CN2777404Y - Ultragravity liquid adsorption dehumidification and regeneration apparatus - Google Patents
Ultragravity liquid adsorption dehumidification and regeneration apparatus Download PDFInfo
- Publication number
- CN2777404Y CN2777404Y CN 200520054595 CN200520054595U CN2777404Y CN 2777404 Y CN2777404 Y CN 2777404Y CN 200520054595 CN200520054595 CN 200520054595 CN 200520054595 U CN200520054595 U CN 200520054595U CN 2777404 Y CN2777404 Y CN 2777404Y
- Authority
- CN
- China
- Prior art keywords
- hypergravity
- regenerator
- air
- rotating shaft
- packed bed
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
The utility model provides a supergravity liquid adsorbing, dehumidifying and regenerating device which comprises a supergravity absorber and a supergravity regenerator, wherein the supergravity absorber is communicated with indoor air and the supergravity regenerator is communicated with outdoor air. The position between the supergravity absorber and the supergravity regenerator is provided with a cool liquid storing tank, a heat exchanger, a regenerating heater, a hot liquid storing tank and a cooler. The supergravity absorber and the supergravity regenerator are also respectively connected with an indoor blower and an outdoor blower and can be a cross flow type or a counter flow type. The device has the advantages of simple structure, low cost, safety, convenient overhaul, and strong adjustability and mass transfer coefficient reaches more than 0.5m/s. Air treating capacity increases more than 50 percent, and efficiency can enhances more than 40 percent. The volume can reduce more than 60 percent compared with the existing device, and application range is wider.
Description
Technical field
The utility model relates to liquid absorption dehumidifying and regeneration techniques, specifically is meant a kind of super gravity liquid absorption dehumidifying and regenerating unit.
Background technology
Liquid dehumidification system has been subjected to paying close attention to widely because its environmental friendliness, energy consumption are low, can play the advantages such as effect that purify air in dehumidifying.In traditional liquid dehumidification system, the application of packed tower and internally cooled dehumidifier is comparatively extensive.Owing to packed tower is to rely on the gravity effect to realize that the gas-liquid contact carries out mass transfer, and gravitational field a little less than, liquid film flows slower, and the gas-liquid contact area is less, and heat and mass transfer process is slow, need long-pending than large contact surface, thereby this equipment volume is huge, and space availability ratio is low, and the air-treatment amount is little, effect on moisture extraction is relatively poor, and is difficult to again use in the vehicles and family room.The internally cooled dehumidifier can be taken away the latent heat that discharges in the absorption process in dehumidification process, can improve absorption efficiency, but because the gas-liquid contact area is limited, efficient improves not obvious.Solution after the dehumidifying needs regenerator to regenerate, and general dehumidification solution is regenerated with equipment such as packed towers, improve system effectiveness, need to increase surface area, the inevitable pipe-line system that makes equally is complicated, and equipment volume is very huge, and power of regeneration is also relatively poor, and cost is also high.Above reason makes the application of traditional liquid dehumidification system be subjected to certain restriction.Though there are some dehumidification systems to be used for building, because it is bulky, the application aspect miniaturization is very restricted.
At home, the Chinese invention patent specification of the CN1174312A that on February 25th, 1998 was announced is mentioned and is utilized liquid dehumidifying to carry out the method and apparatus that the air evaporation cooling is regulated, dehumidifier is divided into except that wet channel and humidification cooling duct, method for dehumidifying liquid be treat dehumidified air flow through dehumidifier remove wet channel the time, cooling air (outdoor air) cools off at the cooling duct humidification, aerial temperature and humidity is regulated in the direct evaporative cooling of this equipment utilization dry air and indirect evaporation cooling, utilizes explosive evaporation and non-boiling under the normal pressure to evaporate the regeneration that the two effect regenerations of uniting are realized dehumidifying liquid.On May 7th, 2003, the CN1415909A Chinese invention patent ublic specification of application of bulletin was mentioned a kind of multistage method for dehumidifying liquid, liquid dehumidifying is divided into two-stage or more than the two-stage, every grade liquid independent loops, every grade of strength of fluid is all different, but there is the unidirectional migration of solution between level and the level, promptly moved to the low level of concentration by the high level of solution concentration, the level that solution concentration is the highest is replenished certain quantity solution by the external world, and the rarest level of solution concentration is discharged certain solution to the external world.Pending air adopts modes such as spray or filler by constantly dry, thereby obtains dry air successively by at different levels.This invention has the efficient height, the characteristics that the heat and mass area is little.Because pending air can from one-level or discharge not at the same level, also can never at the same levelly suck from sucking with one-level, from one-level or discharge not at the same level, therefore can regulate the humidity of handling the back air neatly.More than these system's complex structures, the dehumidifying and regeneration efficient not high, and the maintenance also the difficulty.
