requirement sometimes again, causes cold-hot counteraction, energy waste; There is condensate in the surface cooler coil pipe, is prone to breed bacteria.
The utility model content
The utility model provides a kind of solution damping with full heat recovery device full air unit, improves refrigerating efficiency, prevents the energy waste that cold-hot counteraction brings, and avoids the surface cooler coil temperature to cross the low problem that produces condensate.
The utility model is realized through following technical scheme: the full air unit of a kind of solution damping with full heat recovery device; Comprise: the full heat recovery module of solution, solution damping module and solution regeneration module; Inner hygroscopic solution all forms solution and circulates up and down, contacts with gas; Surface cooler; Return airway, order pass behind top and the solution regeneration module of full heat recovery module outside the communication chamber; New wind air channel, order are passed behind bottom, solution damping module and the surface cooler of full heat recovery module in the communication chamber; First heat exchanger connects each solution damping module, makes hygroscopic solution in the solution damping module first heat exchanger of flowing through form solution and circulate up and down; Second heat exchanger connects each solution regeneration module, makes hygroscopic solution in the solution regeneration module second heat exchanger of flowing through form said solution and circulate up and down; Wherein, first heat exchanger is connected with expansion valve through compressor respectively with second heat exchanger and forms refrigerant circulation; The bottom of solution damping module is communicated with the bottom of solution regeneration module, forms the solution regeneration cycle.
Further; Solution damping module and solution regeneration module all are provided with a plurality of; Return airway is in proper order through a plurality of solution regeneration modules, and new wind air channel is in proper order through a plurality of solution damping modules, each solution damping module all with corresponding a connection of solution regeneration module.
Further, first heat exchanger and second heat exchanger are provided with a plurality of.
Further, the full heat recovery module of solution, solution damping module and solution regeneration module are equipped with the solution water circulating pump and form solution and circulate up and down.
Further, in the bottom of solution damping module and the pipeline that the bottom of solution regeneration module is communicated with heat exchanger plates being installed changes.
Further, new wind air channel is being provided with the pipeline that mixes with return air before through surface cooler.
Further, the solution regeneration module is provided with water pipe and the interior solution cavity of solution regeneration module that water compensating valve is communicated with the external world.
Further, first heat exchanger and second heat exchanger are connected with an expansion valve through a compressor jointly and form circulation.
Further; First heat exchanger and second heat exchanger have a plurality of respectively; Compressor and expansion valve have a plurality of accordingly respectively, and each first heat exchanger is connected with an expansion valve through a corresponding compressor respectively with each second heat exchanger and forms separately independently circulation.
Through technique scheme, the major advantage of the utility model is, carries out the solution damping through the full heat exchange module of gas-liquid is set, and improves dehumidification rate, do not need air cooling-down to dew point is dehumidified, and avoided the low excessively problem of bringing of dehumidifying back air themperature.
Description of drawings
The accompanying drawing that constitutes the part of the utility model is used to provide the further understanding to the utility model, and illustrative examples of the utility model and explanation thereof are used to explain the utility model, do not constitute the improper qualification to the utility model.In the accompanying drawings:
Fig. 1 shows the annexation sketch map of solution damping unit of first embodiment of the utility model;
Fig. 2 shows the annexation sketch map of solution damping unit of second embodiment of the utility model.
The specific embodiment
Embodiment to the utility model is elaborated below in conjunction with accompanying drawing, but the multitude of different ways that the utility model can be defined by the claims and cover is implemented.
The solution damping unit of an embodiment of the utility model has been shown among Fig. 1.This unit has made full use of the characteristic of solution efficient absorbent, in conjunction with multi-stage solution damping/regeneration unit, solution-type full heat recovery device, high temperature cold water coil pipe, realizes the cool-down dehumidification process to air.
Concrete air-treatment flow process is following:
In summer, return air at first carries out full recuperation of heat through the solution-type full heat recovery device with new wind.New wind after the full recuperation of heat gets in the unit lower floor damping module, contact with the concentrated solution that is evaporated the device cooling and realizes dehumidifying, mixes with another strand return air then, delivers to indoor after the process surface cooler is lowered the temperature by high temperature cold water.In the damping module solution absorption moisture thinning after, then send into the upper strata regeneration module, after the device that the is condensed heating, and contact through the return air after the recuperation of heat, moisture is discharged to realize concentrating regenerates.Damping that structure is identical and regeneration module series connection, the processing procedure of damping of promptly feasible formation multi-stage solution and regeneration.
The principle and the summer of unit winter operation are similar, and difference is through the cross valve switching refrigerant flow direction and summer condition to be moved on the contrary, make the condenser in summer switch to evaporimeter, and the evaporimeter in summer switches to condenser; Feed hot water in the surface cooler and convert heater into.New wind, mixes with return air again by the solution warming and humidifying earlier through full recuperation of heat then, and is indoor through sending into after the coil pipe heating.
This unit can satisfy the air-treatment requirement in places such as megastore, supermarket, meeting room, auditorium, gymnasium to the all-air system design.
Solution damping unit with damping of two-stage solution and regeneration is an example, and the schematic diagram of its summer operation is as shown in Figure 1.Its critical piece comprises that (comprise full heat exchange module 1, solution regeneration module B, C and solution damping module E, F, surface cooler 2, compressor 3, left condenser 4, right condenser 5, left evaporimeter 6, right evaporimeter 7, left heat exchanger plates change 8 to the gas-liquid contact modules, right heat exchanger plates changes 9, each full heat exchange module is furnished with solution water circulating pump 10, expansion valve 11, left water compensating valve 12 and right water compensating valve 13.The process gas-liquid directly contacts full heat exchange module A to return air respectively, D carries out full recuperation of heat with new wind, and solution successively directly contacts with return air with new wind through the conveying from the bottom to top of water pump.Through the return air after the recuperation of heat successively with upper solution regeneration module B, C in after the higher weak solution heat exchange and absorbent solution moisture of temperature, after be discharged to outdoor; Pretreated new wind then gets among the solution damping module E of lower floor, the F, after temperature lower concentrated solution heat exchange and dehumidifying, mixes with another strand return air, and is indoor through delivering to after surface cooler 2 coolings.
Wherein, damping module E and regeneration module C, F and B correspond to one group respectively.Left heat exchanger plates is set between the higher concentrated solution of the temperature that flows out from module C and the lower weak solution of the temperature that flows out from module E changes 8 and reclaim heats, the solution that circulates between module B and the F uses right heat exchanger plates to change 9 recovery heats.After the weak solution of module F outlet and the solution in the module B bottom solution groove were mixed, with the high temperature refrigeration working medium heat exchange of flowing out from compressor 3 in the right condenser 5, solution was heated the back and delivers to the regeneration of module top spray by solution water circulating pump 10; Concentration raises after emitting moisture; Concentrated solution after the regeneration flows back to damping module F, with the solution of F bottom solution groove mixed after, again with right evaporimeter 7 in the cryogenic refrigeration working medium heat exchange of flowing out from expansion valve 11; After being cooled, solution delivers to the dehumidifying of module top spray by solution circulation pump 10; Solution concentration is thinning after absorbing airborne moisture, delivers among the regeneration module B to concentrate, so circulation again.Operation principle between module C, the E and module B, F are identical.Left side water compensating valve 12 is used for the solution concentration of control module C, and right water compensating valve 13 is used for the solution concentration of control module B.The new wind processing section of unit utilizes the evaporimeter of heat pump that the dehumidifying concentrated solution is cooled off on the one hand, to strengthen the latent heat that discharges in solution dehumidification ability and the absorption dehumidifying process; The condenser that utilizes heat pump on the other hand heats the regeneration weak solution, again with full recuperation of heat after return air carry out full heat exchange, solution is promptly concentrated regeneration.Referring to Fig. 1, mark the circulating path of solution among the figure with solid arrow, the with dashed lines arrow marks the circulating path of refrigeration working medium.The utility model is through regulating the cold of each evaporimeter of refrigeration system; Can regulate the temperature of dehumidification solutions at different levels; Control the concentration of dehumidification solutions at different levels simultaneously through suitable moisturizing; Realization to reduce the irreversible loss of process, improves the Energy Efficiency Ratio (COP) that unit is handled new wind to the progressively dehumidifying and the cooling of new wind; Simultaneously, the unit surface cooler is only handled sensible heat load, can adopt high-temperature water, can reduce the energy consumption of producing chilled water.
