CN101708872B - Solar desalting device - Google Patents
Solar desalting device Download PDFInfo
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- CN101708872B CN101708872B CN2009102732516A CN200910273251A CN101708872B CN 101708872 B CN101708872 B CN 101708872B CN 2009102732516 A CN2009102732516 A CN 2009102732516A CN 200910273251 A CN200910273251 A CN 200910273251A CN 101708872 B CN101708872 B CN 101708872B
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- 238000011033 desalting Methods 0.000 title 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 112
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 68
- 229910052742 iron Inorganic materials 0.000 claims abstract description 56
- 238000009833 condensation Methods 0.000 claims abstract description 53
- 230000005494 condensation Effects 0.000 claims abstract description 53
- 238000001704 evaporation Methods 0.000 claims abstract description 48
- 230000008020 evaporation Effects 0.000 claims abstract description 42
- 238000007791 dehumidification Methods 0.000 claims abstract description 26
- 239000013505 freshwater Substances 0.000 claims abstract description 25
- 238000010612 desalination reaction Methods 0.000 claims abstract description 23
- 239000011552 falling film Substances 0.000 claims abstract description 21
- 238000005192 partition Methods 0.000 claims abstract description 11
- 239000011521 glass Substances 0.000 claims description 16
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 10
- 229910052802 copper Inorganic materials 0.000 claims description 10
- 239000010949 copper Substances 0.000 claims description 10
- 239000012774 insulation material Substances 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 6
- 239000010408 film Substances 0.000 claims description 4
- 239000003365 glass fiber Substances 0.000 claims description 4
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 17
- 239000012267 brine Substances 0.000 description 16
- 238000004891 communication Methods 0.000 description 10
- 150000003839 salts Chemical class 0.000 description 8
- 238000011160 research Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000012546 transfer Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000909 electrodialysis Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005246 galvanizing Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/138—Water desalination using renewable energy
- Y02A20/142—Solar thermal; Photovoltaics
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
本发明具体涉及一种太阳能脱盐装置。其技术方案是:蒸发凝结箱(13)内有3~5层底部为三角形凹槽状的铁盘(14),每条凹槽下装有一条V形流槽(15),V形流槽(15)与箱内淡水出口(18)相通。蒸发凝结箱(13)底部通过水管和第一水泵(1)与加湿去湿塔(6)内的冷凝管(12)相通,冷凝管(12)通过水管经向阳随动太阳能集热器(11)后与蜂窝降膜蒸发器(8)相通。加湿去湿塔(6)内设有塑料隔板(9),其上部和下部分别装有上风扇(10)和下风扇(7),加湿去湿塔(6)左侧底部通过水管和第二水泵(2)与蒸发凝结箱(13)内的第二层铁盘(14)相通。本发明具有热能利用充分、运行温度较高、蒸发量和淡水产量较大的特点。
The invention specifically relates to a solar desalination device. Its technical scheme is: there are 3~5 layers of bottoms in the evaporation and condensation box (13) that are triangular groove-shaped iron plates (14), each groove is equipped with a V-shaped launder (15), the V-shaped launder (15) communicate with fresh water outlet (18) in the case. The bottom of the evaporation and condensation box (13) communicates with the condensation pipe (12) in the humidification and dehumidification tower (6) through the water pipe and the first water pump (1), and the condensation pipe (12) passes through the water pipe through the sun-facing follow-up solar heat collector (11 ) communicates with the honeycomb falling film evaporator (8). The humidifying and dehumidifying tower (6) is provided with a plastic partition (9), and its upper and lower parts are respectively equipped with an upper fan (10) and a lower fan (7). The left bottom of the humidifying and dehumidifying tower (6) passes through the water pipe and the Two water pumps (2) communicate with the second layer of iron pan (14) in the evaporation condensation box (13). The invention has the characteristics of sufficient heat energy utilization, high operating temperature, large evaporation and fresh water output.
Description
技术领域technical field
本发明属于脱盐技术领域,具体涉及一种太阳能脱盐装置。The invention belongs to the technical field of desalination, and in particular relates to a solar desalination device.
背景技术Background technique
盐水和苦咸水的淡化是解决今后世界水资源紧张问题的重要方向。目前较为成熟的脱盐技术主要有多效蒸发、反渗透和电渗析等,但都存在投资高、能耗大、且消耗的都为不可再生能源等缺点。在众多的能源中,太阳能以其无限的储量和完全清洁的特征脱颖而出并愈来愈受到重视。太阳能脱盐具有不需或仅消耗很少的常规能源,不会产生二次污染,运行费用低等优势,是今后新能源与新脱盐工艺研究的主要方向之一(左潞等海水淡化太阳能蒸馏技术研究现状与展望,河海大学学报,2008,36:753-757)。The desalination of salt water and brackish water is an important direction to solve the problem of water shortage in the world in the future. At present, relatively mature desalination technologies mainly include multi-effect evaporation, reverse osmosis and electrodialysis, etc., but they all have disadvantages such as high investment, high energy consumption, and consumption of non-renewable energy. Among the numerous energy sources, solar energy stands out with its unlimited reserves and completely clean characteristics, and has been paid more and more attention. Solar desalination has the advantages of no or little consumption of conventional energy, no secondary pollution, and low operating costs. It is one of the main directions for future research on new energy and new desalination processes (Zuo Lu et al. Research Status and Prospects, Journal of Hohai University, 2008, 36: 753-757).
目前,太阳能脱盐技术主要分为主动系统和被动式系统两大类。被动式太阳能脱盐系统由于没有外部加热方式,因此产水量很低,没有太大的实用价值(徐进扬等太阳能蒸馏器的试验研究,节能,2005,2:42-43)。一些常见的太阳能蒸馏器(郑宏飞具有折皱底面的多级迭盘式太阳能蒸馏器的模拟实验研究,太阳能学报,2004,25:200-203;张小艳等多级迭盘式太阳能蒸馏器的实验研究,水处理技术,2003,29:233-235)虽然是主动系统,但是存在蒸汽容易泄露,系统产水量不大,热能利用不充分等缺点。其它单一的太阳能脱盐技术和装置,如降膜蒸发-气流吸收等(郭强几种不同类型太阳能蒸馏器的传热研究与性能分析,新能源及工艺,2005,29-33),也都存在热能利用率不高、运行温度较低以及蒸发驱动力较大等缺陷。At present, solar desalination technology is mainly divided into two categories: active system and passive system. Since the passive solar desalination system has no external heating method, the water production is very low and has no practical value (Xu Jinyang et al. Experimental research on solar stills, Energy Saving, 2005, 2: 42-43). Some common solar stills (Zheng Hongfei's simulation experiment research on multi-stage stacked disc solar stills with wrinkled bottom surfaces, Acta Solar Sinica, 2004, 25: 200-203; Zhang Xiaoyan et al. Experimental research on multi-stage stacked disc solar stills, Water Treatment Technology, 2003, 29: 233-235) is an active system, but there are disadvantages such as easy leakage of steam, small water production in the system, and insufficient utilization of heat energy. Other single solar desalination technologies and devices, such as falling film evaporation-airflow absorption, etc. (Guo Qiang's heat transfer research and performance analysis of several different types of solar stills, New Energy and Technology, 2005, 29-33), also exist Defects such as low thermal energy utilization rate, low operating temperature, and large evaporation driving force.
发明内容Contents of the invention
本发明旨在克服已有的技术缺陷,目的是提供一种热能利用充分、运行温度较高、蒸发量和淡水产量较大的太阳能脱盐装置。The invention aims to overcome the existing technical defects, and aims to provide a solar desalination device with sufficient thermal energy utilization, high operating temperature, large evaporation and fresh water output.
为实现上述目的,本发明采用的技术方案是:该装置由蒸发凝结箱、加湿去湿塔和向阳随动太阳能集热器三部分组成。In order to achieve the above object, the technical solution adopted by the present invention is: the device is composed of three parts: an evaporation and condensation box, a humidification and dehumidification tower and a sun-facing follow-up solar heat collector.
蒸发凝结箱的结构是:箱体内水平地固定有3~5层铁盘,铁盘底面折压成5~20条三角形凹槽,除最上层铁盘外,其余各层铁盘的三角形凹槽一端均封闭,另一端均通过铁盘连通槽互通,每层铁盘连通槽与该层铁盘连通管的上端相通,铁盘连通管的下端位于下一层铁盘连通槽的上方;每层铁盘的每条三角形凹槽的正下方均对应装有一条V形流槽,每层的每条V形流槽的一端均封闭,另一端亦通过流槽连通槽互通,每层流槽连通槽通过流槽连通管上下相通,最下层的流槽连通槽与蒸发凝结箱上的箱内淡水出口水平连通;箱内淡水出口距箱底的高度为箱体高度的1/4~1/3,进水口略低于箱内淡水出口,排水口位于箱体底部;蒸发凝结箱的箱体四侧和底部均用保温材料包覆,最上层铁盘与蒸发凝结箱箱壁之间的空隙用保温材料密封。The structure of the evaporation and condensation box is: 3 to 5 layers of iron plates are fixed horizontally in the box, and the bottom surface of the iron plates is folded into 5 to 20 triangular grooves. Except for the top iron plate, the triangular grooves of the other iron plates are One end is closed, and the other end communicates with each other through the iron plate communication groove. The iron plate communication groove of each layer communicates with the upper end of the iron plate communication pipe of the layer, and the lower end of the iron plate communication pipe is located above the iron plate communication groove of the next layer; A V-shaped chute is installed directly under each triangular groove of the iron plate. One end of each V-shaped chute in each layer is closed, and the other end is also communicated through the chute connecting groove, and each layer of chute is connected. The trough communicates up and down through the launder connecting pipe, and the launder connecting trough at the lowest level communicates horizontally with the fresh water outlet in the tank on the evaporation and condensation tank; the height between the fresh water outlet in the tank and the bottom of the tank is 1/4~1/3 of the height of the tank, The water inlet is slightly lower than the fresh water outlet in the tank, and the drain is located at the bottom of the tank; the four sides and the bottom of the tank of the evaporation and condensation tank are covered with thermal insulation materials, and the gap between the uppermost iron plate and the tank wall of the evaporation and condensation tank is covered with thermal insulation materials. The material is sealed.
加湿去湿塔的结构是:加湿去湿塔内的右侧装有冷凝管,左侧装有蜂窝降膜蒸发器;在冷凝管和蜂窝降膜蒸发器间竖直设置有塑料隔板,塑料隔板安装在基墙上,塑料隔板最上部和最下部的中间位置处分别设置有上风扇和下风扇;在加湿去湿塔的右侧底部装有塔内淡水出口,加湿去湿塔的左侧装有溢流口;加湿去湿塔的顶部固定安装有向阳随动太阳能集热器。The structure of the humidification and dehumidification tower is: the right side of the humidification and dehumidification tower is equipped with a condensation pipe, and the left side is equipped with a honeycomb falling film evaporator; a plastic partition is vertically arranged between the condensation pipe and the honeycomb falling film evaporator. The clapboard is installed on the base wall, and the upper fan and the lower fan are respectively installed in the middle of the uppermost and lower part of the plastic clapboard; the fresh water outlet in the tower is installed at the right bottom of the humidification and dehumidification tower, and the humidification and dehumidification tower An overflow port is installed on the left side; the top of the humidification and dehumidification tower is fixedly installed with a sun-following solar collector.
向阳随动太阳能集热器由向阳旋转底座和12~15根太阳能玻璃真空集热管组成,12~15根太阳能玻璃真空集热管并排相互固定,质心处安装在向阳旋转底座上;每根太阳能玻璃真空集热管的下端相互连通为进水端,上端相互连通为出水端。The sun-following solar collector consists of a sun-facing rotating base and 12-15 solar glass vacuum heat-collecting tubes, 12-15 solar-glass vacuum heat-collecting tubes are fixed side by side, and the center of mass is installed on the sun-facing rotating base; The lower ends of the heat collecting tubes are connected to each other as water inlet ends, and the upper ends are connected to each other as water outlet ends.
蒸发凝结箱的底部通过水管和第一水泵与加湿去湿塔内的冷凝管下端相通,冷凝管上端通过水管与向阳随动太阳能集热器的太阳能玻璃真空集热管的进水端相通,向阳随动太阳能集热器的太阳能玻璃真空集热管的出水端通过水管与加湿去湿塔内的蜂窝降膜蒸发器的上端相通,加湿去湿塔左侧的底部通过水管和第二水泵连通至蒸发凝结箱内的第二层铁盘的上方;上述水管均用保温材料包覆。The bottom of the evaporation and condensation box communicates with the lower end of the condensation pipe in the humidification and dehumidification tower through the water pipe and the first water pump. The water outlet end of the solar glass vacuum heat collecting tube of the mobile solar collector communicates with the upper end of the honeycomb falling film evaporator in the humidification and dehumidification tower through the water pipe, and the bottom of the left side of the humidification and dehumidification tower is connected to the evaporation and condensation through the water pipe and the second water pump. Above the second-layer iron plate in the box; the above-mentioned water pipes are all covered with thermal insulation materials.
所述的每层铁盘分别经铁盘支撑杆固定在蒸发凝结箱箱壁,每层铁盘均经表面镀锌处理;每层V形流槽分别经流槽支撑杆固定在蒸发凝结箱箱壁,每层V形流槽为PVC材质。The iron plates of each layer are respectively fixed on the wall of the evaporation and condensation box through the iron plate support rods, and the surface of each layer of iron plates is galvanized; The wall and each layer of V-shaped flow grooves are made of PVC.
所述的蜂窝降膜蒸发器的材质为蜂窝状玻璃纤维无机湿膜。The material of the honeycomb falling film evaporator is honeycomb glass fiber inorganic wet film.
所述的冷凝管为10~12根镀锌铜管竖直均匀排列,镀锌铜管的柱面上沿竖直方向均匀地开有6~10条凹槽。The condensation pipes are 10-12 galvanized copper pipes vertically and uniformly arranged, and 6-10 grooves are evenly formed on the cylindrical surface of the galvanized copper pipes along the vertical direction.
所述的上风扇固定安装在塔顶上,下风扇固定安装在基墙上,基墙高度为加湿去湿塔高度的1/8~1/6;上风扇的出风口面向加湿去湿塔的右侧,下风扇的出风口面向加湿去湿塔的左侧。The upper fan is fixedly installed on the top of the tower, the lower fan is fixedly installed on the foundation wall, the height of the foundation wall is 1/8 to 1/6 of the height of the humidification and dehumidification tower; the air outlet of the upper fan faces the side of the humidification and dehumidification tower On the right side, the air outlet of the lower fan faces the left side of the humidification and dehumidification tower.
所述的塑料隔板为两张平行的塑料板,两张塑料板间的距离约为上风扇或下风扇的厚度。The plastic partition is two parallel plastic plates, and the distance between the two plastic plates is about the thickness of the upper fan or the lower fan.
由于采用上述技术方案,本发明的向阳随动太阳能集热器可按照太阳的运动轨迹运动以保证阳光直射到太阳能玻璃真空集热管表面,从而大大提高太阳能的利用效率,同时由于阳光长时间的直射使得太阳能玻璃真空集热管能有效加热盐水,系统的运行温度很高;蜂窝降膜蒸发器采用玻璃纤维无机湿膜,具有吸水性好,增湿强度高等特点,被加热的盐水在该蜂窝降膜蒸发器上蒸发所需的驱动力很小,蒸发量较大。另外,上、下风扇能产生快速的循环气流,循环气流经蜂窝降膜蒸发器表面也能进一步促进盐水的蒸发;冷凝管和铁盘分别为镀锌铜管和镀锌铁盘,不仅传热效果好也能有效防止盐水对冷凝管和铁盘的腐蚀;镀锌铜管在竖直方向的柱面上均匀地开有凹槽,能有效加强冷凝和传热过程;蒸发凝结箱四周以及最上层铁盘和箱体间用保温材料包覆,不仅能有效保存箱内热量促进铁盘上盐水的蒸发,还能防止蒸汽的外泄;铁盘底部为三角形凹槽状,可以增大冷凝面,有利于箱内蒸汽的凝结。蜂窝降膜蒸发器产生的蒸汽对冷凝管中的盐水可以起到加热的作用,同时在冷凝管上冷凝释放出的潜热也可以加热冷凝管中的盐水。未蒸发的浓盐水在蒸发凝结箱内的铁盘上进一步蒸发,蒸汽和其凝结时释放出的潜热同样也对上一层铁盘内的浓盐水起到了加热的作用。Due to the adoption of the above-mentioned technical scheme, the sun-following solar heat collector of the present invention can move according to the trajectory of the sun to ensure that the sunlight directly hits the surface of the solar glass vacuum heat collector tube, thereby greatly improving the utilization efficiency of solar energy. The solar glass vacuum heat collection tube can effectively heat the brine, and the operating temperature of the system is very high; the honeycomb falling film evaporator adopts glass fiber inorganic wet film, which has the characteristics of good water absorption and high humidification strength, and the heated brine is in the honeycomb falling film. The driving force required for evaporation on the evaporator is small, and the amount of evaporation is large. In addition, the upper and lower fans can generate a fast circulating air flow, and the circulating air passing through the surface of the honeycomb falling film evaporator can further promote the evaporation of salt water; the condensing pipe and the iron plate are galvanized copper tube and galvanized iron plate respectively, which not only have good heat transfer effect It can also effectively prevent the salt water from corroding the condensing pipe and the iron plate; the galvanized copper pipe has grooves evenly on the vertical cylindrical surface, which can effectively strengthen the condensation and heat transfer process; The plate and the box are covered with thermal insulation material, which can not only effectively preserve the heat in the box, promote the evaporation of salt water on the iron plate, but also prevent the leakage of steam; the bottom of the iron plate is in the shape of a triangular groove, which can increase the condensation surface and effectively Facilitate the condensation of steam in the box. The steam generated by the honeycomb falling film evaporator can heat the brine in the condenser pipe, and the latent heat released by condensation on the condenser pipe can also heat the brine in the condenser pipe. The unevaporated brine is further evaporated on the iron plate in the evaporation and condensation box, and the latent heat released by the steam and its condensation also heats the brine in the iron plate on the upper layer.
本发明最大程度地吸收了太阳能,运行温度较高,整个脱盐过程多次充分利用了蒸汽的潜热和盐水自身的显热,极大地提高了整个脱盐装置的热利用效率和产水率。The invention absorbs solar energy to the greatest extent, and has a high operating temperature. The whole desalination process makes full use of the latent heat of steam and the sensible heat of brine itself for many times, which greatly improves the heat utilization efficiency and water production rate of the whole desalination device.
因此,本发明具有热能利用充分、运行温度较高、蒸发量和淡水产量较大的特点。尤其适合用于小岛或能源紧张地区制取淡水。Therefore, the present invention has the characteristics of sufficient heat energy utilization, high operating temperature, large evaporation and fresh water output. It is especially suitable for producing fresh water in small islands or energy-stressed areas.
附图说明Description of drawings
图1为本发明一种结构示意图;Fig. 1 is a kind of structural representation of the present invention;
图2是图1中A-A俯视示意图;Fig. 2 is a top view diagram of A-A in Fig. 1;
图3是图1中B-B俯视示意图。Fig. 3 is a schematic top view of B-B in Fig. 1 .
具体实施方式Detailed ways
下面结合附图和具体实施方式对本发明做进一步的描述,并非对保护范围的限制:Below in conjunction with accompanying drawing and specific embodiment, the present invention is further described, not limiting the scope of protection:
实施例1Example 1
一种太阳能脱盐装置。该装置如图1所示,该装置由蒸发凝结箱13、加湿去湿塔6和向阳随动太阳能集热器11三部分组成。A solar desalination device. This device is shown in Figure 1, and this device is made up of three parts of evaporating and condensing
蒸发凝结箱13的结构是:箱体内水平地固定有4层铁盘14,每层铁盘14的底面折压成8条三角形凹槽,除最上层铁盘14外,其余3层铁盘14的三角形凹槽一端均封闭,另一端均通过铁盘连通槽21互通,每层铁盘连通槽21与该层铁盘连通管17的上端相通,铁盘连通管17的下端位于下一层铁盘连通槽21的上方;每层铁盘14的每条三角形凹槽的正下方均对应装有一条V形流槽15,每层的每条V形流槽15的一端均封闭,另一端通过流槽连通槽23互通,每层流槽连通槽23通过流槽连通管16上下相通,最下层的流槽连通槽23与蒸发凝结箱13上的箱内淡水出口18水平连通;箱内淡水出口18距箱底的高度为箱体高度的1/3,进水口19略低于箱内淡水出口18,排水口20位于箱体底部;蒸发凝结箱13的箱体四侧和底部均用保温材料包覆,最上层铁盘14与蒸发凝结箱13箱壁之间的空隙用保温材料密封。The structure of the evaporation and
加湿去湿塔6的结构是:加湿去湿塔6内的右侧装有冷凝管12,左侧装有蜂窝降膜蒸发器8;在冷凝管12和蜂窝降膜蒸发器8间竖直设置有塑料隔板9,塑料隔板9安装在基墙4上,塑料隔板9最上部和最下部的中间位置处分别设置有上风扇10和下风扇7;在加湿去湿塔6的右侧底部装有塔内淡水出口3,加湿去湿塔6的左侧装有溢流口5;加湿去湿塔6的顶部固定安装有向阳随动太阳能集热器11。The structure of the humidification and
向阳随动太阳能集热器11由向阳旋转底座和12根太阳能玻璃真空集热管组成,12根太阳能玻璃真空集热管并排相互固定,质心处安装在向阳旋转底座上;每根太阳能玻璃真空集热管的下端相互连通为进水端,上端相互连通为出水端。Sunward follower
蒸发凝结箱13的底部通过水管和第一水泵1与加湿去湿塔6内的冷凝管12下端相通,冷凝管12上端通过水管与向阳随动太阳能集热器11的太阳能玻璃真空集热管的进水端相通,向阳随动太阳能集热器11的太阳能玻璃真空集热管的出水端通过水管与加湿去湿塔6内的蜂窝降膜蒸发器8的上端相通,加湿去湿塔6左侧的底部通过水管和第二水泵2连通至蒸发凝结箱13内的第二层铁盘14的上方;上述水管均用保温材料包覆。The bottom of the evaporating and
所述的每层铁盘14如图2和图3所示,分别经铁盘支撑杆22固定在蒸发凝结箱13箱壁,每层铁盘14均经表面镀锌处理;每层V形流槽15分别经流槽支撑杆24固定在蒸发凝结箱13箱壁,每层V形流槽15为PVC材质。Described every layer of
所述的蜂窝降膜蒸发器8的材质为蜂窝状玻璃纤维无机湿膜。The material of the honeycomb falling
所述的冷凝管12为10根镀锌铜管竖直均匀排列,镀锌铜管的柱面上沿竖直方向均匀地开有8条凹槽。The
所述的上风扇10固定安装在塔顶上,下风扇7固定安装在基墙4上,基墙4高度为加湿去湿塔6高度的1/8;上风扇10的出风口面向加湿去湿塔6的右侧,下风扇7的出风口面向加湿去湿塔6的左侧。The
所述的塑料隔板9为两张平行的塑料板,两张塑料板间的距离约为上风扇10或下风扇7的厚度。The
本发明进行盐水或苦咸水淡化过程如下:首先关闭蒸发凝结箱13上的排水口20,通过进水口19加入要处理的盐水,待盐水水面接近进水口19时停止加入盐水并关闭进水口19。然后依次启动向阳太阳能随动集热器11、第一水泵1、上风扇10、下风扇7和第二水泵2。蒸发凝结箱13中的盐水通过冷凝管12进入向阳随动太阳能集热器11,经向阳随动太阳能集热器11加热后的盐水再进入蜂窝降膜蒸发器8,经蜂窝降膜蒸发器8后未蒸发完的浓盐水被第二水泵2泵入蒸发凝结箱13中的第二层铁盘14上。The process of desalination of salt water or brackish water in the present invention is as follows: first close the
加湿去湿塔6内的上风扇10和下风扇7产生的循环气流快速流过蜂窝降膜蒸发器8表面使被加热的盐水迅速蒸发成水蒸气,水蒸汽随循环气流与冷凝管12接触并在其表面凝结成塔内淡水后经塔内淡水出口3引出。The circulating airflow produced by the
泵入蒸发凝结箱13中的第二层铁盘14上浓盐水经铁盘连通管17逐层下降,铁盘14上的浓盐水蒸发产生的蒸汽在上一层铁盘14背部凝结成箱内淡水并由V形流槽15通过箱内淡水出口18引出。铁盘14上未蒸发完的浓盐水进入蒸发凝结箱13底部后被第一水泵1泵往冷凝管12进行新一轮的循环。在脱盐过程中,当蒸发凝结箱13底部盐水接近饱和时要停止第一水泵1、第二水泵2、上风扇10和下风扇7,然后通过排水口20排出蒸发凝结箱13内接近饱和的盐水。本装置具有热能利用充分、运行温度较高、蒸发量和淡水产量较大的特点。The concentrated brine on the second layer of
实施例2Example 2
一种太阳能脱盐装置。该装置结构如图1、图2和图所示。箱体内水平地固定有3层或5层铁盘14;箱内淡水出口18距箱底的高度为箱体高度的1/4~1/3;向阳随动太阳能集热器11由向阳旋转底座和13~15根太阳能玻璃真空集热管组成;冷凝管12为11或12根镀锌铜管竖直均匀排列,镀锌铜管的柱面上沿竖直方向均匀地开有6~7或9~10条凹槽;基墙4高度为加湿去湿塔6高度的1/8~1/6。A solar desalination device. The structure of the device is shown in Figure 1, Figure 2 and Figure 2. There are 3 or 5 layers of
其余同实施例1。All the other are with embodiment 1.
本具体实施方式最大程度地吸收了太阳能,运行温度较高,整个脱盐过程多次充分利用了蒸汽的潜热和盐水自身的显热,极大地提高了整个脱盐装置的热利用效率和产水率。This specific embodiment absorbs solar energy to the greatest extent, and the operating temperature is high. The whole desalination process makes full use of the latent heat of steam and the sensible heat of brine itself for many times, which greatly improves the heat utilization efficiency and water production rate of the whole desalination device.
因此,本具体实施方式具有热能利用充分、运行温度较高、蒸发量和淡水产量较大的特点。尤其适合用于小岛或能源紧张地区制取淡水。Therefore, this specific embodiment has the characteristics of sufficient heat energy utilization, high operating temperature, large evaporation and fresh water production. It is especially suitable for producing fresh water in small islands or energy-stressed areas.
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