The regenerating unit of hygroscopic solution in the liquid dehumidification system that the Chinese utility model patent specification of the CN2584262Y that on November 5th, 2003 was announced is mentioned, this invention comprise have casing with outer wind channel, regenerator, filler, reservoir and solution pump, its design feature is: the import department in housing is provided with regenerator, place filler in the cavity of enclosure interior, the bottom of filler is immersed in the solution tank, on the liquid level of solution in solution tank solution pump is set.Outdoor new wind passes the filler that soaks and carries out caloic exchange behind regenerator, realize the regeneration of dehumidizer, this device non-environmental-pollution, can make full use of solar energy, minimizing heat transfer link, simple in structure, operating cost is cheap, the regeneration efficiency height of solution.Though the relative conventional apparatus regeneration efficiency of these systems increases, increase rate is very limited.
Summary of the invention
The purpose of this utility model is to overcome prior art problems and deficiency, provides a kind of absorption dehumidifying and regeneration efficiency higher, can realize the super gravity liquid absorption dehumidifying and the regenerating unit of device miniaturization.
The purpose of this utility model realizes by following proposal: this super gravity liquid absorption dehumidifying comprises hypergravity absorber, hypergravity regenerator with regenerating unit, described hypergravity absorber is communicated with room air, described hypergravity regenerator is communicated with outdoor air, be connected by cold reservoir, heat exchanger, regenerative heater, hot reservoir, cooler between described hypergravity absorber, the hypergravity regenerator, described hypergravity absorber, hypergravity regenerator also are connected with indoor fan, outdoor fan respectively.
For realizing the utility model better, described hypergravity absorber comprises housing, rotating shaft, packed bed, described housing is provided with air inlet, exhaust outlet, inlet, leakage fluid dram, described leakage fluid dram is arranged on housing bottom, and successively with described cold reservoir, the tube side of heat exchanger, regenerative heater connects, described inlet successively with described cooler, heat exchanger shell pass, hot reservoir connects, described air inlet is connected with described indoor fan, described exhaust outlet is connected with devaporizer, described devaporizer is connected with spray header, and the exhaust outlet of described devaporizer is communicated with room air; Described packed bed is fixedly connected on rotating shaft the inner, its inside is provided with filler, inactive liquid distributor, described inactive liquid distributor is connected with the housing inlet, the flow through direction of described packed bed of described rotating shaft and air is parallel or vertical, air and liquid is cross-flow or counter current contacting in described packed bed, described rotating shaft outer end is connected with shaft coupling, and described shaft coupling is connected with drive unit.
Described hypergravity regenerator comprises housing, rotating shaft, packed bed, described housing is provided with air inlet, exhaust outlet, inlet, leakage fluid dram, described leakage fluid dram is arranged on housing bottom, and be connected with described hot reservoir, described inlet is connected with described regenerative heater, described air inlet is connected with described outdoor fan, and described exhaust outlet is communicated with outdoor air; Described packed bed is fixedly connected on rotating shaft the inner, its inside is provided with filler, inactive liquid distributor, described inactive liquid distributor is connected with the housing inlet, the flow through direction of described packed bed of described rotating shaft and air is parallel or vertical, air and liquid is cross-flow or counter current contacting in described packed bed, described rotating shaft outer end is connected with shaft coupling, and described shaft coupling is connected with drive unit.
Between described cold reservoir and the heat exchanger, between regenerative heater and the hypergravity regenerator, between cooler and the hypergravity absorber, be connected with solution pump respectively.
Described cooler is connected with cooling water pipe.
Described inactive liquid distributor comprises feed tube, spray head, and described spray head is connected with feed tube, and it is arranged in the inner chamber of described packed bed, and relative with filler.
