CN204665533U - A kind of solution-type air-conditioner set of constant enthalpy dehumidifying - Google Patents
A kind of solution-type air-conditioner set of constant enthalpy dehumidifying Download PDFInfo
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- CN204665533U CN204665533U CN201520251974.7U CN201520251974U CN204665533U CN 204665533 U CN204665533 U CN 204665533U CN 201520251974 U CN201520251974 U CN 201520251974U CN 204665533 U CN204665533 U CN 204665533U
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Abstract
The utility model discloses the solution-type air-conditioner set of a kind of constant enthalpy dehumidifying, comprise refrigerant-cycle systems and solution recycle system, wherein, described solution recycle system comprises solution total heat recovery subsystem and solution dehumidification regeneration subsystem; Described total heat recovery subsystem comprises at least two loops, and each loop comprises the release core body, collection box, recovery pump and the recovery core body that are communicated with in turn, and the release core body in each loop is at least 2 and parallel with one another; Release core body in each loop is arranged on air-supply wind path, reclaims core body and is arranged on return air wind path.The utility model combines the advantage of freeze drying and solution dehumidification, simplifies process, and salting liquid charging amount is reduced; And avoid the corrosion of solution heat exchanger in conventional solution dehumidifying, thus increase the service life of equipment.
Description
Technical field
The utility model relates to solution-type air-conditioner set, especially a kind of solution-type air-conditioner set of constant enthalpy dehumidifying.
Background technology
The salting liquid with hygroscopic effect is larger to corrosion of metal, and along with the rising of solution temperature, this corrosion rate can be accelerated, conventional soln formula air conditioner adopts the heat exchanger that series connection one is additional in solution dehumidification core body, to regulate the temperature of heat exchange solution, namely heat exchanger carries out exchange heat between solution and cold-producing medium.For the corrosion avoiding heat exchanger to be subject to salting liquid, improve life of product, need to adopt novel solution dehumidification, regeneration.
In conventional solution-type total heat recovery system, 1 recovery pump only can realize 1 grade of recuperation of heat.In order to reduce product initial cost and operating cost, economize energy reduction energy consumption, need the charging amount of minimizing salting liquid and improve 1 recovery pump can realize more than 1 grade of recuperation of heat effect.
Utility model content
Utility model object: provide the solution-type air-conditioner set that a kind of constant enthalpy dehumidifies, to solve the problems referred to above that prior art exists.
Technical scheme: a kind of solution-type air-conditioner set of constant enthalpy dehumidifying, comprise refrigerant-cycle systems and solution recycle system, wherein, described solution recycle system comprises solution total heat recovery subsystem and solution dehumidification regeneration subsystem;
Described total heat recovery subsystem comprises at least two loops, and each loop comprises the release core body, collection box, recovery pump and the recovery core body that are communicated with in turn, and the release core body in each loop is at least 2 and parallel with one another; Release core body in each loop is arranged on air-supply wind path, reclaims core body and is arranged on return air wind path.
Further, described solution dehumidification regeneration subsystem comprises solution dehumidification unit and regeneration of waste liquor unit, described solution dehumidification unit comprises the dehumidifying core body, the first liquor box and the dehumidifying pump that are communicated with successively, and described dehumidifying core body is arranged at air-supply wind path and is positioned at the air intake of pressure fan; Described regeneration of waste liquor unit comprises the regeneration core body, the second liquor box and the regenerative pump that are communicated with successively, and described regeneration core body is positioned at return air wind path.
Further, described refrigerant-cycle systems comprises the condenser and evaporimeter that are interconnected and form closed-loop path, a communicating pipe between condenser and evaporimeter is provided with expansion valve, be provided with cross valve and compressor another communicating pipe, the loop that compressor consists of cross valve access condenser and evaporimeter; Described evaporimeter air-supply wind path and dehumidifying core body and pressure fan between.
Further, the solution-type air-conditioner set of constant enthalpy dehumidifying has an exhaust blower, and described exhaust blower is positioned at return air wind path and is positioned at and reclaims by core body.
Further, in total heat recovery subsystem, the collection box in each loop is communicated with by the first balance pipe.
Further, be communicated with by the second balance pipe between described first liquor box and the second liquor box.
Beneficial effect: in the utility model, has 2 recovery pumps, corresponding 4 grades of release core bodys and 2 grades of recovery core bodys, and 1 recovery pump can realize 1.5 grades of recuperations of heat, changes the mode that tradition 1 recovery pump only realizes 1 grade of recuperation of heat.
Further, after utilizing forecooler (i.e. evaporimeter) and solution total heat recovery system to carry out pretreatment (cool-down dehumidification) to new wind, the new wind processed is dehumidified again by solution dehumidification core body, in solution dehumidification process, do not have energy to input, and namely realizes constant enthalpy dehumidifying.The utility model combines the advantage of freeze drying and solution dehumidification, simplifies process, and salting liquid charging amount is reduced; And avoid the corrosion of solution heat exchanger in conventional solution dehumidifying, thus increase the service life of equipment.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Fig. 2 a is the principle schematic of Fresh air handing process.
Fig. 2 b is Fresh air handing process psychrometric chart.
Detailed description of the invention
It should be noted that, in the utility model, in order to description technique scheme in more detail, the identical device in loop, device or unit, adopt the mode such as " first ", " second " to describe, to show differentiation.But the term such as " first ", " second " is also not interpreted as the importance and functions difference to some extent of each unit or unit.
Simultaneously, use term " to comprise " in this manual and/or " comprising " time, it indicates exists described feature, entirety, step, operation, element and/or assembly, but does not get rid of existence or additional other features one or more, entirety, step, operation, element, assembly and/or their combination.
As shown in Figure 1, a kind of solution-type air-conditioner set of constant enthalpy dehumidifying, comprises refrigerant-cycle systems and solution recycle system.The compressor 1 that refrigerant-cycle systems is connected by freon pipeline, cross valve 2, condenser 3, expansion valve 4, evaporimeter 5 form;
Solution recycle system comprises solution total heat recovery subsystem and solution dehumidification regeneration subsystem, and solution total heat recovery system comprises the first recovery core body 6, second and reclaims core body 7, first release core body 8, second release core body 9, the 3rd release core body 10, the 4th release core body 11, first collection box 12, second collection box 13, first recovery pump 14, second recovery pump 15 and solution line composition;
Solution dehumidification regeneration subsystem comprises solution dehumidification unit and regeneration of waste liquor unit, wherein solution dehumidification unit is made up of the pump 18 that dehumidifies, dehumidifying core body 16, first liquor box 17 and solution line, and regeneration of waste liquor unit is made up of regenerative pump 21, regeneration core body 19, second liquor box 20 and solution line.
The course of work:
New wind enters solution total heat recovery system, namely core body 9, the 3rd release core body 10, the 4th release core body 11 is discharged by the first release core body 8, second successively, evaporimeter 5 is entered after cool-down dehumidification, enter solution dehumidification core body 16 after further cool-down dehumidification by salt-solution absorption moisture, namely after constant enthalpy dehumidifying, warp sends into indoor by pressure fan 22;
Return air enters solution total heat recovery system via exhaust blower 23, namely reclaim core body 6, second by first successively and reclaim core body 7, enter condenser 3 after warming and humidifying, after heating up further, enter regeneration of waste liquor core body 19, moisture in absorption and regeneration solution, namely drains into outdoor after equal-enthalpy humidifying;
The high temperature and high pressure gas that compressor 1 is discharged enters condenser 3 by cross valve 2, in condenser 3, cool also condensation become subcooled liquid (its liberated heat is taken away by air), evaporimeter 5 is entered again after expansion valve 4 reducing pressure by regulating flow, become superheated steam after the heat of the air of evaporimeter 5 is flow through in absorption to be inhaled in compressor by cross valve 2, thus complete the circulation of refrigerant system;
Solution in solution dehumidification core body 16 enters the first liquor box 17, enters solution dehumidification core body 16 by dehumidifying pump 18; Solution in regeneration of waste liquor core body 19 enters the second liquor box 20, enters regeneration of waste liquor core body 19 by regenerative pump 21.
The effect of the first balance pipe 24 is the solution level of balance unit first collection box 12 and the second collection box 13 and is balanced the solution concentration of the first collection box 12 and the second collection box 13 by molecular diffusion; In like manner, the effect of the second balance pipe 25 is the solution level of balance unit first liquor box 17 and the second liquor box 20 and is balanced the solution concentration of the first liquor box 17 and the second liquor box 20 by molecular diffusion.
In the above-described embodiments, the first liquor box is weak solution case, and the second liquor box is concentrated solution case.
In a word, in the utility model, system utilizes solution to discharge core body and forecooler (i.e. evaporimeter) carries out pretreatment (cool-down dehumidification) to new wind, utilizes solution dehumidification core body to carry out degree of depth dehumidification treatments (constant enthalpy dehumidifying) to the new wind after process; Utilize solution recovery core body and condenser to carry out pretreatment (warming and humidifying) to return air, utilize the return air after process to regenerate solution.
More than describe preferred embodiment of the present utility model in detail; but; the utility model is not limited to the detail in above-mentioned embodiment; within the scope of technical conceive of the present utility model; can carry out multiple equivalents to the technical solution of the utility model, these equivalents all belong to protection domain of the present utility model.It should be noted that in addition, each the concrete technical characteristic described in above-mentioned detailed description of the invention, in reconcilable situation, can be combined by any suitable mode.In order to avoid unnecessary repetition, the utility model illustrates no longer separately to various possible combination.In addition, also can be combined between various different embodiment of the present utility model, as long as it is without prejudice to thought of the present utility model, it should be considered as content disclosed in the utility model equally.
Claims (6)
1. a solution-type air-conditioner set for constant enthalpy dehumidifying, it is characterized in that, comprise refrigerant-cycle systems and solution recycle system, wherein, described solution recycle system comprises solution total heat recovery subsystem and solution dehumidification regeneration subsystem;
Described total heat recovery subsystem comprises at least two loops, each loop comprises the release core body (8,9,10,11), collection box (12,13), the recovery pump (14,15) that are communicated with in turn and reclaims core body (6,7), and the release core body in each loop is at least 2 and parallel with one another; Release core body in each loop is arranged on air-supply wind path, reclaims core body and is arranged on return air wind path.
2. the solution-type air-conditioner set of constant enthalpy dehumidifying as claimed in claim 1, it is characterized in that, described solution dehumidification regeneration subsystem comprises solution dehumidification unit and regeneration of waste liquor unit,
Described solution dehumidification unit comprises dehumidifying core body (16), the first liquor box (17) and the pump (18) that dehumidifies that are communicated with successively, and described dehumidifying core body is arranged at air-supply wind path and is positioned at the air intake of pressure fan (22);
Described regeneration of waste liquor unit comprises the regeneration core body (19), the second liquor box (20) and the regenerative pump (21) that are communicated with successively, and described regeneration core body is positioned at return air wind path.
3. the solution-type air-conditioner set of constant enthalpy dehumidifying as claimed in claim 2, it is characterized in that, described refrigerant-cycle systems comprises the condenser (3) and evaporimeter (5) that are interconnected and form closed-loop path, be provided with expansion valve (4) communicating pipe between condenser and evaporimeter, be provided with cross valve (2) and compressor (1) another communicating pipe, the loop that compressor consists of cross valve access condenser and evaporimeter; Described evaporimeter air-supply wind path and dehumidifying core body and pressure fan between.
4. the solution-type air-conditioner set of constant enthalpy dehumidifying as claimed in claim 1, is characterized in that, the solution-type air-conditioner set of constant enthalpy dehumidifying has an exhaust blower (23), and described exhaust blower is positioned at return air wind path and is positioned at and reclaims by core body.
5. the solution-type air-conditioner set of the constant enthalpy dehumidifying as described in any one of Claims 1-4, is characterized in that, in total heat recovery subsystem, the collection box in each loop is communicated with by the first balance pipe (24).
6. the solution-type air-conditioner set of constant enthalpy dehumidifying as claimed in claim 2 or claim 3, is characterized in that, is communicated with between described first liquor box (17) and the second liquor box (20) by the second balance pipe (25).
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| CN201520251974.7U CN204665533U (en) | 2015-04-23 | 2015-04-23 | A kind of solution-type air-conditioner set of constant enthalpy dehumidifying |
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| CN201520251974.7U CN204665533U (en) | 2015-04-23 | 2015-04-23 | A kind of solution-type air-conditioner set of constant enthalpy dehumidifying |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105571020A (en) * | 2016-03-09 | 2016-05-11 | 华南理工大学 | Multistage hollow fiber membrane liquid dehumidifying device applicable to hot and humid area |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105571020A (en) * | 2016-03-09 | 2016-05-11 | 华南理工大学 | Multistage hollow fiber membrane liquid dehumidifying device applicable to hot and humid area |
| CN105571020B (en) * | 2016-03-09 | 2018-01-05 | 华南理工大学 | A kind of multistage hollow-fibre membrane liquid dehumidifying device for being applicable damp-heat area |
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Effective date of registration: 20191206 Address after: 211151 No.2, Wangshan Road, Hengxi street, Jiangning District, Nanjing City, Jiangsu Province Patentee after: Nanjing South Cooling Air Conditioning Equipment Co., Ltd. Address before: Jiangning District of Nanjing City, Jiangsu province 211151 Hengxi Street Community Wu Tao Wang Road No. 2-2 Patentee before: Nanjing HanWei NanLeng Refrigeration Group Co., Ltd. |