CN102261701A - Multilevel heat recovery composite dehumidifying fresh air treatment machine - Google Patents
Multilevel heat recovery composite dehumidifying fresh air treatment machine Download PDFInfo
- Publication number
- CN102261701A CN102261701A CN2011101211294A CN201110121129A CN102261701A CN 102261701 A CN102261701 A CN 102261701A CN 2011101211294 A CN2011101211294 A CN 2011101211294A CN 201110121129 A CN201110121129 A CN 201110121129A CN 102261701 A CN102261701 A CN 102261701A
- Authority
- CN
- China
- Prior art keywords
- heat pump
- heat recovery
- runner
- temperature heat
- air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000011084 recovery Methods 0.000 title claims abstract description 34
- 239000002131 composite material Substances 0.000 title claims abstract 3
- 230000008929 regeneration Effects 0.000 claims abstract description 39
- 238000011069 regeneration method Methods 0.000 claims abstract description 39
- 150000001875 compounds Chemical class 0.000 claims abstract description 16
- 238000007791 dehumidification Methods 0.000 claims abstract description 15
- 238000001816 cooling Methods 0.000 claims abstract description 10
- 238000001035 drying Methods 0.000 claims abstract description 10
- 238000006243 chemical reaction Methods 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims 5
- 230000006835 compression Effects 0.000 claims 1
- 238000007906 compression Methods 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract description 18
- 238000004378 air conditioning Methods 0.000 abstract description 10
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 230000001172 regenerating effect Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 7
- 239000003507 refrigerant Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000008676 import Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000001413 cellular effect Effects 0.000 description 2
- 239000002274 desiccant Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000008520 organization Effects 0.000 description 2
- 238000007664 blowing Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 208000011580 syndromic disease Diseases 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Images
Landscapes
- Drying Of Gases (AREA)
- Central Air Conditioning (AREA)
Abstract
本发明公开了一种多级热回收复合除湿新风处理机，包括依次通过风管串联连接板式热交换器、预冷除湿器、干燥转轮、显热回收转轮、送风温度调节器、送风风机构成的处理风路径；以及依次串联蒸发冷却器、板式热交换器、显热回收转轮、低温热泵热回收器、高温热泵冷凝器、干燥转轮、高温热泵蒸发器、再生风机构成的再生风路径。本发明通过多级热回收，减少再生空气的加热能耗和处理空气的冷却能耗，达到节能的目的，同时，两级复合除湿，能有效提高机组的除湿能力，可应用于各种公共建筑、商业建筑、工业建筑的夏季空调和冬季供暖，适合于大型中央空调系统的新风处理，尤其适合于闷热潮湿地区的温湿度独立控制空调系统的新风处理。
The invention discloses a multi-stage heat recovery compound dehumidification fresh air processor, which comprises a plate heat exchanger, a precooling dehumidifier, a drying wheel, a sensible heat recovery wheel, a temperature regulator for air supply, The processing air path composed of the air fan; and the sequentially connected evaporative cooler, plate heat exchanger, sensible heat recovery runner, low-temperature heat pump heat recovery device, high-temperature heat pump condenser, drying runner, high-temperature heat pump evaporator, and regenerative fan Regeneration wind path. The invention reduces the heating energy consumption of regeneration air and the cooling energy consumption of air treatment through multi-stage heat recovery, so as to achieve the purpose of energy saving. At the same time, the two-stage composite dehumidification can effectively improve the dehumidification capacity of the unit, and can be applied to various public buildings , summer air conditioning and winter heating of commercial buildings and industrial buildings, suitable for fresh air treatment of large central air conditioning systems, especially suitable for fresh air treatment of air conditioning systems with independent temperature and humidity control in hot and humid areas.
Description
Technical field
The present invention relates to air processor, specifically is the new wind air processing machine of the compound dehumidifying of a kind of multistage recuperation of heat.
Background technology
The consumption of energy savings reduces the discharging of environmental contaminants, realizes the sustainable development of the energy, is the common topic of paying close attention in the world today.Building energy consumption occupies sizable ratio in social total energy consumption, in China, therefore this ratio, reduces building energy consumption and become one of vital task of China's energy-saving and emission-reduction near 30%.Air conditioning energy consumption is the main body of building energy consumption, saves air conditioning energy consumption, and especially air conditioner fresh air is handled energy consumption, is the effective way that realizes building energy conservation.
It is the main flow form of following air conditioning mode that humiture is independently controlled, and it is by separating air-conditioning temperature-reducing and dehumidifying, and the traditional air-conditioning system energy consumption is big, the shortcoming of air quality difference thereby overcome.Realize that humiture independently controls, need provide dry nice and cool outdoor fresh air for building.For sultry humid area, the moisture removal that new wind requires is big, adopt traditional dehumidification by condensation, though can guarantee the moisture removal that requires, but the refrigerant temperature that requires is low, cause refrigeration system because of the performance energy consumption that descends increases, will inevitably cause new wind to cross cold and needs heat more simultaneously, further increased air conditioner fresh air processing energy consumption.Though and employing single-stage runner desiccant dehumidification can not cause new wind cold excessively, is difficult to meet the requirements of moisture removal usually, perhaps the regeneration temperature of Yao Qiuing is very high, increases the regeneration energy consumption greatly.
