CN221237973U - Condensate energy recovery system for purifying air conditioning unit - Google Patents
Condensate energy recovery system for purifying air conditioning unit Download PDFInfo
- Publication number
- CN221237973U CN221237973U CN202322936884.9U CN202322936884U CN221237973U CN 221237973 U CN221237973 U CN 221237973U CN 202322936884 U CN202322936884 U CN 202322936884U CN 221237973 U CN221237973 U CN 221237973U
- Authority
- CN
- China
- Prior art keywords
- condensed water
- water
- condensate
- recovery
- heat exchange
- 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.)
- Active
Links
- 238000011084 recovery Methods 0.000 title claims abstract description 86
- 238000004378 air conditioning Methods 0.000 title claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 194
- 238000010438 heat treatment Methods 0.000 claims abstract description 16
- 230000001502 supplementing effect Effects 0.000 claims abstract description 7
- 238000004140 cleaning Methods 0.000 claims abstract description 5
- 238000007791 dehumidification Methods 0.000 claims description 16
- 238000004891 communication Methods 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000005265 energy consumption Methods 0.000 description 6
- 238000001816 cooling Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000009471 action Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000002262 irrigation Effects 0.000 description 1
- 238000003973 irrigation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Landscapes
- Devices For Blowing Cold Air, Devices For Blowing Warm Air, And Means For Preventing Water Condensation In Air Conditioning Units (AREA)
Abstract
The utility model relates to the technical field of energy recovery, and discloses a condensed water mass energy recovery system for a purified air conditioning unit, which comprises the following components: the condensed water generating module is used for processing the high-humidity air in the purified air conditioning unit into low-humidity air so as to generate condensed water; the condensed water collecting and lifting module comprises a condensed water recovery water tank which is used for storing condensed water generated by the condensed water generating module; the condensed water energy recovery module is used for exchanging heat of condensed water in the condensed water recovery water tank to the heating space; the condensed water quality recovery module comprises a condensed water secondary utilization device, wherein the condensed water secondary utilization device is used for collecting condensed water subjected to heat exchange by the condensed water energy recovery module, and the condensed water subjected to heat exchange is used for supplementing water or cleaning other functional modules. The condensed water energy recovery system of the purified air conditioning unit improves the recovery and reutilization efficiency of the cold energy of the condensed water and saves energy.
Description
Technical Field
The utility model relates to the technical field of energy recovery, in particular to a condensed water mass energy recovery system for a purified air conditioning unit.
Background
Along with the increasing demands of the market for electronic components, the number of electronic clean plants is increased, the construction scale is increased, and the demand for purifying air is increased. The condensate water is used as a byproduct of cold and hot treatment of the purifying air conditioning unit, the water quality is clean, the condensate water quantity is continuously increased along with the increase of the purified air quantity, and the cold energy contained in the condensate water continuously is quite considerable.
However, most factories in the industry directly drain condensed water at present, and part of factories with energy conservation consciousness can recycle the condensed water as a substitute for tap water, but the modes do not reasonably utilize the cold energy contained in the condensed water to places with demands, so that energy waste is caused.
Disclosure of utility model
The utility model provides a condensed water energy recovery system for a purified air conditioning unit, which improves the recovery and reutilization efficiency of condensed water cold energy and saves energy.
The utility model provides a condensed water mass energy recovery system for a purified air conditioning unit, which comprises the following components:
the condensed water generating module is used for processing the high-humidity air of the purified air conditioning unit into low-humidity air so as to generate condensed water;
The condensate water collecting and lifting module comprises a condensate water recovery tank, wherein the condensate water recovery tank is used for storing condensate water generated by the condensate water generating module;
The condensed water energy recovery module is used for exchanging heat of condensed water in the condensed water recovery water tank to the heating space;
The condensed water quality recovery module comprises a condensed water secondary utilization device, wherein the condensed water secondary utilization device is used for collecting condensed water subjected to heat exchange by the condensed water quality recovery module and using the condensed water subjected to heat exchange for supplementing water or cleaning other functional modules.
According to the condensate energy recovery system of the purified air conditioning unit, the condensate is recovered and stored by the condensate recovery water tank, and then the cold energy contained in the condensate is recovered and utilized to the heating space, so that the air conditioning energy consumption of the heating space is reduced. After the cold energy of the condensed water is recovered, the water quantity is reused, and water is replenished or cleaned for water points in factories. The recovery system can fully play the role of condensed water, thereby making the best use of things and saving energy more accurately.
In some possible embodiments, the condensate water generating module comprises a dehumidification coil, the high humidity air flowing in a direction perpendicular to the dehumidification coil.
In some possible embodiments, the condensate recovery tank is for receiving condensate from the dehumidification coil.
