Dehumidification system
By combining the dehumidification rotor and the temperature adjustment device, a cold source and a heat source are provided, which achieves efficient dehumidification and energy-saving effects of the dehumidification system, and solves the problems of high energy consumption and refrigerant pollution in the prior art.
Patent Information
- Application Number
- CN202422683145.8
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-11-05
- Publication Date
- 2025-08-29
- Estimated Expiration
- 2034-11-05
AI Technical Summary
In the existing commercial fresh air dehumidification system, compressor refrigeration and dehumidification have problems with small air volume, noise pollution and refrigerant pollution, while the PTC electric heating dehumidification of the rotor has high energy consumption and requires an additional cold source, resulting in an increase in energy consumption.
The dehumidification rotor is combined with a temperature adjustment device, and the cold source and heat source are provided through the cold water assembly and the hot water assembly respectively, so as to realize long-term circulating adsorption and desorption of the dehumidification rotor, reduce the humidity of the gas to be processed, increase the temperature of the regenerated gas, and reduce energy consumption.
It achieves efficient dehumidification, reduces energy consumption, solves the air volume limit of compressor refrigeration and dehumidification and the high energy consumption of rotor PTC electric heating, and avoids refrigerant pollution.
Smart Images

Figure CN223283159U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of fresh air dehumidification, in particular to a dehumidification system. Background Art
[0002] Currently, commercial fresh air dehumidification systems primarily use compressor-based refrigeration dehumidification or rotary PTC electric heating dehumidification. Compressor-based refrigeration dehumidification is primarily suitable for small air volumes and one-to-one use, limiting its scope of application. Furthermore, compressor-based refrigeration dehumidification is environmentally friendly due to the presence of refrigerants (fluorocarbons) and noise pollution from the compressor. Rotary PTC electric heating consumes relatively high energy and requires an additional cooling source to cool the fresh air, further increasing energy consumption. Utility Model Content
[0003] The purpose of the utility model is to provide a dehumidification system, which is used to enable the dehumidification wheel of the dehumidification system to perform long-term cyclic adsorption and desorption without separating the heat source or the cold source, thereby reducing energy consumption.
[0004] The purpose of this utility model is achieved by the following technical solutions:
[0005] The present application provides a dehumidification system, the dehumidification system comprising at least one dehumidifier and a temperature regulating device;
[0006] The dehumidifier comprises:
[0007] at least one desiccant wheel having a treatment zone and a regeneration zone;
[0008] a treatment adsorption air path, along which the gas to be treated flows, and through which the gas to be treated passes through the treatment area of the dehumidification wheel, for adsorbing and dehumidifying the gas to be treated;
[0009] at least one regeneration and desorption air passage, along which regeneration gas flows, and the regeneration and desorption air passage passes through the regeneration zone of the dehumidification rotor, for performing desorption and regeneration on the regeneration zone of the dehumidification rotor;
[0010] Among them, the temperature regulating device is used to cool down the gas to be treated and to heat up the regenerated gas respectively. After the gas to be treated flows through the temperature regulating device, it passes through the treatment area of the dehumidification wheel, which is used to dehumidify and adsorb the gas to be treated. After the regenerated gas flows through the temperature regulating device, it passes through the regeneration area of the dehumidification wheel, which is used to regenerate and desorb the regeneration area of the dehumidification wheel.
[0011] Preferably, the temperature regulating device comprises a cold water component and a hot water component, wherein the cold water component and the hot water component respectively have a flowing medium therein;
[0012] After the gas to be processed passes through the cold water component, the temperature of the gas to be processed decreases, and the flow medium in the cold water component increases;
[0013] After the regeneration gas passes through the hot water component, the temperature of the regeneration gas increases, and the flow medium in the hot water component decreases.