Comprehensively described, prior art has the following disadvantages: 1, Chang Gui single-stage rotary wheel dehumidifying regeneration temperature height, adopt other low-grade energies such as solar energy, waste heat to be difficult to reach its regeneration temperature requirement, the high-grade energy such as needs use electric energy are finished thermal regeneration, and energy resource consumption is bigger.2, the single-stage rotary wheel dehumidifying is limited in one's ability, is difficult to satisfy sultry humid area and realizes that humiture independently controls the requirement to the fresh air dehumidification ability.3, there is low, the shortcoming cold, that energy consumption is big of blowing of refrigerating efficiency in dehumidification by condensation.
Summary of the invention
In order to solve the problems of the technologies described above, the invention provides the new wind air processing machine of the compound dehumidifying of multistage recuperation of heat that a kind of energy consumption is low, efficient is high.
The technical scheme that the present invention addresses the above problem is: comprise devaporizer, heat-exchangers of the plate type, the precooling dehumidifier, dry runner, sensible heat reclaims runner, the wind pushing temperature adjuster, breeze fan, the hot pump in low temp heat regenerator, the high temperature heat pump condenser, the high temperature heat pump compressor, the high temperature heat pump evaporimeter, the high temperature heat pump expansion valve, the regeneration blower fan, first control valve, second control valve, four-port conversion value, the hot pump in low temp compressor, the hot pump in low temp expansion valve, bypath valve, the bypass air channel; Described heat-exchangers of the plate type, precooling dehumidifier, dry runner, sensible heat reclaim runner, wind pushing temperature adjuster, breeze fan and are connected in series formation processing wind path directly by airduct successively; Described devaporizer, heat-exchangers of the plate type, sensible heat recovery runner, hot pump in low temp heat regenerator, high temperature heat pump condenser, dry runner, high temperature heat pump evaporimeter, regeneration blower fan are followed in series to form regeneration wind path footpath; Between described precooling dehumidifier and the wind pushing temperature adjuster is relation in parallel, and first control valve, second control valve are housed on the parallel branch, and after the two branch road parallel connections, its two ends are connected with the A port of hot pump in low temp expansion valve, four-port conversion value respectively; Described hot pump in low temp heat regenerator is connected with C port, the hot pump in low temp expansion valve of four-port conversion value respectively by pipeline; Described hot pump in low temp compressor is connected between the D port and B port of four-port conversion value; High temperature heat pump evaporimeter, high temperature heat pump compressor, high temperature heat pump condenser, high temperature heat pump expansion valve are connected closed the connection successively.
In the compound dehumidifying fresh air processor of above-mentioned multistage recuperation of heat, described dry runner is divided into dry runner treatment region and dry rotary wheel regeneration district, and it respectively accounts for 180 ° fan section.
In the compound dehumidifying fresh air processor of above-mentioned multistage recuperation of heat, it is cellular rotary heat exchanger that described sensible heat reclaims runner, is divided into sensible heat and reclaims runner treatment region and sensible heat recovery runner exhaust zone, and it respectively accounts for 180 ° fan section.
In the compound dehumidifying fresh air processor of above-mentioned multistage recuperation of heat, sensible heat reclaim runner treatment region side and sensible heat reclaims runner exhaust zone side, between import of precooling dehumidifier and dry runner treatment region side outlet, between high temperature heat pump condenser inlet and high temperature heat pump evaporator outlet, be respectively equipped with bypass air channel and by-passing valve.
In the compound dehumidifying fresh air processor of above-mentioned multistage recuperation of heat, described breeze fan and regeneration blower fan are the frequency control blower fan.
In the compound dehumidifying fresh air processor of above-mentioned multistage recuperation of heat, described precooling dehumidifier is a surface-type heat exchanger, and the bottom is provided with the condensate water gathering-device.
In the compound dehumidifying fresh air processor of above-mentioned multistage recuperation of heat, described heat-exchangers of the plate type is the distributary air-air heat exchanger; Devaporizer is for realizing the direct evaporative cooler or the wet-membrane humidifier of equal-enthalpy humidifying.
Technique effect of the present invention is: 1) the present invention organically combines dehumidification by condensation and rotary wheel dehumidifying, has improved the dehumidifying effect of system, can reduce the regeneration temperature of runner simultaneously, and the cold excessively situation of new wind can not occur; 2) the present invention uses multistage recuperation of heat dexterously, realizes that the step of energy is recycled, and reduces the energy consumption for cooling of the new wind of summer condition and the heating energy consumption of regeneration air, reduces the new wind heating energy consumption of winter condition simultaneously; 3) the present invention does not need other auxiliary thermal source to carry out desiccant regeneration except that the certain electric energy of blower fan, heat pump consumption.