Described filler is woven wire, foam metal, pottery or gasket packing.
Described liquid is LiBr solution, LiCl solution, CaCl2 solution, triethylene glycol or their mixed liquor.
In this super gravity liquid absorption dehumidifying and regenerating unit, the hypergravity absorber can adopt identical structure simultaneously with the hypergravity regenerator, and promptly air and liquid all are that cross-flow contacts or all is counter current contacting in packed bed; Also can adopt different structures respectively, promptly air and liquid are respectively a kind of during counter current contacting or cross-flow contact in packed bed.
During the utility model work, the rotating speed of its rotating shaft requires more than 1000 rev/mins, to realize the state of hypergravity, make rotating shaft, packed bed produce powerful centrifugal force, the microcosmic of greatly having strengthened between the gas-liquid mixes, and makes the attenuation of gas-liquid film, and resistance to mass tranfer reduces, mass tranfer coefficient is than one of the following raising of conventional gravity condition more than the order of magnitude, thereby mass transfer effect is significantly improved.
Operation principle of the present utility model is:
(1) absorption dehumidifying process: start drive unit and indoor fan, driving rotating shaft by shaft coupling rotates, treat that dehumidified air enters from the air inlet of described hypergravity absorber, under the air pressure positive action, axially pass the filler of described packed bed, described liquid is introduced the inner chamber of packed bed from the feed tube of described inactive liquid distributor, be showered into the filler inner edge through described spray head, liquid outwards throws away under the centrifugal action of described packed bed, and treat dehumidified air cross-flow or counter current contacting with this, realize the dehumidifying of air.Dry air is discharged from the exhaust outlet of described hypergravity absorber, enters devaporizer, by the spray header spray water mist, after the adjusting temperature and humidity reaches the requirement of air-treatment, sends into indoor the utilization; The liquid that is thrown out of behind the absorption dehumidifying becomes diluent liquid, compiles after leakage fluid dram is discharged at housing bottom, enters described cold reservoir.
(2) liquid temperature-rise period: the described liquid behind the absorption dehumidifying flows out from described cold reservoir, send into described heat exchanger tube side by described solution pump, carry out heat exchange with the described liquid after the regeneration in the described heat exchanger shell pass, (this regenerative heater both can use the high-grade energy such as electric energy, steam to pass through described regenerative heater then, can use low-grade energies such as solar energy, geothermal energy, waste heat again) heat the rising temperature, send into the inlet of described hypergravity regenerator at last by described solution pump.
(3) liquid regenerative process: start drive unit and outdoor fan simultaneously, driving rotating shaft by shaft coupling rotates, outdoor air enters from the air inlet of described hypergravity regenerator, under the air pressure positive action, axially pass the filler of described packed bed, introduce the inner chamber of packed bed from the feed tube of described inactive liquid distributor through the described liquid of heating, be showered into the filler inner edge through described spray head, liquid outwards throws away under the centrifugal action of described packed bed, and with outdoor air cross-flow or counter current contacting, moisture in the liquid is taken away by outdoor air, realizes the regeneration of liquid.The air of entrapped moisture is discharged to outdoor from the exhaust outlet of described hypergravity regenerator; The liquid that is thrown out of after the regeneration reverts to original concentration, compiles after leakage fluid dram is discharged at housing bottom, enters described hot reservoir.
(4) liquid temperature-fall period: the described liquid after the regeneration flows out from described hot reservoir, enter the shell side of described heat exchanger and the described liquid behind the interior absorption dehumidifying of tube side and carry out heat exchange, enter cooler then, further lower the temperature by the cold water in the cooling water pipe, send into the inlet of described hypergravity absorber at last by described solution pump, proceed the absorption dehumidifying process.
When this device running hours, this plurality of processes is carried out simultaneously, as mentioned above, just can better finish the process of whole absorption dehumidifying and regeneration.
The utility model compared with prior art has following advantage and beneficial effect:
(1) air-treatment amount is big, and controllability is strong, the efficient height; Rotating shaft, packed bed that (1000～3000 rev/mins of turn ups) rotated in the utility model utilization at a high speed produce powerful centrifugal force, the gas-liquid mass transfer effect is significantly improved, mass tranfer coefficient is than one of the following raising of conventional gravity condition more than the order of magnitude, reach more than the 0.5m/s, the air-treatment amount increases more than 50%, and efficient can improve more than 40%.