[0014] Preferably, the temperature regulating device comprises a chiller having an evaporation side and a condensation side;
[0015] The evaporation side of the chiller is arranged corresponding to the cold water component, for reducing the temperature of the medium inside the cold water component; the condensation side of the chiller is arranged corresponding to the hot water component, for increasing the temperature of the medium inside the hot water component.
[0016] Preferably, the temperature regulating device comprises a semiconductor module, wherein the semiconductor module has a cold end and a hot end;
[0017] The cold end of the semiconductor module is correspondingly arranged to the cold water component for reducing the temperature of the medium inside the cold water component; the hot end of the semiconductor module is correspondingly arranged to the hot water component for increasing the temperature of the medium inside the hot water component.
[0018] Preferably, the cold water component and / or the hot water component each have a circulating medium therein; and / or,
[0019] The medium is water.
[0020] Preferably, the cold water assembly includes a cold water tank, a refrigeration circulation pump and at least one first heat exchange component;
[0021] The medium inside the temperature regulating device is cooled inside the cold water tank, and the first heat exchange component is arranged on the processing adsorption air path on the air inlet side of the dehumidification wheel processing area;
[0022] Wherein, the refrigeration circulation pump transports the medium in the cold water tank to the first heat exchange component through a pipeline, and the medium inside the first heat exchange component flows back to the cold water tank through a pipeline; and / or,
[0023] The hot water assembly includes a hot water tank, a heating circulation pump and at least one second heat exchange component;
[0024] The medium inside the temperature regulating device is heated inside the hot water tank, and the second heat exchange component is arranged on the regeneration and desorption air path on the air inlet side of the regeneration zone of the dehumidification wheel;
[0025] The heating circulation pump transports the medium in the hot water tank to the second heat exchange component through a pipeline, and the medium in the second heat exchange component flows back to the hot water tank through a pipeline.
[0026] Preferably, the first heat exchange component is a refrigeration microchannel heat exchanger; and / or,
[0027] The second heat exchange component is a heating microchannel heat exchanger.
[0028] Preferably, the dehumidification system further comprises a first airflow driving component and at least one second airflow driving component;
[0029] The first airflow driving component is provided on the processing adsorption air path, and is used to make the gas to be processed flow in the processing adsorption air path;
[0030] The second airflow driving component is provided on the regeneration and desorption air path, and is used to make the regeneration gas flow in the regeneration and desorption air path; and / or,
[0031] The first airflow driving component and the second airflow driving component are both fans.
[0032] Preferably, the dehumidification system further comprises a first filter component and at least one second filter component;
[0033] The first filter component is arranged on the air inlet side of the treatment adsorption air path, and is used to filter impurities in the gas to be treated;
[0034] The second filter component is arranged on the air inlet side of the regeneration and desorption air path, and is used to filter impurities in the regeneration gas; and / or,
[0035] The first filter component and the second filter component are both filters.
[0036] Preferably, the dehumidification wheels share the treatment adsorption air path, and each of the dehumidification wheels has one regeneration desorption air path.
[0037] Compared with the prior art, the beneficial effects of the present invention include at least:
[0038] The temperature regulating device of the dehumidification system has both heating and cooling effects, and can cool and dehumidify the outdoor air. It can not only provide low-temperature air for the indoor room, but also reduce the humidity of the gas to be treated, provide the dehumidification wheel of the dehumidifier with gas with lower humidity, and reduce the dehumidification pressure of the dehumidification wheel treatment area. At the same time, the temperature regulating device can increase the temperature of the regenerated gas to meet the regeneration temperature of the dehumidification wheel regeneration zone, realize the desorption regeneration of the dehumidification wheel regeneration zone, and enable the dehumidification wheel of the dehumidification system to perform long-term cyclic adsorption and desorption without separating the heat source or the cold source separately, thereby reducing energy consumption.
[0039] Furthermore, the chiller can provide cold water and hot water to the cold water component and the hot water component respectively, providing a cold source for cooling the treated gas and a heat source for heating the regenerated gas respectively, making full use of the cold water and hot water generated by the chiller, which is more energy-efficient and solves the problems of small applicable air volume and limited scope of use due to one-to-one use of compressor refrigeration dehumidification.
[0040] The semiconductor module can cool down and heat up the medium flowing in the cold water component and the hot water component, respectively providing a cold source for cooling the treated gas and a heat source for heating the regenerated gas. The flowing medium is used to take away the cold at the cold end and the heat at the hot end of the semiconductor module, which can improve the operating efficiency of the semiconductor module and save energy. It solves the problem of high energy consumption caused by the use of rotary PTC electric heating for desorption in the regeneration zone, and there is no need to set up an additional cold source to cool the fresh air, further reducing energy consumption. At the same time, it can also solve the problem of environmental pollution and noise pollution caused by the refrigerant (fluorocarbon) in the use of compressor refrigeration and dehumidification. BRIEF DESCRIPTION OF THE DRAWINGS
[0041] Figure 1 This is a structural diagram of a dehumidification system provided by an embodiment of the present utility model;
[0042] Figure 2 This embodiment of the utility model Figure 1 A schematic diagram of the structure of a dehumidification wheel is added on the basis of FIG.
[0043] Figure 3 This utility model embodiment Figure 1 A schematic diagram of a structure in which multiple dehumidification wheels are added on the basis of FIG.
[0044] Figure 4 This is a structural diagram of another dehumidification system provided by an embodiment of the present utility model;
[0045] Figure 5 This embodiment of the utility model Figure 4 A structural diagram of a dehumidification wheel is added on the basis of FIG.
[0046] In the picture:
[0047] 1. Dehumidifier; 11. First dehumidification rotor; 12. Second dehumidification rotor;
[0048] 2. Chiller;
[0049] 3. Semiconductor module;
[0050] 4. Cold water tank; 401. First cold microchannel heat exchanger; 402. Second cold microchannel heat exchanger;
[0051] 5. Refrigeration circulation pump;
[0052] 6. Hot water tank; 601. First hot microchannel heat exchanger; 602. Second hot microchannel heat exchanger;
[0053] 7. Heating circulation pump;
[0054] 81. Processing fan; 82. First regeneration fan; 83. Second regeneration fan;
[0055] 91. First filter; 92. Second filter; 93. Third filter. DETAILED DESCRIPTION
[0056] Example embodiments will now be described more fully with reference to the accompanying drawings. However, the example embodiments can be implemented in many forms and should not be construed as limited to the embodiments set forth herein; rather, these embodiments are provided to make this disclosure more comprehensive and complete and to fully convey the concepts of the example embodiments to those skilled in the art. Identical reference numerals in the figures denote identical or similar structures, and thus repeated descriptions thereof will be omitted.
[0057] The words expressing positions and directions described in this utility model are all explained with reference to the accompanying drawings as examples, but they can be changed as needed, and all such changes are included in the protection scope of this utility model.
[0058] Reference Figures 1 to 5 The present application provides a dehumidification system, which includes at least one dehumidifier 1 and a temperature control device. The system includes: at least one dehumidification wheel, a treatment adsorption air path, at least one regeneration desorption air path and a temperature control device.
[0059] Specifically, the dehumidifier 1 includes at least one dehumidification rotor, a treatment adsorption air path, and at least one regeneration desorption air path. The dehumidification rotor has a treatment area and a regeneration area. One or more dehumidification rotors are provided. The dehumidification rotors can perform adsorption dehumidification on the gas to be treated in the treatment adsorption air path. When there are multiple dehumidification rotors, the gas to be treated in the treatment adsorption air path passes through multiple dehumidification rotors in sequence for adsorption dehumidification, which can improve the adsorption and dehumidification effect of the dehumidification system. At the same time, each dehumidification rotor has a regeneration desorption air path, which can perform desorption regeneration on the dehumidification rotor, ensuring that each dehumidification rotor regeneration zone maintains a good regeneration and desorption effect.
[0060] The gas to be treated flows along the treatment adsorption air path, which passes through the treatment area of the dehumidification wheel to adsorb and dehumidify the gas to be treated; the gas to be treated can be outdoor air, which can be transported indoors after adsorption and dehumidification through the treatment adsorption air path to provide dry gas for the indoor space.
[0061] The regeneration gas flows along the regeneration desorption air path, and the regeneration desorption air path passes through the regeneration zone of the dehumidification wheel, and is used to desorb and regenerate the regeneration zone of the dehumidification wheel; the regeneration gas can be indoor air, and the indoor air of the regeneration desorption air path passes through the regeneration zone of the dehumidification wheel to desorb and regenerate the regeneration zone of the dehumidification wheel, and the high-humidity air after desorption can be discharged to the outside.
[0062] Among them, the temperature regulating device is used to cool the gas to be treated and heat the regenerated gas respectively. The gas to be treated flows through the temperature regulating device and then passes through the treatment area of the dehumidification wheel for dehumidification and adsorption of the gas to be treated. The gas to be treated is cooled and dehumidified by the temperature regulating device, and then the low-temperature dry air is transported to the room through adsorption and dehumidification by the dehumidification wheel. The regenerated gas flows through the temperature regulating device and then passes through the regeneration area of the dehumidification wheel for regeneration and desorption of the regeneration area of the dehumidification wheel. The regenerated gas in the room is heated by the temperature regulating device, and the high-temperature regenerated gas flows through the regeneration area of the dehumidification wheel for desorption and regeneration of the regeneration area, and then the high-humidity regenerated gas is discharged to the outside.
[0063] Therefore, the temperature regulating device of the dehumidification system has both heating and cooling effects, and can cool and dehumidify the outdoor air. It can not only provide low-temperature air for the indoor room, but also reduce the humidity of the gas to be treated, and provide the dehumidification wheel of the dehumidifier 1 with gas with lower humidity, thereby reducing the dehumidification pressure of the dehumidification wheel treatment area. At the same time, the temperature regulating device can increase the temperature of the regenerated gas to meet the regeneration temperature of the dehumidification wheel regeneration zone, thereby realizing the desorption regeneration of the dehumidification wheel regeneration zone, so that the dehumidification wheel of the dehumidification system can perform long-term cyclic adsorption and desorption without separating the heat source or the cold source separately, thereby reducing energy consumption.
[0064] In a specific embodiment, the temperature regulating device has a cold water component and a hot water component, and the cold water component and the hot water component respectively have a flowing medium inside; as a preferred embodiment, the cold water component and / or the hot water component respectively have a circulating flowing medium inside, and the medium is preferably water, which has a large specific heat capacity and a low cost. Of course, other media in the existing technology can also be used, and this is not the only limitation here.
[0065] After the gas to be treated passes through the cold water component, the temperature of the gas to be treated decreases, and the flowing medium in the cold water component increases in temperature. The heated medium flows in the cold water component and cools down, so that the cold water component can continuously cool and dehumidify the gas to be treated.
[0066] After the regeneration gas passes through the hot water component, the regeneration gas is heated up, and the flowing medium in the hot water component is cooled down. The cooled medium flows in the hot water component and heats up, so that the hot water component can continuously heat the regeneration gas, thereby realizing continuous regeneration of the dehumidification wheel regeneration area.
[0067] In a specific embodiment, referring to Figure 1 and Figure 2 The temperature regulating device includes a chiller 2, which has an evaporation side and a condensation side; at this time, the medium flowing in the cold water component and the hot water component is water. The evaporation side of the chiller 2 is arranged corresponding to the cold water component, and is used to reduce the temperature of the medium inside the cold water component; the condensation side of the chiller 2 is arranged corresponding to the hot water component, and is used to increase the temperature of the medium inside the hot water component. As a result, the chiller 2 can provide cold water and hot water to the cold water component and the hot water component respectively, providing a cold source for cooling the gas to be treated and a heat source for heating the regenerated gas, respectively, making full use of the cold water and hot water generated by the chiller 2, which is more energy-efficient and solves the problems of small applicable air volume and limited scope of use due to one-to-one use of compressor refrigeration dehumidification.
[0068] like Figure 1 As shown, when the dehumidifier 1 of the dehumidification system has a dehumidification wheel, the cold water component on the evaporation side and the hot water component on the condensation side of the chiller 2 respectively provide corresponding cold source and heat source for the first dehumidification wheel 11 of the dehumidifier 1.
[0069] like Figure 2 As shown, in Figure 1 On the basis of the scheme shown, a dehumidifier wheel is added to the dehumidifier 1. At this time, the cold water component on the evaporation side and the hot water component on the condensation side of the chiller 2 respectively provide corresponding cold sources and heat sources for the first dehumidification wheel 11 and the second dehumidification wheel 12 of the dehumidifier 1.
[0070] In addition, if Figure 3 As shown, multiple dehumidifiers 1 can be added according to the power of the chiller 2. Each dehumidifier 1 can have one or more dehumidification wheels, so that corresponding cold sources and heat sources can be provided for more dehumidifiers 1 at the same time, making full use of the energy of the chiller 2.
[0071] In a specific embodiment, referring to Figure 4 and Figure 5The temperature regulating device includes a semiconductor module 3, which has a cold end and a hot end. The cold end of the semiconductor module 3 is arranged in correspondence with the cold water component to reduce the temperature of the medium inside the cold water component; the hot end of the semiconductor module 3 is arranged in correspondence with the hot water component to increase the temperature of the medium inside the hot water component. Thus, the semiconductor module 3 can cool down and heat up the medium flowing in the cold water component and the hot water component, respectively providing a cold source for cooling the gas to be treated and a heat source for heating the regenerated gas. The flowing medium is used to carry away the cold at the cold end and the heat at the hot end of the semiconductor module 3, thereby improving the operating efficiency of the semiconductor module 3 and saving more energy. This solves the problem of high energy consumption caused by the use of a rotary PTC electric heating method for desorption in the regeneration zone, and eliminates the need for an additional cold source to cool the fresh air, further reducing energy consumption. At the same time, it can also solve the problem of environmental pollution and noise pollution caused by the refrigerant (fluorocarbon) in the compressor refrigeration dehumidification.
[0072] like Figure 4 As shown, when the dehumidifier 1 of the dehumidification system has a dehumidification wheel, the cold water component at the cold end and the hot water component at the hot end of the semiconductor module 3 provide corresponding cold source and heat source for the first dehumidification wheel 11 of the dehumidifier 1 respectively.
[0073] like Figure 5 As shown, in Figure 4 A dehumidification wheel is added on the basis of the shown solution. At this time, the cold water component at the cold end and the hot water component at the hot end of the semiconductor module 3 respectively provide corresponding cold source and heat source for the first dehumidification wheel 11 and the second dehumidification wheel 12 of the dehumidifier 1.
[0074] In a specific embodiment, referring to Figure 1 、 Figure 2 、 Figure 4 and Figure 5 The cold water component includes a cold water tank 4, a refrigeration circulation pump 5 and at least one first heat exchange component. The first heat exchange component is preferably a refrigeration microchannel heat exchanger, and the number of the first heat exchange components is preferably equal to that of the dehumidification wheel; the medium inside the temperature regulating device is cooled inside the cold water tank 4, and the first heat exchange component is arranged on the treatment adsorption air path on the air inlet side of the dehumidification wheel treatment area, so that the gas to be treated is cooled and dehumidified before flowing through the dehumidification wheel treatment area; wherein, the refrigeration circulation pump 5 transports the medium in the cold water tank 4 to the first heat exchange component through a pipeline, and the medium inside the first heat exchange component returns to the cold water tank 4 through the pipeline, so that the low-temperature medium in the cold water tank 4 can pass through the first heat exchange component to cool and dehumidify the gas to be treated, and at the same time, the medium after heating in the first heat exchange component flows back to the cold water tank 4 for cooling again, thereby realizing the circulating refrigeration of the medium inside the cold water component and continuously cooling and dehumidifying the gas to be treated.
[0075] The hot water component includes a hot water tank 6, a heating circulation pump 7 and at least one second heat exchange component. The second heat exchange component is preferably a heating microchannel heat exchanger, and the number of the second heat exchange components is preferably equal to that of the dehumidification wheel; the medium inside the temperature regulating device is heated inside the hot water tank 6, and the second heat exchange component is arranged on the regeneration and desorption air path on the air inlet side of the dehumidification wheel regeneration zone, so that the regeneration gas is heated before flowing through the dehumidification wheel regeneration zone, and the temperature of the regeneration gas after heating can reach the regeneration and desorption temperature of the dehumidification wheel regeneration zone; wherein, the heating circulation pump 7 transports the medium in the hot water tank 6 to the second heat exchange component through a pipeline, and the medium inside the second heat exchange component flows back to the hot water tank 6 through the pipeline, so that the high-temperature medium in the hot water tank 6 can heat the regeneration gas through the second heat exchange component, and at the same time, the medium after cooling in the second heat exchange component flows back to the hot water tank 6 for heating again, thereby realizing the circulation heating of the medium inside the hot water component and continuously heating the regeneration gas.
[0076] Reference Figure 1 and Figure 4 When the dehumidifier 1 of the dehumidification system only has the first dehumidification wheel 11, the first heat exchange component is the first cold microchannel heat exchanger 401, and the second heat exchange component is the first hot microchannel heat exchanger 601. The refrigeration circulation pump 5 transports the low-temperature medium in the cold water tank 4 to the first cold microchannel heat exchanger 401 to cool and dehumidify the gas to be treated, and the heating circulation pump 7 transports the high-temperature medium in the hot water tank 6 to the first hot microchannel heat exchanger 601 to heat the regenerated gas.
[0077] Reference Figure 2 and Figure 4 When the dehumidifier 1 of the dehumidification system has a first dehumidification rotor 11 and a second dehumidification rotor 12, the first heat exchange component includes a first cold microchannel heat exchanger 401 and a second cold microchannel heat exchanger 402, and the second heat exchange component includes a first hot microchannel heat exchanger 601 and a second hot microchannel heat exchanger 602. The refrigeration circulation pump 5 transports the low-temperature medium in the cold water tank 4 to the first cold microchannel heat exchanger 401 and the second cold microchannel heat exchanger 402, and sequentially enters the treatment area of the first dehumidification rotor 11 and the second dehumidification rotor 12. The gas to be treated on the side is cooled and dehumidified. The use of a two-stage wheel for dehumidification can improve the efficiency of the wheel dehumidification, so that the gas discharged from the adsorption air path is drier and meets the humidity requirements of the room; the heating circulation pump 7 transports the high-temperature medium in the hot water tank 6 to the first hot microchannel heat exchanger 601 and the second hot microchannel heat exchanger 602, and heats the regeneration gas in the regeneration and desorption air paths of the first dehumidification wheel 11 and the second dehumidification wheel 12 respectively, so that both dehumidification wheels have better regeneration and desorption effects.
[0078] It should be noted that if Figure 1 、 Figure 2 and Figure 3In the equipment used in the temperature regulating device, the chiller 2 is used as the cold source and heat source. When the medium inside the cold water tank 4 and the hot water tank 6 is water, the cold water tank 4 and the hot water tank 6 can be directly connected to the evaporation side and the condensation side of the chiller 2, so that the chiller 2 can use the cold water tank 4 and the hot water tank 6 to produce cold water and hot water, that is, the chiller 2 directly produces cold water and hot water to cool and dehumidify the to-be-treated gas in the adsorption air path and to heat the regenerated gas in the regeneration desorption air path. Compared with the indirect heat conduction between the cold water tank 4 and the hot water tank 6 and the chiller 2, the energy utilization efficiency of the chiller 2 can be improved, and more energy-saving.
[0079] In a specific embodiment, referring to Figure 1 、 Figure 2 、 Figure 4 and Figure 5 The dehumidification system further includes a first airflow driving component and at least one second airflow driving component; wherein the first airflow driving component and the second airflow driving component are preferably fans, and the number of the second airflow driving components is preferably equal to the number of the dehumidification wheels.
[0080] The first airflow driving component is arranged on the treatment adsorption air path, and is used to make the gas to be treated flow in the treatment adsorption air path, thereby providing power for the gas to be treated to overcome the resistance of the treatment adsorption air path; the second airflow driving component is arranged on the regeneration desorption air path, and is used to make the regeneration gas flow in the regeneration desorption air path, thereby providing power for the regeneration gas to overcome the resistance of the regeneration desorption air path.
[0081] It should be noted that in Figure 1 and Figure 4 In the embodiment, the first air flow driving component is a processing fan 81, and the second air flow driving component includes a first regeneration fan 82; Figure 2 and Figure 5 In the figure, the first airflow driving component is the processing fan 81, and the second airflow driving component includes a first regeneration fan 82 and a second regeneration fan 83. The two regeneration fans are respectively used to drive the regeneration gas flow in the regeneration and desorption air paths of the two dehumidification wheels.
[0082] In a specific embodiment, referring to Figure 1 、 Figure 2 、 Figure 4 、 Figure 5 The dehumidification system further includes a first filter component and at least one second filter component; wherein the first filter component and the second filter component are both filters, and the number of the second filter components is preferably equal to the number of the dehumidification wheels.
[0083] The first filter component is arranged on the air inlet side of the treatment adsorption air path, and is used to filter impurities in the gas to be treated; the second filter component is arranged on the air inlet side of the regeneration desorption air path, and is used to filter impurities in the regeneration gas.
[0084] It should be noted that in Figure 1 and Figure 4 In the embodiment, the first filter component is a first filter 91, and the second filter component includes a second filter 92; Figure 2 and Figure 5 In the embodiment, the first filter component is a first filter 91, and the second filter component includes a second filter 92 and a third filter 93. The first filter 91 is preferably arranged on the air inlet side of the first cold microchannel heat exchanger 401 to filter impurities such as particles in the gas to be treated entering the adsorption air path. The second filter 92 and the third filter 93 are preferably arranged on the air inlet side of the first hot microchannel heat exchanger 601 and the air inlet side of the second hot microchannel heat exchanger 602 to filter impurities such as particles in the regeneration gas entering the regeneration desorption air path.
[0085] Although the embodiments of the present invention have been shown and described above, it can be understood that the above embodiments are illustrative and cannot be understood as limiting the present invention. Ordinary technicians in this field can change, modify, replace and modify the above embodiments within the scope of the utility model without departing from the principles and purpose of the utility model. All of these changes should fall within the scope of protection of the claims of the present invention.
Claims
1. A dehumidification system, characterized in that: The dehumidification system includes at least one dehumidifier and a temperature regulating device; The dehumidifier comprises: at least one desiccant wheel having a treatment zone and a regeneration zone; a treatment adsorption air path, along which the gas to be treated flows, and through which the gas to be treated passes through the treatment area of the dehumidification wheel, for adsorbing and dehumidifying the gas to be treated; at least one regeneration and desorption air passage, along which regeneration gas flows, and the regeneration and desorption air passage passes through the regeneration zone of the dehumidification rotor, for performing desorption and regeneration on the regeneration zone of the dehumidification rotor; Among them, the temperature regulating device is used to cool down the gas to be treated and to heat up the regenerated gas respectively. After the gas to be treated flows through the temperature regulating device, it passes through the treatment area of the dehumidification wheel, which is used to dehumidify and adsorb the gas to be treated. After the regenerated gas flows through the temperature regulating device, it passes through the regeneration area of the dehumidification wheel, which is used to regenerate and desorb the regeneration area of the dehumidification wheel.
2. The dehumidification system according to claim 1, characterized in that: The temperature regulating device comprises a cold water component and a hot water component, wherein the cold water component and the hot water component respectively have a flowing medium therein; After the gas to be processed passes through the cold water component, the temperature of the gas to be processed decreases, and the flow medium in the cold water component increases; After the regeneration gas passes through the hot water component, the temperature of the regeneration gas increases, and the flow medium in the hot water component decreases.
3. The dehumidification system according to claim 2, characterized in that: The temperature regulating device includes a chiller having an evaporation side and a condensation side; The evaporation side of the chiller is arranged corresponding to the cold water component, for reducing the temperature of the medium inside the cold water component; the condensation side of the chiller is arranged corresponding to the hot water component, for increasing the temperature of the medium inside the hot water component.
4. The dehumidification system according to claim 2, characterized in that: The temperature regulating device includes a semiconductor module having a cold end and a hot end; The cold end of the semiconductor module is correspondingly arranged to the cold water component for reducing the temperature of the medium inside the cold water component; the hot end of the semiconductor module is correspondingly arranged to the hot water component for increasing the temperature of the medium inside the hot water component.
5. The dehumidification system according to claim 2, characterized in that: The cold water component and / or the hot water component each have a circulating medium therein; and / or, The medium is water.
6. The dehumidification system according to claim 5, characterized in that: The cold water assembly includes a cold water tank, a refrigeration circulation pump and at least one first heat exchange component; The medium inside the temperature regulating device is cooled inside the cold water tank, and the first heat exchange component is arranged on the processing adsorption air path on the air inlet side of the dehumidification wheel processing area; Wherein, the refrigeration circulation pump transports the medium in the cold water tank to the first heat exchange component through a pipeline, and the medium inside the first heat exchange component flows back to the cold water tank through a pipeline; and / or, The hot water assembly includes a hot water tank, a heating circulation pump and at least one second heat exchange component; The medium inside the temperature regulating device is heated inside the hot water tank, and the second heat exchange component is arranged on the regeneration and desorption air path on the air inlet side of the regeneration zone of the dehumidification wheel; The heating circulation pump transports the medium in the hot water tank to the second heat exchange component through a pipeline, and the medium in the second heat exchange component flows back to the hot water tank through a pipeline.
7. The dehumidification system according to claim 6, characterized in that: The first heat exchange component is a refrigeration microchannel heat exchanger; and / or, The second heat exchange component is a heating microchannel heat exchanger.
8. The dehumidification system according to claim 7, characterized in that: The dehumidification system further includes a first airflow driving component and at least one second airflow driving component; The first airflow driving component is provided on the processing adsorption air path, and is used to make the gas to be processed flow in the processing adsorption air path; The second airflow driving component is provided on the regeneration and desorption air path, and is used to make the regeneration gas flow in the regeneration and desorption air path; and / or, The first airflow driving component and the second airflow driving component are both fans.
9. The dehumidification system according to claim 1, characterized in that: The dehumidification system further includes a first filter component and at least one second filter component; The first filter component is arranged on the air inlet side of the treatment adsorption air path, and is used to filter impurities in the gas to be treated; The second filter component is arranged on the air inlet side of the regeneration and desorption air path, and is used to filter impurities in the regeneration gas; and / or, The first filter component and the second filter component are both filters.
10. The dehumidification system according to claim 1, characterized in that: The dehumidification wheels share the treatment adsorption air path, and each of the dehumidification wheels has one regeneration desorption air path.