The present invention can be applicable to the summer air-conditioning and the heat supply in winter of various public buildings, commercial building, industrial building, and the new wind that is suitable for large-scale central air conditioner system is handled, and the new wind that is particularly suitable for the humiture independence control air conditioner system of sultry humid area is handled.
Description of drawings
Fig. 1 is a structural representation of the present invention;
Fig. 2 is that sensible heat reclaims runner partitioned organization schematic diagram among Fig. 1;
Fig. 3 is a dry runner partitioned organization schematic diagram among Fig. 1;
Fig. 4 is a summer condition operational process schematic diagram;
Fig. 5 is a winter condition operational process schematic diagram.
The specific embodiment
Below in conjunction with accompanying drawing, the present invention is described in further detail.
Referring to Fig. 1, the present invention includes devaporizer 1, heat-exchangers of the plate type 2, precooling dehumidifier 3, dry runner 4, sensible heat recovery runner 5, wind pushing temperature adjuster 6, breeze fan 7, hot pump in low temp heat regenerator 8, high temperature heat pump condenser 9, high temperature heat pump compressor 10, high temperature heat pump evaporimeter 11, high temperature heat pump expansion valve 12, regeneration blower fan 13, first control valve 14, second control valve 15, four-port conversion value 16, hot pump in low temp compressor 17, hot pump in low temp expansion valve 18, bypath valve 19, bypass air channel 20.
Described heat-exchangers of the plate type 2, precooling dehumidifier 3, dry runner 4, sensible heat reclaim runner 5, wind pushing temperature adjuster 6, breeze fan 7 and are connected in series formation processing wind path directly by airduct successively; Described devaporizer 1, heat-exchangers of the plate type 2, sensible heat recovery runner 5, hot pump in low temp heat regenerator 8, high temperature heat pump condenser 9, dry runner 4, high temperature heat pump evaporimeter 11, regeneration blower fan 13 are followed in series to form regeneration wind path footpath; Between described precooling dehumidifier 3 and the wind pushing temperature adjuster 6 is relation in parallel, is equipped with on the parallel branch after first control valve 14,15, the two branch road parallel connections of second control valve, and its two ends are connected with the A port of hot pump in low temp expansion valve 18, four-port conversion value 16 respectively; Described hot pump in low temp heat regenerator 8 is connected with C port, the hot pump in low temp expansion valve 18 of four-port conversion value 16 respectively by pipeline; Described hot pump in low temp compressor 17 is connected between the D port and B port of four-port conversion value 16; High temperature heat pump evaporimeter 11, high temperature heat pump compressor 10, high temperature heat pump condenser 9, high temperature heat pump expansion valve 12 are connected closed the connection successively.
It is cellular rotary heat exchanger that sensible heat among the present invention reclaims runner 5, be divided into sensible heat and reclaim runner exhaust zone 23 and sensible heat recovery runner treatment region 24, sensible heat reclaims runner exhaust zone 23 and sensible heat recovery runner treatment region 24 respectively accounts for 180 ° fan section, as shown in Figure 2.
Dry runner 4 among the present invention is divided into dry rotary wheel regeneration district 25 and dry runner treatment region 26, and dry runner treatment region 25 and dry rotary wheel regeneration district 26 respectively account for 180 ° fan section, as shown in Figure 3.
Processing wind path footpath concrete structure among the present invention is: outdoor new wind inlet duct 21 links to each other with the new wind side-entrance of heat-exchangers of the plate type 2, the new wind side outlet of heat-exchangers of the plate type 2 is connected with precooling dehumidifier 3 by airduct, and described precooling dehumidifier 3 is provided with the condensate water gathering-device for surface-type heat exchanger and bottom.Precooling dehumidifier 3 is connected by airduct with dry runner treatment region 26 again, and dry runner treatment region 26 opposite sides directly are connected with sensible heat recovery runner treatment region 24 by airduct.The opposite side that sensible heat reclaims runner treatment region 24 is connected with wind pushing temperature adjuster 6, and wind pushing temperature adjuster 6 links to each other with breeze fan 7 again, and breeze fan 7 links to each other with air-conditioned room by ajutage again.
Regeneration wind path footpath concrete structure among the present invention is: building exhaust duct 22 is connected with devaporizer 1, devaporizer 1 is connected with the air draft side-entrance of heat-exchangers of the plate type 2 by airduct, the wind exhausting outlet of heat-exchangers of the plate type 2 is connected by airduct with the exhaust zone that sensible heat reclaims runner 5, the exhaust zone opposite side that sensible heat reclaims runner 5 and hot pump in low temp heat regenerator 8 are connected by airduct, hot pump in low temp heat regenerator 8 is connected with high temperature heat pump condenser 9 by airduct, high temperature heat pump condenser 9 is connected to dry rotary wheel regeneration district 25 by airduct, the opposite side in dry rotary wheel regeneration district 25 is connecting high temperature heat pump evaporimeter 11 by airduct, and the high temperature heat pump evaporimeter is connected to regeneration blower fan 13.
The high temperature heat pump evaporimeter 11 in addition, high temperature heat pump compressor 10, and high temperature heat pump condenser 9, high temperature heat pump expansion valve 12 is connected into the loop successively, forms the high temperature heat pump heat recovery system.Between precooling dehumidifier 3 and the wind pushing temperature adjuster 6 is relation in parallel, and each branch road is equipped with control valve 1 respectively, control valve 2 15, and after the two branch road parallel connections, its two ends connect the A port of hot pump in low temp expansion valve 18, four-port conversion value 16 respectively; Hot pump in low temp heat regenerator 8 is connected with C port, the hot pump in low temp expansion valve 18 of four-port conversion value 16 respectively by pipeline; Hot pump in low temp compressor 17 is connected between the D port and B port of four-port conversion value 16.
Secondly reclaim runner treatment region side and sensible heat recovery runner exhaust zone side at sensible heat, between 3 imports of precooling dehumidifier and the dry runner treatment region side outlet, between the outlet of the import of high temperature heat pump condenser 9 and high temperature heat pump evaporimeter 11, be respectively equipped with bypass air channel 20 and by-passing valve 19.
Summer air-conditioning embodiment:
As shown in Figure 4, air handling process is: when outdoor high temperature high humidity fresh air (processing air) draws down taking out of breeze fan 7, form new wind by outdoor new wind inlet duct 21 and enter heat-exchangers of the plate type 2, carry out indirect sensible heat exchange with the building air draft after lowering the temperature through evaporative cooling, temperature reduces, enter precooling dehumidifier 3 afterwards, further cooled off by low-temperature refrigerant, and tentatively dehumidify from hot pump in low temp system.Fresh air after the preliminary dehumidifying enters dry runner 4, and by further dry, simultaneous temperature raises.Dried fresh air enters sensible heat and reclaims runner 5, carried out preliminary sensible heat precooling from the building air draft of heat-exchangers of the plate type 2, through wet cooling such as wind pushing temperature adjuster 6 is further, meet the requirements of wind pushing temperature, then after breeze fan 7 is sent into air-conditioned room.Wherein breeze fan 7 adopts the frequency control blower fan, adjusts rotation speed of fan according to duct resistance in running, with the air quantity and the blast of satisfying the demand.
As shown in Figure 4, building air draft processing procedure is: relatively dry nice and cool building air draft (regeneration air) is drawn down taking out of regeneration blower fan 13, form air draft by building exhaust duct 22 and enter devaporizer 1, carry out the equal-enthalpy humidifying cooling therein, absorb the heat of new wind then in heat-exchangers of the plate type 2, temperature raises slightly, enters the exhaust zone that sensible heat reclaims runner 5 then, further carry out heat exchange with new wind, temperature further raises.Air draft after preliminary the intensification successively enters hot pump in low temp heat regenerator 8, high temperature heat pump condenser 9, respectively by the high temperature refrigerant steam heated from hot pump in low temp and high temperature heat pump, reaches the regeneration temperature of runner therein.The regeneration air of high temperature drying enters dry rotary wheel regeneration district 25, and the drier in the dry runner 4 is regenerated, and recovers the dehumidifying effect of drier.Enter high temperature heat pump evaporimeter 11 through the regeneration air after the renewing zone, its heat energy is passed to low-temperature refrigerant in the high temperature heat pump evaporimeter 11, by high temperature heat pump system this part energy is passed to regeneration air before the dry runner 4 again.Enter atmosphere through the regeneration air after the high temperature heat pump evaporimeter 11 through regeneration blower fan 13.The blower fan 13 of wherein regenerating adopts the frequency control blower fan, and it can adjust rotation speed of fan according to duct resistance, with the air quantity and the blast of satisfying the demand.
The winter heating embodiment:
In the winter time under the operational mode, devaporizer 1, precooling dehumidifier 3, dry runner 4, sensible heat reclaim runner 5, high temperature heat pump heat recovery system all with out of service as shown in Figure 5.
Air handling process is: outdoor fresh cold air enters heat-exchangers of the plate type 2, carries out heat exchange with the higher indoor exhaust wind of temperature from building, and temperature raises.Fresh air after the preliminary preheating enters wind pushing temperature adjuster 6 through by-pass line, is arrived wind pushing temperature by the high temperature refrigerant steam heated from hot pump in low temp, sends into indoor through breeze fan 7 then.
Building air draft processing procedure is: the building air draft is passed to new wind through heat-exchangers of the plate type 2 with energy, and temperature reduces, and enters hot pump in low temp heat regenerator 8 through by-pass line 20 then, further heat energy is passed to new wind, improves new wind-warm syndrome degree.By-pass line 20 is passed through in air draft through hot pump in low temp heat regenerator 8 again, enters atmosphere by regeneration blower fan 13.
Above content described in this specification only is to structure example of the present invention explanation.The various modifications that specific embodiments described in the invention is made, replenish, perhaps adopt similar mode to replace, only otherwise depart from structure of the present invention, perhaps do not surmount the defined scope of these claims, all should belong to protection scope of the present invention.
Claims (7)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110121129 CN102261701B (en) | 2011-05-11 | 2011-05-11 | Multilevel heat recovery composite dehumidifying fresh air treatment machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201110121129 CN102261701B (en) | 2011-05-11 | 2011-05-11 | Multilevel heat recovery composite dehumidifying fresh air treatment machine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102261701A true CN102261701A (en) | 2011-11-30 |
| CN102261701B CN102261701B (en) | 2013-06-19 |
Family
ID=45008442
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201110121129 Expired - Fee Related CN102261701B (en) | 2011-05-11 | 2011-05-11 | Multilevel heat recovery composite dehumidifying fresh air treatment machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102261701B (en) |
Cited By (29)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102705205A (en) * | 2012-05-28 | 2012-10-03 | 深圳百时得能源环保科技有限公司 | Pre-treating and variable-flow device of air compression system |
| CN102927627A (en) * | 2012-11-05 | 2013-02-13 | 江苏国莱特空调设备有限公司 | Condensation heat recovery type movable temperature and humidity control device |
| CN103836736A (en) * | 2014-02-10 | 2014-06-04 | 三湘股份有限公司 | Intelligent fresh air purification and full heat exchange equipment and control method thereof |
| CN104792065A (en) * | 2014-12-19 | 2015-07-22 | 上海伯涵热能科技有限公司 | Heat pump system for heating drying medium and recovering waste heat in stepped mode |
| CN104984636A (en) * | 2015-06-18 | 2015-10-21 | 彭福明 | A high-efficiency heat pump dehumidifier |
| CN108027155A (en) * | 2015-09-30 | 2018-05-11 | 株式会社前川制作所 | Dehumanization method and dehydrating unit |
| CN108489251A (en) * | 2018-06-11 | 2018-09-04 | 南京农业大学 | A kind of pump type heat low-temperature circulating formula crop dryer of waste heat recoverable |
| CN108499327A (en) * | 2018-03-21 | 2018-09-07 | 东南大学 | A kind of adjustable high-pressure solution dehumidifying of pressure leak source and waste-heat recovery device and method |
| CN109959099A (en) * | 2019-04-22 | 2019-07-02 | 山西阳旭新能源科技有限公司 | A kind of Multi-functional dehumidifying fresh air waste heat recycling hot water air conditioning device |
| CN110375395A (en) * | 2019-08-13 | 2019-10-25 | 河南中瑞制冷科技有限公司 | Industrial combined type depth dehumidification system |
| CN110375396A (en) * | 2019-08-13 | 2019-10-25 | 河南中瑞制冷科技有限公司 | A kind of large size depth dehumidification system and its working method |
| CN110454878A (en) * | 2019-08-08 | 2019-11-15 | 江苏苏净集团有限公司 | An energy-saving rotary dehumidifier |
| CN110594919A (en) * | 2019-09-29 | 2019-12-20 | 北京四季通能源科技有限公司 | Air source heat pump system and control method thereof |
| CN110678248A (en) * | 2017-03-24 | 2020-01-10 | 马西莫·维琴蒂尼 | Apparatus and method for producing water |
| CN111102661A (en) * | 2020-01-10 | 2020-05-05 | 同济大学 | An energy-saving variable dehumidification heat pump type rotary dehumidifier unit and its control method |
| WO2021114715A1 (en) * | 2019-12-13 | 2021-06-17 | 艾默生环境优化技术(苏州)有限公司 | Runner dehumidification device regeneration system and runner dehumidification device |
| CN112984649A (en) * | 2019-12-13 | 2021-06-18 | 艾默生环境优化技术(苏州)有限公司 | Regeneration system of rotating wheel dehumidification equipment and rotating wheel dehumidification equipment |
| CN113007821A (en) * | 2021-04-12 | 2021-06-22 | 海南大学 | Indoor dehumidification method realized through window |
| CN113028524A (en) * | 2021-04-05 | 2021-06-25 | 西安科技大学 | Multi-split type solid dehumidification multifunctional air conditioning system and application method thereof |
| CN113154551A (en) * | 2021-05-12 | 2021-07-23 | 慧湿环境科技（上海）有限公司 | Hot water type low-temperature regeneration rotating wheel dehumidification fresh air system of high-temperature heat pump |
| CN113218012A (en) * | 2020-07-09 | 2021-08-06 | 中国建筑科学研究院有限公司 | Anti-frosting fresh air heat recovery device and control method thereof |
| CN113566322A (en) * | 2021-08-04 | 2021-10-29 | 西安科技大学 | A kind of multi-energy complementary dehumidification rotary air conditioning system and using method thereof |
| CN113905804A (en) * | 2019-06-12 | 2022-01-07 | 阿特拉斯·科普柯空气动力股份有限公司 | Compressor system and method for supplying compressed gas |
| CN114165860A (en) * | 2021-12-13 | 2022-03-11 | 必信能源科技(苏州)有限公司 | Heat pump regeneration system for rotary wheel dehumidification |
| CN114543216A (en) * | 2022-02-28 | 2022-05-27 | 深圳市德尼环境技术有限公司 | Waste heat recovery type energy-saving dehumidification air conditioner |
| CN115143546A (en) * | 2022-06-13 | 2022-10-04 | 武汉理工大学 | Method for realizing joint control of pollutants by using double-layer composite rotary air-conditioning system |
| CN116294542A (en) * | 2023-03-02 | 2023-06-23 | 东南大学 | A full-condition composite dehumidification system for suspension bridge main cables based on waste heat recovery |
| CN118310105A (en) * | 2024-04-18 | 2024-07-09 | 广东海洋大学 | Evaporative cooling device and method for heat-driven rotary dehumidification |
| CN118729515A (en) * | 2024-08-27 | 2024-10-01 | 广东西屋康达空调有限公司 | A rotary dehumidification method and device for anti-condensation step temperature regulation, and storage medium |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1996023185A1 (en) * | 1995-01-25 | 1996-08-01 | Engelhard/Icc | Hybrid air-conditioning system and operating method |
| US5551245A (en) * | 1995-01-25 | 1996-09-03 | Engelhard/Icc | Hybrid air-conditioning system and method of operating the same |
| JPH10197010A (en) * | 1996-12-27 | 1998-07-31 | Ebara Corp | Air conditioner and air conditioning system |
| JPH10205819A (en) * | 1997-01-21 | 1998-08-04 | Ebara Corp | Air conditioner and air conditioning system |
| CN200968680Y (en) * | 2006-11-17 | 2007-10-31 | 广东西屋康达空调有限公司 | Dried pipe coil constant air conditioning air-conditioning unit |
| CN201096388Y (en) * | 2007-06-06 | 2008-08-06 | 重庆大学 | Multifunctional air conditioner device |
| CN201255472Y (en) * | 2008-04-18 | 2009-06-10 | 南京师范大学 | Energy accumulation type air conditioning dehumidification system |
| CN201547895U (en) * | 2009-11-09 | 2010-08-11 | 杭州捷瑞空气处理设备有限公司 | A Fresh Air Rotary Dehumidification Air Conditioner with Recycled Condensation Heat |
| CN202119021U (en) * | 2011-05-11 | 2012-01-18 | 湖南科技大学 | Multistage heat-recovery compound-dehumidifying new air processor |
-
2011
- 2011-05-11 CN CN 201110121129 patent/CN102261701B/en not_active Expired - Fee Related
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1996023185A1 (en) * | 1995-01-25 | 1996-08-01 | Engelhard/Icc | Hybrid air-conditioning system and operating method |
| US5551245A (en) * | 1995-01-25 | 1996-09-03 | Engelhard/Icc | Hybrid air-conditioning system and method of operating the same |
| JPH10197010A (en) * | 1996-12-27 | 1998-07-31 | Ebara Corp | Air conditioner and air conditioning system |
| JPH10205819A (en) * | 1997-01-21 | 1998-08-04 | Ebara Corp | Air conditioner and air conditioning system |
| CN200968680Y (en) * | 2006-11-17 | 2007-10-31 | 广东西屋康达空调有限公司 | Dried pipe coil constant air conditioning air-conditioning unit |
| CN201096388Y (en) * | 2007-06-06 | 2008-08-06 | 重庆大学 | Multifunctional air conditioner device |
| CN201255472Y (en) * | 2008-04-18 | 2009-06-10 | 南京师范大学 | Energy accumulation type air conditioning dehumidification system |
| CN201547895U (en) * | 2009-11-09 | 2010-08-11 | 杭州捷瑞空气处理设备有限公司 | A Fresh Air Rotary Dehumidification Air Conditioner with Recycled Condensation Heat |
| CN202119021U (en) * | 2011-05-11 | 2012-01-18 | 湖南科技大学 | Multistage heat-recovery compound-dehumidifying new air processor |
Cited By (42)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102705205A (en) * | 2012-05-28 | 2012-10-03 | 深圳百时得能源环保科技有限公司 | Pre-treating and variable-flow device of air compression system |
| CN102705205B (en) * | 2012-05-28 | 2015-12-23 | 深圳百时得能源环保科技有限公司 | A kind of pretreatment of air compression system and variable-flow device |
| CN102927627A (en) * | 2012-11-05 | 2013-02-13 | 江苏国莱特空调设备有限公司 | Condensation heat recovery type movable temperature and humidity control device |
| CN103836736A (en) * | 2014-02-10 | 2014-06-04 | 三湘股份有限公司 | Intelligent fresh air purification and full heat exchange equipment and control method thereof |
| CN103836736B (en) * | 2014-02-10 | 2016-08-17 | 三湘股份有限公司 | Intelligent fresh air purifies and Total heat exchange equipment and control method thereof |
| CN104792065A (en) * | 2014-12-19 | 2015-07-22 | 上海伯涵热能科技有限公司 | Heat pump system for heating drying medium and recovering waste heat in stepped mode |
| CN104792065B (en) * | 2014-12-19 | 2017-06-20 | 浙江普林艾尔电器工业有限公司 | A kind of dried medium step heats the heat pump with exhaust heat stepped recovery |
| CN104984636A (en) * | 2015-06-18 | 2015-10-21 | 彭福明 | A high-efficiency heat pump dehumidifier |
| CN108027155A (en) * | 2015-09-30 | 2018-05-11 | 株式会社前川制作所 | Dehumanization method and dehydrating unit |
| CN110678248B (en) * | 2017-03-24 | 2022-05-13 | 荣达高科技有限公司 | Apparatus and method for producing water |
| CN110678248A (en) * | 2017-03-24 | 2020-01-10 | 马西莫·维琴蒂尼 | Apparatus and method for producing water |
| CN108499327A (en) * | 2018-03-21 | 2018-09-07 | 东南大学 | A kind of adjustable high-pressure solution dehumidifying of pressure leak source and waste-heat recovery device and method |
| CN108489251A (en) * | 2018-06-11 | 2018-09-04 | 南京农业大学 | A kind of pump type heat low-temperature circulating formula crop dryer of waste heat recoverable |
| CN108489251B (en) * | 2018-06-11 | 2023-08-29 | 南京农业大学 | Heat pump type low-temperature circulating grain drier capable of recycling waste heat |
| CN109959099A (en) * | 2019-04-22 | 2019-07-02 | 山西阳旭新能源科技有限公司 | A kind of Multi-functional dehumidifying fresh air waste heat recycling hot water air conditioning device |
| CN109959099B (en) * | 2019-04-22 | 2024-06-07 | 广东腾耀机电工程有限公司 | Multifunctional dehumidifying fresh air waste heat recovery hot water air conditioning device |
| CN113905804A (en) * | 2019-06-12 | 2022-01-07 | 阿特拉斯·科普柯空气动力股份有限公司 | Compressor system and method for supplying compressed gas |
| CN110454878A (en) * | 2019-08-08 | 2019-11-15 | 江苏苏净集团有限公司 | An energy-saving rotary dehumidifier |
| CN110375396A (en) * | 2019-08-13 | 2019-10-25 | 河南中瑞制冷科技有限公司 | A kind of large size depth dehumidification system and its working method |
| CN110375395A (en) * | 2019-08-13 | 2019-10-25 | 河南中瑞制冷科技有限公司 | Industrial combined type depth dehumidification system |
| CN110594919A (en) * | 2019-09-29 | 2019-12-20 | 北京四季通能源科技有限公司 | Air source heat pump system and control method thereof |
| CN110594919B (en) * | 2019-09-29 | 2024-02-13 | 北京四季通能源科技有限公司 | Air source heat pump system and control method thereof |
| WO2021114715A1 (en) * | 2019-12-13 | 2021-06-17 | 艾默生环境优化技术(苏州)有限公司 | Runner dehumidification device regeneration system and runner dehumidification device |
| CN112984649A (en) * | 2019-12-13 | 2021-06-18 | 艾默生环境优化技术(苏州)有限公司 | Regeneration system of rotating wheel dehumidification equipment and rotating wheel dehumidification equipment |
| CN111102661A (en) * | 2020-01-10 | 2020-05-05 | 同济大学 | An energy-saving variable dehumidification heat pump type rotary dehumidifier unit and its control method |
| CN111102661B (en) * | 2020-01-10 | 2023-11-24 | 同济大学 | An energy-saving variable dehumidification heat pump rotor dehumidification unit and its control method |
| CN113218012A (en) * | 2020-07-09 | 2021-08-06 | 中国建筑科学研究院有限公司 | Anti-frosting fresh air heat recovery device and control method thereof |
| CN113028524A (en) * | 2021-04-05 | 2021-06-25 | 西安科技大学 | Multi-split type solid dehumidification multifunctional air conditioning system and application method thereof |
| CN113028524B (en) * | 2021-04-05 | 2022-04-22 | 西安科技大学 | Multi-split type solid dehumidification multifunctional air conditioning system and application method thereof |
| CN113007821A (en) * | 2021-04-12 | 2021-06-22 | 海南大学 | Indoor dehumidification method realized through window |
| CN113007821B (en) * | 2021-04-12 | 2022-10-18 | 海南大学 | A method of indoor dehumidification through windows |
| CN113154551A (en) * | 2021-05-12 | 2021-07-23 | 慧湿环境科技（上海）有限公司 | Hot water type low-temperature regeneration rotating wheel dehumidification fresh air system of high-temperature heat pump |
| CN113566322B (en) * | 2021-08-04 | 2022-08-05 | 西安科技大学 | Using method of multi-energy complementary dehumidification rotary wheel air-conditioning system |
| CN113566322A (en) * | 2021-08-04 | 2021-10-29 | 西安科技大学 | A kind of multi-energy complementary dehumidification rotary air conditioning system and using method thereof |
| CN114165860A (en) * | 2021-12-13 | 2022-03-11 | 必信能源科技(苏州)有限公司 | Heat pump regeneration system for rotary wheel dehumidification |
| CN114543216B (en) * | 2022-02-28 | 2023-06-02 | 深圳市德尼环境技术有限公司 | Waste heat recovery type energy-saving dehumidifying air conditioner |
| CN114543216A (en) * | 2022-02-28 | 2022-05-27 | 深圳市德尼环境技术有限公司 | Waste heat recovery type energy-saving dehumidification air conditioner |
| CN115143546A (en) * | 2022-06-13 | 2022-10-04 | 武汉理工大学 | Method for realizing joint control of pollutants by using double-layer composite rotary air-conditioning system |
| CN116294542A (en) * | 2023-03-02 | 2023-06-23 | 东南大学 | A full-condition composite dehumidification system for suspension bridge main cables based on waste heat recovery |
| CN118310105A (en) * | 2024-04-18 | 2024-07-09 | 广东海洋大学 | Evaporative cooling device and method for heat-driven rotary dehumidification |
| CN118729515A (en) * | 2024-08-27 | 2024-10-01 | 广东西屋康达空调有限公司 | A rotary dehumidification method and device for anti-condensation step temperature regulation, and storage medium |
| CN118729515B (en) * | 2024-08-27 | 2024-11-05 | 广东西屋康达空调有限公司 | Anti-condensation step temperature-regulating rotary dehumidification method and equipment and storage medium |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102261701B (en) | 2013-06-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102261701B (en) | Multilevel heat recovery composite dehumidifying fresh air treatment machine | |
| CN103075770B (en) | Rotating wheel dehumidification device utilizing indoor exhaust evaporation cooling and use method of rotating wheel dehumidification device | |
| CN201547895U (en) | A Fresh Air Rotary Dehumidification Air Conditioner with Recycled Condensation Heat | |
| CN103791576B (en) | A kind of low-grade heat source drives and becomes solution temperature two-stage liquid desiccant air conditioning | |
| CN204665595U (en) | Tandem heat-recycling air treatment device | |
| CN105444310B (en) | A kind of double cold source intelligent fresh air units of double plates | |
| CN102384539B (en) | Composite air-conditioning system combining air source heat pump system and rotating wheel dehumidification system | |
| CN102506475A (en) | Heat pump system of heat humidity independent control driven by condensation waste heat and based on solid dehumidification | |
| CN207162794U (en) | Recovery type heat double runner level Four dehumidifier/air-conditioning system with high temperature refrigerant cooling | |
| CN202149545U (en) | Fresh air fan set with heat recovery and humidification functions | |
| CN101105347A (en) | Heat pump air conditioner with adjustable humidity | |
| CN202993416U (en) | Condensing heat recycling energy-saving turning wheel dehumidifier | |
| CN101118075A (en) | Solar-powered single-rotor two-stage desiccant air conditioner | |
| CN210070102U (en) | Ground pipe laying water source dehumidification humidification fresh air unit | |
| CN105276736A (en) | Heat pump type total heat recovery new-air air conditioning unit with condensation reheating function | |
| CN107255336A (en) | A kind of heat pump driven solution dehumidification Fresh air handing unit of single air channel compact | |
| CN110207295A (en) | A kind of heat pump type air conditioner improving refrigeration and heating effect using condensed water | |
| CN1281899C (en) | Hybrid dehumidifying air-conditioner | |
| CN102721133B (en) | Self-cooling type solid desiccant cooling dehumidification air-conditioning system | |
| CN202119021U (en) | Multistage heat-recovery compound-dehumidifying new air processor | |
| CN107270456B (en) | A kind of energy-saving cold and heat supply dehumidifying integrated apparatus | |
| CN105805868B (en) | Regenerate backheat dehumidifying heat pump system and its operation method | |
| CN101231047A (en) | Air conditioning system coupled with high temperature heat pump and dehumidification wheel and high temperature heat pump | |
| CN105805869B (en) | The back-heating type solid desiccant dehumidification air-conditioning system and operation method of Driven by Solar Energy | |
| CN110388815A (en) | Composite air-conditioning system and its working method for grain depot drying |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130619 Termination date: 20160511 |