(2) simple in structure, cost is low; The utility model is compared with legacy equipment, floor space and spatial volume reduce significantly, weight of equipment is lighter, equipment volume can be dwindled more than 60%, make whole liquid absorption dehumidifying and regenerating unit realize miniaturization and indoorization, greatly reduce cost of investment, install safe and reliable, maintenance is convenient, and the scope of application is wider.
Description of drawings
Fig. 1 is the schematic flow sheet of the utility model super gravity liquid absorption dehumidifying and regenerating unit;
Fig. 2 is a kind of structural representation of hypergravity absorber shown in Figure 1;
Fig. 3 is a kind of structural representation of hypergravity regenerator shown in Figure 1;
Fig. 4 is the another kind of structural representation of hypergravity absorber shown in Figure 1;
Fig. 5 is the another kind of structural representation of hypergravity regenerator shown in Figure 1.
The specific embodiment
Below in conjunction with embodiment and accompanying drawing the utility model is described in further detail, but embodiment of the present utility model is not limited thereto.
Embodiment 1
Fig. 1 has provided the schematic flow sheet of the utility model super gravity liquid absorption dehumidifying and regenerating unit, as shown in Figure 1, this super gravity liquid absorption dehumidifying comprises hypergravity absorber 2 with regenerating unit, hypergravity regenerator 5, hypergravity absorber 2 is communicated with room air, hypergravity regenerator 5 is communicated with outdoor air, the leakage fluid dram of hypergravity absorber 2 successively with cold reservoir 13, the tube side of heat exchanger 11, regenerative heater 10, the inlet of hypergravity regenerator 5, the inlet of hypergravity absorber 2 successively with cooler 8, heat exchanger 11 shell sides, hot reservoir 7, the leakage fluid dram of hypergravity regenerator 5 connects, cooler 8 is connected with cooling water pipe 9, between cold reservoir 13 and the heat exchanger 11, between regenerative heater 10 and the hypergravity regenerator 5, between cooler 8 and the hypergravity absorber 2, be connected with solution pump 12 respectively.The air inlet of the air inlet of hypergravity absorber 2, hypergravity regenerator 5 also is connected with indoor fan 1, outdoor fan 6 respectively, the exhaust outlet of hypergravity absorber 2 is connected with devaporizer 3, devaporizer 3 is connected with spray header 4, and the exhaust outlet of devaporizer 3 is communicated with room air.
Fig. 2 has provided a kind of concrete structure of hypergravity absorber 2 shown in Figure 1, as shown in Figure 2, hypergravity absorber 2 comprises housing 2-14, rotating shaft 2-15, packed bed 2-16, housing is provided with air inlet 2-14-1, exhaust outlet 2-14-2, inlet 2-14-3, leakage fluid dram 2-14-4, leakage fluid dram 2-14-4 is arranged on housing 2-14 bottom, the flow through direction of packed bed 2-16 of rotating shaft 2-15 and air is parallel, air contacts with the cross-flow in packed bed 2-16 of liquid LiBr solution, packed bed 2-16 is fixedly connected on rotating shaft 2-15 the inner, its inside is provided with filler metal silk screen 2-17, inactive liquid distributor 2-18, inactive liquid distributor 2-18 is connected with housing inlet 2-14-3, inactive liquid distributor 2-18 comprises feed tube 2-18-1, spray head 2-18-2, spray head 2-18-2 is connected with feed tube 2-18-1, it is arranged in the inner chamber of packed bed 2-16, and 2-17 is relative with the filler metal silk screen, and rotating shaft 2-15 outer end is connected with shaft coupling 2-19, and shaft coupling 2-19 is connected with drive unit.
