CN100595491C - Composite solution dehumidification system based on ultrasonic atomization technology - Google Patents
Composite solution dehumidification system based on ultrasonic atomization technology Download PDFInfo
- Publication number
- CN100595491C CN100595491C CN200810041926A CN200810041926A CN100595491C CN 100595491 C CN100595491 C CN 100595491C CN 200810041926 A CN200810041926 A CN 200810041926A CN 200810041926 A CN200810041926 A CN 200810041926A CN 100595491 C CN100595491 C CN 100595491C
- Authority
- CN
- China
- Prior art keywords
- dehumidification
- solution
- atomization
- tower
- 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.)
- Expired - Fee Related
Links
- 238000007791 dehumidification Methods 0.000 title claims abstract description 100
- 238000000889 atomisation Methods 0.000 title claims abstract description 48
- 238000005516 engineering process Methods 0.000 title claims abstract description 17
- 239000002131 composite material Substances 0.000 title claims description 6
- 150000001875 compounds Chemical class 0.000 claims abstract description 5
- 230000008929 regeneration Effects 0.000 claims description 7
- 238000011069 regeneration method Methods 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 4
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 claims description 4
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 2
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 2
- 239000001110 calcium chloride Substances 0.000 claims description 2
- 239000000919 ceramic Substances 0.000 claims description 2
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 claims description 2
- 238000009413 insulation Methods 0.000 claims 1
- 150000003839 salts Chemical class 0.000 abstract description 11
- 238000004378 air conditioning Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 54
- 239000000945 filler Substances 0.000 description 14
- 238000012856 packing Methods 0.000 description 8
- 239000003595 mist Substances 0.000 description 6
- 238000011160 research Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 238000012546 transfer Methods 0.000 description 5
- 238000005265 energy consumption Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- 238000013461 design Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Images
Landscapes
- Drying Of Gases (AREA)
Abstract
Description
技术领域: Technical field:
本发明涉及一种溶液除湿系统,尤其是一种基于超声波雾化技术的复合溶液除湿系统。属于空调节能技术领域。The invention relates to a solution dehumidification system, in particular to a composite solution dehumidification system based on ultrasonic atomization technology. The utility model belongs to the technical field of air conditioning energy saving.
背景技术: Background technique:
空调耗电在京沪等大城市夏季总耗电量中能占到40%,民用建筑空调系统调查研究发现,夏季空调的除湿能耗占整个空气处理能耗的20%-40%,因此可见,除湿系统的节能在空调系统节能中具有举足轻重的地位。在除湿系统中,溶液除湿不但能够很好的利用太阳能、工业余热等低品位热源,而且系统的设计和结构可以非常灵活,既可以单独使用起到除湿的目的,又可以与传统的空调系统配合使用,有效降低其能耗;同时所使用的除湿溶液能够消灭空气中的细菌和微生物,有助于提高室内空气品质。因此,溶液除湿技术以其无可比拟的优势在近年来得到了广泛的关注与研究。The power consumption of air conditioners can account for 40% of the total power consumption in summer in big cities such as Beijing and Shanghai. The investigation and research on air conditioning systems in civil buildings have found that the dehumidification energy consumption of air conditioners in summer accounts for 20%-40% of the entire air processing energy consumption, so it can be seen that , The energy saving of the dehumidification system plays a decisive role in the energy saving of the air conditioning system. In the dehumidification system, solution dehumidification can not only make good use of low-grade heat sources such as solar energy and industrial waste heat, but also the design and structure of the system can be very flexible. It can be used alone for the purpose of dehumidification, and can also be used in conjunction with traditional air conditioning systems. Use, effectively reduce its energy consumption; at the same time, the dehumidification solution used can eliminate bacteria and microorganisms in the air, which helps to improve indoor air quality. Therefore, solution dehumidification technology has received extensive attention and research in recent years due to its incomparable advantages.
其中采用填料的除湿塔模块是溶液除湿系统中的基本传热传质单元,也是系统的基本组成部件,多个除湿塔模块可以拼组出多种不同的溶液除湿系统形式。填料式除湿塔可以利用较简单的几何结构实现较大的比表面积,传热传质效率较高,是应用最广泛的除湿塔,其主要缺点是:1除湿溶液除湿时吸热升温;2空气流过时压力降较大。对于这两个缺点不少学者做过深入的研究。对于第一点有人提出了内冷型除湿塔和对除湿溶液进行换热冷却的除湿塔,取得了较好的效果;对于第二点,不断有学者提出新型的具有高比表面积的填料。已有技术中,由世俊,张卫江在《金属填料型直接蒸发式空气冷却器的研究[J]》一文中(制冷学报,1994(4):28-31)和陈颖在《一种蜂窝纸毡填料用于除湿液体再生过程的实验研究》(制冷学报Vol.28,No.3 June.2007)一文中分别提出了两种填料形式,但这两篇文章同时也均指出虽然两种填料形式大大的提高了比表面积,却一样没有解决随着填料高度增加填料润湿表面积增加但是压降同样增加的缺点。此外孙贺江,由世俊在《空调用金属填料传热传质性能实验》(天津大学学报Vol.38 No.6 Jun.2005)一文中也明确指出:“实验表明,填料的比表面积对填料的传热及传质性能影响比较大.但比表面积增大会导致填料阻力有明显增长,因此,不能一味地强调靠增加填料的比表面积来改善填料的热工性能.”Among them, the dehumidification tower module with filler is the basic heat and mass transfer unit in the solution dehumidification system, and also the basic component of the system. Multiple dehumidification tower modules can be combined to form a variety of different solution dehumidification system forms. The packed dehumidification tower can use a relatively simple geometric structure to achieve a large specific surface area, and has high heat and mass transfer efficiency. It is the most widely used dehumidification tower. Its main disadvantages are: 1. The dehumidification solution absorbs heat and heats up during dehumidification; 2. The air The pressure drop is larger when flowing through. Many scholars have done in-depth research on these two shortcomings. For the first point, some people have proposed an internal cooling dehumidification tower and a dehumidification tower for heat exchange and cooling of the dehumidification solution, which have achieved good results; for the second point, some scholars have continuously proposed new types of fillers with high specific surface areas. In the prior art, by Shi Jun, Zhang Weijiang in "Research on Metal Packing Type Direct Evaporative Air Cooler [J]" (Journal of Refrigeration, 1994 (4): 28-31) and Chen Ying in "A Honeycomb Two types of fillers were proposed in the article "Experimental Research on Paper Felt Fillers Used in Dehumidification Liquid Regeneration Process" (Journal of Refrigeration Vol.28, No.3 June.2007), but both articles also pointed out that although the two fillers The form greatly improves the specific surface area, but it does not solve the disadvantage that the wetted surface area of the filler increases with the increase of the filler height, but the pressure drop also increases. In addition, Sun Hejiang and You Shijun also clearly pointed out in the article "Experiments on Heat and Mass Transfer Performance of Metal Fillings for Air Conditioners" (Journal of Tianjin University Vol.38 No.6 Jun.2005): "The experiments show that the specific surface area of the filler has a great Heat transfer and mass transfer performance have a relatively large impact. However, the increase in specific surface area will lead to a significant increase in the resistance of the filler. Therefore, it is not possible to blindly emphasize the improvement of the thermal performance of the filler by increasing the specific surface area of the filler.”
因而填料技术的进一步发展大大的受到了除湿塔对阻力要求的限制。填料设计过程中不仅要考虑提高其比表面积,同时也要考虑降低压损并使其具有良好的孔隙率,这一系列的要求使得填料技术的长足发展受到了限制,同时单纯追求填料的高比表面积必然带来填料研究难度的加大,以及成本增高、加工困难等一系列问题。在这样一种情况下如何通过结合新的技术改进除湿系统,提高除湿塔比表面积同时提高除湿塔效率显得格外重要。Therefore, the further development of packing technology is greatly limited by the resistance requirements of dehumidification towers. In the process of packing design, it is necessary not only to increase its specific surface area, but also to reduce pressure loss and make it have good porosity. This series of requirements restricts the long-term development of packing technology. The surface area will inevitably increase the difficulty of filler research, as well as a series of problems such as increased cost and difficult processing. In such a case, how to improve the dehumidification system by combining new technologies, increasing the specific surface area of the dehumidification tower and improving the efficiency of the dehumidification tower is particularly important.
发明内容: Invention content:
为了克服已有技术的不足和缺陷,本发明提供一种简单的,易于实现的,高效的基于超声波雾化技术的复合溶液除湿系统。In order to overcome the deficiencies and defects of the prior art, the present invention provides a simple, easy-to-implement, and efficient composite solution dehumidification system based on ultrasonic atomization technology.
本发明是通过以下技术方案实现:本发明在传统的除湿塔基础上增加一个溶液雾化装置,溶液雾化装置包括超声波发生器和雾化室,其中超声波发生器中的超声波换能器置于雾化室底部,雾化室下部装有浓溶液,浓溶液淹没超声波换能器。雾化室进气口与待处理空气相通,雾化室出气口与除湿塔进气口相通,除湿塔出气口排出除湿空气。雾化室的浓溶液出口与除湿塔溶液槽的浓溶液进口连接,除湿塔溶液槽的稀溶液出口通过再生装置与雾化室浓溶液进口相通。The present invention is realized through the following technical solutions: the present invention adds a solution atomization device on the basis of the traditional dehumidification tower, and the solution atomization device includes an ultrasonic generator and an atomization chamber, wherein the ultrasonic transducer in the ultrasonic generator is placed The bottom of the atomization chamber, the lower part of the atomization chamber is filled with concentrated solution, and the concentrated solution submerges the ultrasonic transducer. The air inlet of the atomization chamber communicates with the air to be treated, the air outlet of the atomization chamber communicates with the air inlet of the dehumidification tower, and the air outlet of the dehumidification tower discharges dehumidified air. The concentrated solution outlet of the atomization chamber is connected to the concentrated solution inlet of the solution tank of the dehumidification tower, and the dilute solution outlet of the solution tank of the dehumidification tower communicates with the concentrated solution inlet of the atomization chamber through a regeneration device.
浓溶液淹没超声波换能器,它将电能转换成机械振能,对换能器施加谐振电信号使得换能器产生范围在1-5MHZ的超声波震动,这种超声波震动将盐溶液雾化成直径1-10微米的盐雾颗粒;在雾化室中,浓溶液雾化颗粒与空气混合并充分接触。空气在雾化室到进入除湿塔前这一段,被初步除湿,此除湿过程完全依靠雾化的盐雾颗粒除湿实现;空气和盐雾混合气体进入除湿塔,进行二次除湿,此除湿过程与传统溶液除湿相同。The concentrated solution submerges the ultrasonic transducer, which converts electrical energy into mechanical vibration energy. Applying a resonant electrical signal to the transducer causes the transducer to generate ultrasonic vibrations in the range of 1-5MHZ. This ultrasonic vibration atomizes the salt solution into a diameter of 1 -10 micron salt spray particles; In the spray chamber, the concentrated solution atomized particles are mixed with air and fully contacted. The air is initially dehumidified in the section from the atomization chamber to the dehumidification tower. This dehumidification process is completely achieved by the dehumidification of atomized salt mist particles; the mixed gas of air and salt mist enters the dehumidification tower for secondary dehumidification. This dehumidification process is the same as Same as conventional solutions for dehumidification.
本发明有益效果:由于空气将大量盐雾带入除湿塔,使得除湿塔的除湿比表面积大大增加,同时超声波雾化作用,使得同等质量的盐溶液产生的比表面积大大增加。由于盐雾的存在,塔内比表面积提高,这使得除湿塔对填料的要求得以降低,从而使在填料塔中采用体表面积不是特别大而孔隙率高的填料变得可行。而填料孔隙率提高就意味着除湿塔的阻力损失减少,从而能耗也得以降低。本发明技术较之传统溶液除湿系统而言最大的优点在于不仅可以降低除湿塔对填料要求,降低除湿塔成本,而且可以提高溶液除湿能效比。The beneficial effect of the invention is that the dehumidification specific surface area of the dehumidification tower is greatly increased because the air brings a large amount of salt mist into the dehumidification tower, and the ultrasonic atomization effect greatly increases the specific surface area of the salt solution of the same quality. Due to the presence of salt mist, the specific surface area inside the tower increases, which reduces the requirement for packing in the dehumidification tower, thus making it feasible to use packing with a small body surface area and high porosity in the packed tower. The increase in the porosity of the filler means that the resistance loss of the dehumidification tower is reduced, and the energy consumption is also reduced. Compared with the traditional solution dehumidification system, the technology of the present invention has the biggest advantage that it can not only reduce the requirement of the dehumidification tower for packing, reduce the cost of the dehumidification tower, but also improve the energy efficiency ratio of the solution dehumidification.
附图说明: Description of drawings:
图1是本发明基于超声波雾化技术的复合溶液除湿系统的示意图:Fig. 1 is the schematic diagram of the compound solution dehumidification system based on ultrasonic atomization technology of the present invention:
图中1雾化室进气口,2雾化室,3雾化室出气口,4除湿塔进气口,5填料,6除湿塔出气口,7再生装置,8除湿塔,9除湿塔溶液槽,10溶液泵,11喷头,12超声波发生器,13超声波换能器,14溶液雾化装置。In the figure, 1 atomization chamber inlet, 2 atomization chamber, 3 atomization chamber outlet, 4 dehumidification tower inlet, 5 packing, 6 dehumidification tower outlet, 7 regeneration device, 8 dehumidification tower, 9 dehumidification tower solution Tank, 10 solution pump, 11 nozzle, 12 ultrasonic generator, 13 ultrasonic transducer, 14 solution atomizing device.
具体实施方式: Detailed ways:
下面结合附图对本发明的具体实施做进一步的描述:The concrete implementation of the present invention is described further below in conjunction with accompanying drawing:
如图1所示本发明包括除湿塔8和溶液雾化装置14,其中除湿塔8是一种传统的溶液除湿装置,其形式是传统绝热型除湿塔、带有浓溶液冷却换热装置的绝热型除湿塔,或者是多个除湿塔模块拼组成的除湿塔。溶液雾化装置14包括超声波发生器12和雾化室2,其中超声波发生器12中的超声波换能器13置于雾化室2的底部,雾化室2下部装有浓溶液,浓溶液淹没超声波换能器13,超声波换能器13是采用高频压电陶瓷片制成的。雾化室进气口1与待处理空气相通,雾化室出气口3与除湿塔进气口4相通,除湿塔出气口6排出除湿后的空气。雾化室2下部的浓溶液出口与除湿塔溶液槽9的浓溶液进口连接,除湿塔溶液槽9的稀溶液出口通过再生装置7与雾化室2下部的浓溶液进口相通。浓溶液是采用氯化锂、氯化钙、三甘醇或其组合溶液。As shown in Figure 1, the present invention includes a
除湿开始时超声波发生器12工作,将雾化室2下部的一部分浓溶液雾化成盐雾充满雾化室2上部空间,与待处理空气混合一起进入除湿塔8,稀释后落入除湿塔溶液槽9内;另一部分浓溶液直接输送到除湿塔溶液槽9,经溶液泵10由喷头11喷出,润湿填料5后最后回到除湿塔溶液槽9。两部分浓溶液吸湿后变成稀溶液进入再生装置7循环。At the beginning of dehumidification, the
此溶液循环较传统的溶液除湿装置来说,浓溶液的循环多了雾化环节。待处理空气先进入雾化室2,与盐雾混合,湿度初步降低,再进入除湿塔8,从除湿塔出气口6出来的空气即为除湿后的空气。Compared with the traditional solution dehumidification device, this solution cycle has more atomization links in the cycle of concentrated solution. The air to be treated first enters the atomization chamber 2, mixes with salt mist, and the humidity is initially reduced, and then enters the
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN200810041926A CN100595491C (en) | 2008-08-21 | 2008-08-21 | Composite solution dehumidification system based on ultrasonic atomization technology |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN200810041926A CN100595491C (en) | 2008-08-21 | 2008-08-21 | Composite solution dehumidification system based on ultrasonic atomization technology |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101344293A CN101344293A (en) | 2009-01-14 |
CN100595491C true CN100595491C (en) | 2010-03-24 |
Family
ID=40246347
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN200810041926A Expired - Fee Related CN100595491C (en) | 2008-08-21 | 2008-08-21 | Composite solution dehumidification system based on ultrasonic atomization technology |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN100595491C (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102052715B (en) * | 2010-12-15 | 2013-06-19 | 上海交通大学 | Multi-stage M-shaped air way liquid desiccant dehumidification air-conditioning system utilizing ultrasonic atomization technology |
CN102416309B (en) * | 2011-08-05 | 2013-12-11 | 上海交通大学 | Liquid desiccant ultrasonic regeneration device |
CN102679469B (en) * | 2012-04-27 | 2014-08-27 | 上海交通大学 | Ultrasonic atomization liquid dehumidifying air-conditioning system with spiral channel and pretreatment function |
CN106091133B (en) * | 2016-08-03 | 2021-07-20 | 南京工业大学 | An air treatment device and method |
CN106091132B (en) * | 2016-08-03 | 2021-07-30 | 南京工业大学 | An integrated device for air dehumidification and dust removal and a dehumidification and dust removal method |
CN113251514A (en) * | 2021-05-25 | 2021-08-13 | 贵州中建建筑科研设计院有限公司 | Multi-working-condition air heat and humidity coupling treatment equipment |
-
2008
- 2008-08-21 CN CN200810041926A patent/CN100595491C/en not_active Expired - Fee Related
Non-Patent Citations (4)
Title |
---|
液体除湿空调再生性能试验分析. 沈钰龙,柳建华.能源技术,第29卷第2期. 2008 |
液体除湿空调再生性能试验分析. 沈钰龙,柳建华.能源技术,第29卷第2期. 2008 * |
溶液式空调及其应用. 江亿,李震,陈晓阳,刘晓华.暖通空调,第34卷第11期. 2004 |
溶液式空调及其应用. 江亿,李震,陈晓阳,刘晓华.暖通空调,第34卷第11期. 2004 * |
Also Published As
Publication number | Publication date |
---|---|
CN101344293A (en) | 2009-01-14 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN100595491C (en) | Composite solution dehumidification system based on ultrasonic atomization technology | |
CN101368754B (en) | Solution dehumidification air conditioning equipment using membrane regenerator | |
CN206055832U (en) | The solar energy solution dehumidification system of unit is cooled down for double flash evaporation | |
CN102052715B (en) | Multi-stage M-shaped air way liquid desiccant dehumidification air-conditioning system utilizing ultrasonic atomization technology | |
CN103047724B (en) | Multi-energy complementally driven dehumidification air-conditioning system | |
CN103292611B (en) | Water-saving device used for wet-type air cooler in air-cooled power plant | |
CN206131340U (en) | Environment -friendly air conditioner comdenstion water ultrasonic atomization energy -saving appliance | |
CN109812880B (en) | Solar photo-thermal-photoelectric supercharged air film solution dehumidifying system and method | |
CN202546966U (en) | Non-fan cold air intake clerestory device with direct evaporative cooler | |
CN204457890U (en) | The cooling device of auxiliary condensing system combined by evaporative cooling-absorption heat pump | |
CN104154623A (en) | Constant temperature and humidity air conditioner capable of controlling humidity by heating steam condensate | |
CN102679469B (en) | Ultrasonic atomization liquid dehumidifying air-conditioning system with spiral channel and pretreatment function | |
CN201652662U (en) | A Direct Evaporative Cooling Air Conditioning Unit Combining High-Pressure Micro Mist and Packing | |
CN201652658U (en) | Packing—high-pressure micro-mist composite direct evaporative cooling air conditioning unit | |
CN211060289U (en) | A solution dehumidification dew point evaporative cooling refrigeration system driven by waste heat of air compressor | |
CN104315624A (en) | Air-assisted atomization solution dehumidification air-conditioning system | |
CN201311010Y (en) | Solution dehumidification air conditioner with membrane regenerator | |
CN203336729U (en) | Movable air-conditioning system | |
CN101270899A (en) | Solar-powered compact two-stage parallel liquid desiccant air conditioner | |
CN206377795U (en) | The humidifier of the air conditioner of the automatic water-returning draining of low power consuming | |
CN208253854U (en) | The air humidifier that a kind of pair of air conditioner condensate water recycles | |
CN203116202U (en) | Double-cold-source combined operation air-conditioning system | |
CN202613618U (en) | Evaporative cooling ventilation air-conditioner window with shutters and utilizing solar energy | |
CN207778636U (en) | Multifunction efficient energy-saving solution dehumidifying fresh air handling group | |
CN201327250Y (en) | Energy-saving capacity-increase cleaning system of equipment room precision air conditioner |
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 | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100324 Termination date: 20120821 |