In some possible embodiments, the condensate collection and lifting module further comprises a lifting water pump, an inlet end of the lifting water pump being in communication with the condensate recovery tank, an outlet end of the lifting water pump being in communication with the condensate recovery module.
In some possible embodiments, the condensed water energy recovery module includes a heat exchange tube, a water inlet of the heat exchange tube is communicated with the lift water pump, and a water outlet of the heat exchange tube is communicated with the condensed water secondary utilization device.
In some possible embodiments, the heat exchange tube is a heat exchange coil.
In some possible embodiments, the heat exchange coil is one of a copper tube, an aluminum tube, a stainless steel tube, and a plastic tube.
In some possible embodiments, the outer wall of the heat exchange coil is a light pipe or the outer wall of the heat exchange tube has heat exchange fins.
In some possible embodiments, a water level sensor is provided in the condensate recovery tank for detecting the water level in the condensate recovery tank.
Drawings
Fig. 1 is a schematic structural diagram of a condensate energy recovery system for a purified air conditioning unit according to an embodiment of the present utility model.
In the figure:
1-a condensed water generation module; 2-a condensed water collecting and lifting module; 3-a condensed water energy recovery module; 4-a condensate water quality recovery module; 5-dehumidifying coil; 6-purifying an air conditioning unit; 7-a conveying pipeline; 8-a condensate recovery tank; 9-lifting a water pump; 10-a heat exchange coil; 11-heating space; 12-a secondary condensate water utilization device.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Referring to fig. 1, the condensate energy recovery system of the purifying air conditioning unit in the embodiment of the utility model includes a condensate generating module 1, a condensate collecting and lifting module 2, a condensate energy recovery module 3 and a condensate quality recovery module 4, where the condensate generating module 1, the condensate collecting and lifting module 2, the condensate energy recovery module 3 and the condensate quality recovery module 4 are sequentially communicated to realize recovery and reuse of condensate.
Specifically, the condensed water generating module 1 is used to process the high humidity air in the purified air conditioning unit 6 into low humidity air, and in the process, the gas air is changed from the high humidity state to the low humidity state, thereby generating condensed water. The condensate collecting and lifting module 2 includes a condensate recovering water tank 8 and a lifting water pump 9, and the condensate recovering water tank 8 is used for recovering condensate generated by the condensate generating module 1 and storing and insulating the condensate. The condensed water energy recovery module 3 comprises a heat exchange tube, the heat exchange tube can be a heat exchange coil 10, and the heat exchange area between the heat exchange coil 10 and the heating space 11 can be increased, so that cold energy in condensed water can be better diffused out, and a better heat exchange effect can be achieved. The heat exchange coil 10 is positioned in different heating spaces 11, and when condensate water flows to the heat exchange coil 10 from the condensate water recovery tank 8, the heat exchange coil 10 can be utilized to exchange heat with the heating spaces 11, so that the effect of cooling the heating spaces 11 is achieved. The condensate water quality recovery module 4 comprises a condensate water secondary utilization device 12, the condensate water passing through the heat exchange coil 10 does not contain cold energy, at the moment, the condensate water flows to the condensate water secondary utilization device 12, and the condensate water secondary utilization device 12 is used for supplementing water or cleaning other functional modules with the condensate water.
In the condensate energy recovery system of the purifying air conditioning unit in the embodiment, the condensate water is recovered and stored by utilizing the condensate water recovery water tank 8, and then the cold energy contained in the condensate water is recovered and utilized to the heating space 11, so that the air conditioning energy consumption of the heating space 11 is reduced. After the cold energy of the condensed water is recovered, the water quantity is reused, and water is replenished or cleaned for water points in factories. The recovery system can fully play the role of condensed water, thereby making full use of things and saving energy.
With continued reference to fig. 1, the condensate water generating module 1 includes a dehumidification coil 5, and the highly humid air in the clean air conditioning unit 6 flows from one side of the dehumidification coil 5 to the other side of the dehumidification coil 5, during which the generated condensate water may flow downward along the dehumidification coil 5 under the action of gravity. The condensate water recovery tank 8 may be disposed below the dehumidification coil 5 to receive the condensate water, and no external force is required during the process of flowing the condensate water into the condensate water recovery tank 8, so that energy consumption can be saved. Or a conveying pipeline 7 can be arranged between the condensate water recovery tank 8 and the dehumidification coil 5 so as to convey condensate water into the condensate water recovery tank 8 in a centralized manner, so that waste caused by the condensate water falling outside the condensate water recovery tank 8 can be avoided.
The arrows of the condensate water generating module 1 in fig. 1 can be understood as the flowing direction of air, and the high humidity air can flow in the direction perpendicular to the dehumidification coil 5 when passing through the dehumidification coil 5, so that the contact area between the high humidity air and the dehumidification coil 5 can be increased, thereby achieving better dehumidification effect and generating more condensate water.