The principle and the summer of unit winter operation are similar; Difference is through the cross valve switching refrigerant flow direction and summer condition to be moved on the contrary; Make summer as condenser 4,5 as the solution among evaporator cools module C, the B to return air dehumidifying cooling, and carry out warming and humidifying as the solution among condenser heating E, the F to new wind as 6,7 of evaporimeter summer; Feed hot water in the surface cooler 2 and convert heater into; Through the new wind of the warm and moist behind the warming and humidifying with after another strand return air mixes, pass through send into after surface cooler 2 heats indoor.
At transition season, unit is not opened refrigeration system, only moves the full heat recovery units of A and D, through solution between the superior and the subordinate with the full heat exchange of air, realize full recuperation of heat operating mode operation, can realize to the new wind of indoor supply.
The type of drive of compressor has two kinds in the unit: 1) multiple compressors drives corresponding condenser and evaporimeter, 2 respectively) all condenser and the evaporimeters of compressor driving.Concrete mode is confirmed according to the factors such as capacity of air dewetting, amount of cooling water and refrigeration system.First embodiment has been shown among Fig. 1, has driven all corresponding condenser and evaporimeter with compressor 3 among the figure.Second embodiment has been shown among Fig. 2; Compare with first embodiment; Drive corresponding left condenser 4 and right evaporimeter 7 with compressor 3; Compressor 31 drives corresponding right condenser 5 and left evaporimeter 6, and simultaneously, expansion valve also is provided with expansion valve 11 and expansion valve 112 respectively to be connected the condenser and the evaporimeter of correspondence respectively.
Solution damping unit according to the utility model has following beneficial effect:
1. unit utilizes solution dehumidification to produce dry new wind, new wind with utilize the cold water realization to lower the temperature after return air mixes.Cold water natural cold source capable of using obtains, and also can adopt electric refrigerating machine to produce, as adopts the electricity refrigeration, because the temperature of cold water is higher than prior art, has improved the evaporating temperature of unit thereby can significantly improve refrigerating efficiency;
2. the unit cooling coil adopts the cold water of higher temperatures, does not have the water of coagulating and generates, and can reduce bacteria breed;
3. multistage damping treatment system of solution and heat pump are combined; Utilize the cold cooling solution dehumidification process step by step of the evaporator with heat pump of different evaporating temperatures respectively; Adopt the concentrated regeneration of the heat pump heat exhaust realization solution of different condensation temperatures; To solve air and liquid inventory than being difficult to satisfy simultaneously heat and mass and problem near reversible process, the irreversible loss of minimizing air handling process increases substantially treatment effeciency;
4. the solution-type full heat recovery device is set, in the unit in order to reclaim the air draft energy;
5. utility model is designed the full air unit of heat pump driven solution, and unit efficiency is higher than the full air unit that tradition adopts dehumidification by condensation, has the considerable energy saving advantage.
The preferred embodiment that the above is merely the utility model is not limited to the utility model, and for a person skilled in the art, the utility model can have various changes and variation.All within the spirit and principle of the utility model, any modification of being done, be equal to replacement, improvement etc., all should be included within the protection domain of the utility model.
Claims (9)
1. the full air unit of the solution damping with full heat recovery device is characterized in that, comprising:
The full heat recovery module of solution (1), solution damping module (E, F) and solution regeneration module (B, C), inner hygroscopic solution all forms solution and circulates up and down, contacts with gas;
Surface cooler (2);
Return airway, order pass outside the top (A) and said solution regeneration module (B, C) back communication chamber of said full heat recovery module (1);
New wind air channel, order are passed in bottom (D), said solution damping module (E, F) and said surface cooler (2) the back communication chamber of said full heat recovery module (1);
First heat exchanger (6,7) connects each said solution damping module (E, F), makes hygroscopic solution in the said solution damping module (E, F) said first heat exchanger (6,7) of flowing through form said solution and circulate up and down;
Second heat exchanger (4,5) connects each said solution regeneration module (B, C), makes hygroscopic solution in the said solution regeneration module (B, C) said second heat exchanger (4,5) of flowing through form said solution and circulate up and down;
Wherein, be connected with expansion valve (11) through compressor (3) respectively between said first heat exchanger (6,7) and said second heat exchanger (4,5) and form the refrigerant circulation;
The bottom of said solution damping module (E, F) is communicated with the bottom of said solution regeneration module (B, C), forms the solution regeneration cycle.