Fig. 3 has provided a kind of concrete structure of hypergravity regenerator 5 shown in Figure 1, as shown in Figure 3, hypergravity regenerator 5 comprises housing 5-14, rotating shaft 5-15, packed bed 5-16, housing is provided with air inlet 5-14-1, exhaust outlet 5-14-2, inlet 5-14-3, leakage fluid dram 5-14-4, leakage fluid dram 5-14-4 is arranged on housing 5-14 bottom, the flow through direction of packed bed 5-16 of rotating shaft 5-15 and air is parallel, air contacts with the cross-flow in packed bed 5-16 of liquid LiBr solution, packed bed 5-16 is fixedly connected on rotating shaft 5-15 the inner, its inside is provided with filler metal silk screen 5-17, inactive liquid distributor 5-18, inactive liquid distributor 5-18 is connected with housing inlet 5-14-3, inactive liquid distributor 5-18 comprises feed tube 5-18-1, spray head 5-18-2, spray head 5-18-2 is connected with feed tube 5-18-1, it is arranged in the inner chamber of packed bed 5-16, and 5-17 is relative with the filler metal silk screen, and rotating shaft 5-15 outer end is connected with shaft coupling 5-19, and shaft coupling 5-19 is connected with drive unit.
Embodiment 2
As shown in Figure 1, the utility model super gravity liquid absorption dehumidifying is identical with embodiment 1 described flow process with the flow process of regenerating unit.
Fig. 4 has provided the another kind of concrete structure of hypergravity absorber 2 shown in Figure 1, as shown in Figure 4, hypergravity absorber 2 comprises housing 2-20, rotating shaft 2-21, packed bed 2-22, housing 2-20 is provided with air inlet 2-20-1, exhaust outlet 2-20-2, inlet 2-20-3, leakage fluid dram 2-20-4, leakage fluid dram 2-20-4 is arranged on housing 2-20 bottom, the flow through direction of packed bed 2-22 of rotating shaft 2-21 and air is vertical, air and liquid LiCl solution counter current contacting in packed bed 2-22, packed bed 2-22 is fixedly connected on rotating shaft 2-21 the inner, its inside is provided with padding foam metal 2-23, inactive liquid distributor 2-24, inactive liquid distributor 2-24 is connected with housing inlet 2-20-3, inactive liquid distributor 2-24 comprises feed tube 2-24-1, spray head 2-24-2, spray head 2-24-2 is connected with feed tube 2-24-1, it is arranged in the inner chamber of packed bed 2-22, and 2-23 is relative with the padding foam metal, and rotating shaft 2-21 outer end is connected with shaft coupling 2-25, and shaft coupling 2-25 is connected with drive unit.
Fig. 5 has provided the another kind of concrete structure of hypergravity regenerator 5 shown in Figure 1, as shown in Figure 5, hypergravity absorber 5 comprises housing 5-20, rotating shaft 5-21, packed bed 5-22, housing 5-20 is provided with air inlet 5-20-1, exhaust outlet 5-20-2, inlet 5-20-3, leakage fluid dram 5-20-4, leakage fluid dram 5-20-4 is arranged on housing 5-20 bottom, the flow through direction of packed bed 5-22 of rotating shaft 5-21 and air is vertical, air and liquid LiCl solution counter current contacting in packed bed 5-22, packed bed 5-22 is fixedly connected on rotating shaft 5-21 the inner, its inside is provided with padding foam metal 5-23, inactive liquid distributor 5-24, inactive liquid distributor 5-24 is connected with housing inlet 5-20-3, inactive liquid distributor 5-24 comprises feed tube 5-24-1, spray head 5-24-2, spray head 5-24-2 is connected with feed tube 5-24-1, it is arranged in the inner chamber of packed bed 5-22, and 5-23 is relative with the padding foam metal, and rotating shaft 5-21 outer end is connected with shaft coupling 5-25, and shaft coupling 5-25 is connected with drive unit.
Embodiment 3
As shown in Figure 1, the utility model super gravity liquid absorption dehumidifying is identical with embodiment 1 with the flow process of regenerating unit.
As shown in Figure 2, the structure of hypergravity absorber 2 is identical with hypergravity absorber 2 described structures among the embodiment 1, and wherein filler 2-17 is a pottery, and liquid is CaCl2 solution.
As shown in Figure 5, the structure of hypergravity regenerator 5 is identical with hypergravity regenerator 6 described structures among the embodiment 2, and wherein filler 5-23 is a pottery, and liquid is CaCl2 solution.
Embodiment 4
As shown in Figure 1, the utility model super gravity liquid absorption dehumidifying is identical with embodiment 1 with the flow process of regenerating unit.
As shown in Figure 4, the structure of hypergravity absorber 2 is identical with hypergravity absorber 2 described structures among the embodiment 2, and wherein filler 2-23 is gasket packing, and liquid is triethylene glycol.
As shown in Figure 3, the structure of hypergravity regenerator 5 is identical with hypergravity regenerator 6 described structures among the embodiment 1, and wherein filler 5-17 is gasket packing, and liquid is triethylene glycol.
Embodiment 5
As shown in Figure 1, the utility model super gravity liquid absorption dehumidifying is identical with embodiment 1 with the flow process of regenerating unit.
As shown in Figure 4, the structure of hypergravity absorber 2 is identical with hypergravity absorber 2 described structures among the embodiment 2, and wherein filler 2-23 is a woven wire, and liquid is the mixed liquor of LiBr solution, LiCl solution.
As shown in Figure 3, the structure of hypergravity regenerator 5 is identical with hypergravity regenerator 5 described structures among the embodiment 1, and wherein filler 5-17 is a foam metal, and liquid is the mixed liquor of CaCl2 solution, triethylene glycol.
As mentioned above, just can realize a kind of super gravity liquid absorption dehumidifying of the utility model and regenerating unit preferably.
Claims (8)
1, a kind of super gravity liquid absorption dehumidifying and regenerating unit, it is characterized in that: comprise hypergravity absorber, hypergravity regenerator, described hypergravity absorber is communicated with room air, described hypergravity regenerator is communicated with outdoor air, be connected by cold reservoir, heat exchanger, regenerative heater, hot reservoir, cooler between described hypergravity absorber, the hypergravity regenerator, described hypergravity absorber, hypergravity regenerator also are connected with indoor fan, outdoor fan respectively.
2, by described a kind of super gravity liquid absorption dehumidifying of claim 1 and regenerating unit, it is characterized in that: described hypergravity absorber comprises housing, rotating shaft, packed bed, described housing is provided with air inlet, exhaust outlet, inlet, leakage fluid dram, described leakage fluid dram is arranged on housing bottom, and successively with described cold reservoir, the tube side of heat exchanger, regenerative heater connects, described inlet successively with described cooler, heat exchanger shell pass, hot reservoir connects, described air inlet is connected with described indoor fan, described exhaust outlet is connected with devaporizer, described devaporizer is connected with spray header, and the exhaust outlet of described devaporizer is communicated with room air; Described packed bed is fixedly connected on rotating shaft the inner, its inside is provided with filler, inactive liquid distributor, described inactive liquid distributor is connected with the housing inlet, the flow through direction of described packed bed of described rotating shaft and air is parallel or vertical, described rotating shaft outer end is connected with shaft coupling, and described shaft coupling is connected with drive unit.
3, by described a kind of super gravity liquid absorption dehumidifying of claim 1 and regenerating unit, it is characterized in that: described hypergravity regenerator comprises housing, rotating shaft, packed bed, described housing is provided with air inlet, exhaust outlet, inlet, leakage fluid dram, described leakage fluid dram is arranged on housing bottom, and be connected with described hot reservoir, described inlet is connected with described regenerative heater, and described air inlet is connected with described outdoor fan, and described exhaust outlet is communicated with outdoor air; Described packed bed is fixedly connected on rotating shaft the inner, its inside is provided with filler, inactive liquid distributor, described inactive liquid distributor is connected with the housing inlet, the flow through direction of described packed bed of described rotating shaft and air is parallel or vertical, described rotating shaft outer end is connected with shaft coupling, and described shaft coupling is connected with drive unit.
4, by described a kind of super gravity liquid absorption dehumidifying of claim 1 and regenerating unit, it is characterized in that: between described cold reservoir and the heat exchanger, between regenerative heater and the hypergravity regenerator, between cooler and the hypergravity absorber, be connected with solution pump respectively.
5, by described a kind of super gravity liquid absorption dehumidifying of claim 1 and regenerating unit, it is characterized in that: described cooler is connected with cooling water pipe.
6, by claim 2 or 3 described a kind of super gravity liquid absorption dehumidifying and regenerating units, it is characterized in that: described inactive liquid distributor comprises feed tube, spray head, described spray head is connected with feed tube, and it is arranged in the inner chamber of described packed bed, and relative with filler.
7, by claim 2 or 3 described a kind of super gravity liquid absorption dehumidifying and regenerating units, it is characterized in that: described filler is woven wire, foam metal, pottery or gasket packing.
8, by claim 2 or 3 described a kind of super gravity liquid absorption dehumidifying and regenerating units, it is characterized in that: described liquid is LiBr solution, LiCl solution, CaCl2 solution, triethylene glycol or their mixed liquor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520054595 CN2777404Y (en) | 2005-02-04 | 2005-02-04 | Ultragravity liquid adsorption dehumidification and regeneration apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520054595 CN2777404Y (en) | 2005-02-04 | 2005-02-04 | Ultragravity liquid adsorption dehumidification and regeneration apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2777404Y true CN2777404Y (en) | 2006-05-03 |
Family
ID=36744789
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200520054595 Expired - Fee Related CN2777404Y (en) | 2005-02-04 | 2005-02-04 | Ultragravity liquid adsorption dehumidification and regeneration apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2777404Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105466072A (en) * | 2015-11-19 | 2016-04-06 | 浙江理工大学 | Regeneration device and method for super-gravity heat source tower antifreeze solution |
| CN108939824A (en) * | 2017-05-17 | 2018-12-07 | 上海秀特化工科技有限公司 | Technology and device is absorbed and utilized in a kind of hypergravity zero-emission organic volatile |
-
2005
- 2005-02-04 CN CN 200520054595 patent/CN2777404Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105466072A (en) * | 2015-11-19 | 2016-04-06 | 浙江理工大学 | Regeneration device and method for super-gravity heat source tower antifreeze solution |
| CN105466072B (en) * | 2015-11-19 | 2017-11-17 | 浙江理工大学 | Hypergravity heat source tower anti-freezing solution regenerating unit and method |
| CN108939824A (en) * | 2017-05-17 | 2018-12-07 | 上海秀特化工科技有限公司 | Technology and device is absorbed and utilized in a kind of hypergravity zero-emission organic volatile |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1179160C (en) | Dehumidifier system | |
| CN1136418C (en) | Dehumidifying air conditioner | |
| CN1246646C (en) | Cooling/heating system of air conditioner | |
| CN1272584C (en) | Air-conditioning system | |
| US4341539A (en) | Thermally regenerative desiccant element | |
| KR100855446B1 (en) | Heat exchanger | |
| CN106564979A (en) | Integrated refrigeration, dehumidification and pure water preparation system using solar energy or low-temperature heat source | |
| CN102114378B (en) | Hygroscopic agent and manufacturing method and application thereof | |
| CN1325144C (en) | Super gravity liquid absorption dehumidifying and regenerating system | |
| CN1864829A (en) | A hydrophilic-hydrophobic bipolar composite membrane and method for preparing same | |
| CN201706611U (en) | New wind energy-saving heat pump rotating wheel dehumidifier | |
| CN101810935A (en) | Method and device for regenerating liquid desiccant | |
| CN107120747A (en) | The anti-defrosting system of net for air-source heat pump units dry-air blast and its method of work | |
| CN102721133B (en) | Self-cooling type solid desiccant cooling dehumidification air-conditioning system | |
| CN101816881B (en) | Novel ventilation energy-saving heat pump rotary dehumidifier | |
| CN2777404Y (en) | Ultragravity liquid adsorption dehumidification and regeneration apparatus | |
| CN109812913B (en) | Indirect evaporation inner-cooling type solution fresh air dehumidifying device | |
| CN100340815C (en) | Non-contact type humidifying/dehumidifying device based on hydrophobic polymer film | |
| CN1888624A (en) | Precooler for ventilation of air conditioner | |
| CN111013315A (en) | Organic waste gas adsorption and desorption device | |
| CN101617175A (en) | Damping device and air conditioner | |
| CN113390199B (en) | Solution-air moisture-gathering water taking system and method based on adsorption refrigeration system driving in island region | |
| CN110145830B (en) | Air heat and humidity independent treatment integrated equipment utilizing solution for dehumidification | |
| CN210267587U (en) | Air heat and humidity independent treatment integrated equipment utilizing solution for dehumidification | |
| CN210980049U (en) | Runner heating clean system based on solar heat pump regeneration |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20060503 Termination date: 20120204 |