As shown in fig. 1, the inlet end of the lifting water pump 9 is communicated with the condensed water recovery water tank 8, and the outlet end is communicated with the water inlet of the heat exchange coil 10 of the condensed water energy recovery module 3. Wherein, condensate recovery water tank 8 and lifting water pump 9 accessible pipeline 7 are connected, also accessible pipeline 7 is connected between lifting water pump 9 and the heat exchange coil 10. The lifting water pump 9 can be used for conveying the condensed water in the condensed water recovery water tank 8 into the heat exchange coil 10 so as to facilitate the heat exchange between the heat exchange coil 10 and the heating space 11.
As an alternative embodiment, a water level sensor (not shown) may be further provided in the condensate recovery tank 8, the water level sensor being configured to detect the water level in the condensate recovery tank 8, and when the water level reaches a predetermined value, the lift pump 9 may be turned on to deliver condensate in the condensate recovery tank 8 to the heat exchange coil 10. In this way, space can be made for the condensate recovery tank 8, ensuring that the condensate recovery tank 8 is able to continuously recover condensate produced by the condensate production module 1.
Alternatively, in other embodiments, the heat exchange coil 10 may be disposed at the bottom of the condensate recovery tank 8, and the bottom of the condensate recovery tank 8 may be provided with a flow valve, which communicates with the water inlet of the heat exchange coil 10 through the delivery pipe 7. When the water level in the condensate water recovery tank 8 reaches a certain height, the flow valve can be opened, so that the condensate water in the condensate water recovery tank 8 flows to the heat exchange coil 10 along with the conveying pipeline 7 under the action of gravity. Therefore, the structure of the lifting water pump 9 can be omitted, and the energy consumption of the lifting water pump 9 is reduced, so that the energy is further saved.
As shown in fig. 1, the heat exchange coil 10 may be one of a copper pipe, an aluminum pipe, a stainless steel pipe, and a plastic pipe, and the heat exchange coil 10 may have a circular or oval cross-sectional shape. In addition, the outer wall of the heat exchange coil 10 can be in the form of a light pipe or in the form of a structure with heat exchange fins on the outer wall, so that the heat exchange area between the heat exchange coil and the heating space 11 can be further increased, and the heat exchange effect is further improved.
In this embodiment, the heating space 11 may be, for example, a space with a lot of heat, such as an electrical room, a vacuum pump room, and an air compressor room, or the condensed water from the condensed water recovery water tank 8 may also be used for pre-cooling fresh air, exchanging heat with process cooling water, etc., so as to sufficiently diffuse the cold energy in the condensed water.
The water outlet of the heat exchange coil 10 can be communicated with the condensed water secondary utilization device 12 through the conveying pipeline 7, the condensed water quality recovery module 4 can be divided according to the use requirement in a factory, and condensed water is further applied to functional modules with water requirement, and the functional modules can be modules such as a cooling tower, a water spraying chamber, a green belt, reclaimed water and the like. The condensed water secondary utilization device 12 may be provided with a plurality of water outlets, each of which may be communicated with one of the functional modules for supplementing water to the cooling tower, supplementing water to the shower room, greening irrigation, supplementing water to the medium water, and the like. Or the condensed water can also be used for cleaning sanitary ware. In the condensate water quality recovery module 4, the condensate water replaces tap water, so that energy consumption is saved.
It can be understood that compared with the direct drainage mode and the water quantity recovery mode of condensed water in the current industry, the condensed water energy recovery system of the purifying air conditioning unit provided by the utility model can recover and utilize the cold energy contained in the condensed water to the heating part, so that the energy consumption of the air conditioner at the part is reduced. For industrial plants with larger fresh air volume demand, the water quantity of the generated condensed water is very objective, taking a certain factory in the south as an example, each purification air conditioning unit with 10 ten thousand air volumes can separate out the water quantity of the condensed water of 1.2-1.6 m < 3 >/h in summer, the refrigeration capacity is about 14-20 kw, and taking a 10-degree heat exchange temperature difference as an example, each fresh air unit can generate 28.8-38.4 tons of condensed water in one day, and some plants with larger scales even have tens of air conditioning units, so that the energy and water quantity economic benefits of recycling the condensed water can be seen.
It will be apparent to those skilled in the art that various modifications and variations can be made to the embodiments of the present utility model without departing from the spirit and scope of the utility model. Thus, it is intended that the present utility model also include such modifications and alterations insofar as they come within the scope of the appended claims or the equivalents thereof.