2. the full air unit of the solution damping of band full heat recovery device according to claim 1; It is characterized in that; Said solution damping module (E, F) and said solution regeneration module (B, C) all are provided with a plurality of; Said return airway is in proper order through a plurality of said solution regeneration modules (B, C), and said new wind air channel is in proper order through a plurality of said solution damping modules (E, F), each said solution damping module (E, F) all with said solution regeneration module (B, C) corresponding a connection.
3. the full air unit of the solution damping of band full heat recovery device according to claim 1 is characterized in that, said first heat exchanger (6,7) and said second heat exchanger (4,5) are provided with a plurality of.
4. the full air unit of the solution damping of band full heat recovery device according to claim 1; It is characterized in that the full heat recovery module of said solution (1), solution damping module (E, F) and solution regeneration module (B, C) are equipped with the said solution of solution water circulating pump (10) formation and circulate up and down.
5. the full air unit of the solution damping of band full heat recovery device according to claim 1 is characterized in that, in the bottom of said solution damping module (E, F) and the pipeline that the bottom of said solution regeneration module (B, C) is communicated with heat exchanger plates is installed and is changed (8,9).
6. the full air unit of the solution damping of band full heat recovery device according to claim 1 is characterized in that, said new wind air channel is being provided with the pipeline that mixes with return air before through said surface cooler (2).
7. the full air unit of the solution damping of band full heat recovery device according to claim 1 is characterized in that, said solution regeneration module (B, C) is provided with water compensating valve (12,13), is communicated with extraneous water pipe and the solution cavity in the said solution regeneration module (B, C).
8. the full air unit of the solution damping of band full heat recovery device according to claim 1; It is characterized in that said first heat exchanger (6,7) is connected with a said expansion valve (11) through a said compressor (3) jointly with said second heat exchanger (4,5) and forms circulation.
9. the full air unit of the solution damping of band full heat recovery device according to claim 3; It is characterized in that; Said first heat exchanger (6,7) and said second heat exchanger (4,5) have a plurality of respectively; Said compressor (3) and said expansion valve (11) have a plurality of accordingly respectively, and each said first heat exchanger (6,7) is connected with a said expansion valve (11) through a corresponding said compressor (3) respectively with each said second heat exchanger (4,5) and forms separately independently circulation.
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| Application Number | Priority Date | Filing Date | Title |
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| CN2012200423267U CN202452608U (en) | 2012-02-09 | 2012-02-09 | Solution-humidity-regulating all-air unit with total-heat recovery device |
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| CN2012200423267U CN202452608U (en) | 2012-02-09 | 2012-02-09 | Solution-humidity-regulating all-air unit with total-heat recovery device |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102538087A (en) * | 2012-02-09 | 2012-07-04 | 北京华创瑞风空调科技有限公司 | Solution humidifying all-air unit with total-heat recovering device and solution humidifying method |
| CN102908879A (en) * | 2012-10-22 | 2013-02-06 | 珠海市威望节能科技有限公司 | Efficient energy-saving air dehumidifying system |
| CN102927630A (en) * | 2012-11-07 | 2013-02-13 | 刘拴强 | Total heat recovery type heating and humidifying fresh air handling unit |
| CN104061634A (en) * | 2014-03-14 | 2014-09-24 | 东南大学 | Two-stage high and low temperature liquid desiccant air-conditioning system driven by heat pump and controlling method |
| CN104141985A (en) * | 2014-08-22 | 2014-11-12 | 深圳市晓风建筑环境科技有限公司 | Fresh air handling unit realizing independent control of temperature and humidity |
| CN104501466A (en) * | 2014-12-22 | 2015-04-08 | 丛旭日 | Thermal regeneration solution dehumidifying unit of ground source heat pump |
| CN107270428A (en) * | 2017-06-06 | 2017-10-20 | 江苏格瑞力德空调制冷设备有限公司 | A kind of air-cooled solution humidifying Fresh air handling units of novel wall hanger family formula |
-
2012
- 2012-02-09 CN CN2012200423267U patent/CN202452608U/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102538087A (en) * | 2012-02-09 | 2012-07-04 | 北京华创瑞风空调科技有限公司 | Solution humidifying all-air unit with total-heat recovering device and solution humidifying method |
| CN102908879A (en) * | 2012-10-22 | 2013-02-06 | 珠海市威望节能科技有限公司 | Efficient energy-saving air dehumidifying system |
| CN102927630A (en) * | 2012-11-07 | 2013-02-13 | 刘拴强 | Total heat recovery type heating and humidifying fresh air handling unit |
| CN102927630B (en) * | 2012-11-07 | 2016-04-13 | 刘拴强 | Total heat recovery type warming and humidifying Fresh air handling units |
| CN104061634A (en) * | 2014-03-14 | 2014-09-24 | 东南大学 | Two-stage high and low temperature liquid desiccant air-conditioning system driven by heat pump and controlling method |
| CN104061634B (en) * | 2014-03-14 | 2016-11-02 | 东南大学 | A kind of heat pump driven two-stage high/low temperature solution dehumidifying air-conditioning system and control method |
| CN104141985A (en) * | 2014-08-22 | 2014-11-12 | 深圳市晓风建筑环境科技有限公司 | Fresh air handling unit realizing independent control of temperature and humidity |
| CN104501466A (en) * | 2014-12-22 | 2015-04-08 | 丛旭日 | Thermal regeneration solution dehumidifying unit of ground source heat pump |
| CN107270428A (en) * | 2017-06-06 | 2017-10-20 | 江苏格瑞力德空调制冷设备有限公司 | A kind of air-cooled solution humidifying Fresh air handling units of novel wall hanger family formula |
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Owner name: BEIJING HUACHUANG RUIFENG TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: BEIJING SINOREFINE AIR CONDITIONING TECHNOLOGY CO., LTD. Effective date: 20131112 |
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| C41 | Transfer of patent application or patent right or utility model | ||
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Free format text: CORRECT: ADDRESS; FROM: 100084 HAIDIAN, BEIJING TO: 101300 SHUNYI, BEIJING |
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| TR01 | Transfer of patent right |
Effective date of registration: 20131112 Address after: 101300 Beijing city Shunyi District zhaoquanying Zhaofeng industrial base Dongying Road No. 19 Patentee after: Beijing Huachuang refine Technology Co. Ltd. Address before: 100084, Sohu cyber building, No. 1, Zhongguancun East Road, Beijing, Haidian District 409A Patentee before: Beijing SinoRefine Air Conditioning Technology Co., Ltd. |
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| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20151022 Address after: 100084, Sohu cyber building, No. 1, Zhongguancun East Road, Beijing, Haidian District 409A Patentee after: Beijing SinoRefine Air Conditioning Technology Co., Ltd. Address before: 101300 Beijing city Shunyi District zhaoquanying Zhaofeng industrial base Dongying Road No. 19 Patentee before: Beijing Huachuang refine Technology Co. Ltd. |
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| TR01 | Transfer of patent right | ||
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Effective date of registration: 20170915 Address after: 100084, building 9, building 1, Zhongguancun East Road, Beijing, Haidian District, 04-09A Co-patentee after: Tianjin Huachuang Ruifeng air conditioning equipment Co. Patentee after: Beijing SinoRefine Air Conditioning Technology Co., Ltd. Address before: 100084, Sohu cyber building, No. 1, Zhongguancun East Road, Beijing, Haidian District 409A Patentee before: Beijing SinoRefine Air Conditioning Technology Co., Ltd. |
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| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120926 |