Claims (9)
1. A purified air conditioning unit condensate energy recovery system, comprising:
The condensed water generating module is used for processing the high-humidity air in the purified air conditioning unit into low-humidity air so as to generate condensed water;
The condensate water collecting and lifting module comprises a condensate water recovery tank, wherein the condensate water recovery tank is used for storing condensate water generated by the condensate water generating module;
The condensed water energy recovery module is used for exchanging heat of condensed water in the condensed water recovery water tank to the heating space;
The condensed water quality recovery module comprises a condensed water secondary utilization device, wherein the condensed water secondary utilization device is used for collecting condensed water subjected to heat exchange by the condensed water quality recovery module and using the condensed water subjected to heat exchange for supplementing water or cleaning other functional modules.
2. The purified air conditioning unit condensate energy recovery system of claim 1, wherein the condensate generation module comprises a dehumidification coil, the high humidity air flowing in a direction perpendicular to the dehumidification coil.
3. The purified air conditioning unit condensate energy recovery system of claim 2, wherein said condensate recovery tank is adapted to receive condensate from said dehumidification coil.
4. The purified air conditioning unit condensate energy recovery system of claim 1, wherein the condensate collection and lifting module further comprises a lifting water pump, an inlet end of the lifting water pump is in communication with the condensate recovery tank, and an outlet end of the lifting water pump is in communication with the condensate energy recovery module.
5. The system of claim 4, wherein the condensed water energy recovery module comprises a heat exchange tube, a water inlet of the heat exchange tube is communicated with the lift pump, and a water outlet of the heat exchange tube is communicated with the condensed water secondary utilization device.
6. The system of claim 5, wherein the heat exchange tube is a heat exchange coil.
7. The system of claim 6, wherein the heat exchanging coil is one of a copper tube, an aluminum tube, a stainless steel tube, and a plastic tube.
8. The system of claim 6, wherein the outer wall of the heat exchanging coil is a light pipe or the outer wall of the heat exchanging tube has heat exchanging fins.
9. The system according to claim 1, wherein a water level sensor is provided in the condensate recovery tank, and the water level sensor is configured to detect a water level in the condensate recovery tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322936884.9U CN221237973U (en) | 2023-10-31 | 2023-10-31 | Condensate energy recovery system for purifying air conditioning unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322936884.9U CN221237973U (en) | 2023-10-31 | 2023-10-31 | Condensate energy recovery system for purifying air conditioning unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221237973U true CN221237973U (en) | 2024-06-28 |
Family
ID=91596371
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322936884.9U Active CN221237973U (en) | 2023-10-31 | 2023-10-31 | Condensate energy recovery system for purifying air conditioning unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221237973U (en) |
-
2023
- 2023-10-31 CN CN202322936884.9U patent/CN221237973U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106592695B (en) | A kind of solar air water purifier | |
| CN209852020U (en) | Bus air conditioner condensate water recycling system | |
| CN221237973U (en) | Condensate energy recovery system for purifying air conditioning unit | |
| CN204644093U (en) | Novel sewage sludge drying device | |
| CN206538813U (en) | A kind of solar air water purifier | |
| CN205481610U (en) | Condensate recovery utilizes system | |
| CN110822768A (en) | Intelligent recovery system for waste hot water heat of residential area | |
| CN203848712U (en) | Novel cooling tower device capable of discharging sewage and removing impurities | |
| CN207196767U (en) | Multistage evaporation natural cooling air-conditioner set | |
| CN202561989U (en) | Air conditioner drainage system and air conditioner | |
| CN205170589U (en) | High corruption contains useless evaporation of water crystallization process system of salt | |
| CN205579795U (en) | Automatic cleaning system of air conditioning system air -cooled type off -premises station | |
| CN201874033U (en) | Split air pure water machine | |
| CN208635199U (en) | A kind of novel energy-saving split-type air conditioner without discharge water | |
| CN211178116U (en) | Cooling circulating water management equipment based on cooling tower | |
| CN212246569U (en) | Brewing cooling water recovery and waste heat utilization system | |
| CN212747066U (en) | Thick chloroethylene device of condensation | |
| CN201327250Y (en) | Energy-saving capacity-increase cleaning system of equipment room precision air conditioner | |
| CN210773522U (en) | Concurrent flow type evaporative condenser | |
| CN210832707U (en) | Dry-wet combined cooling circulating water system | |
| CN211953066U (en) | Air treatment device | |
| CN209819775U (en) | Rural domestic air conditioning system of tympanic bulla method evaporation heat exchange | |
| CN106197061B (en) | Cooling tower saturated vapor retracting device and apply its water-saving system | |
| CN209801888U (en) | multistage cooling circulation water device | |
| CN212610084U (en) | Multistage desulfurization waste water enrichment facility |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant |