CN108793299A - A kind of small-sized solar energy sea water desalination apparatus and method - Google Patents
A kind of small-sized solar energy sea water desalination apparatus and method Download PDFInfo
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- 239000013505 freshwater Substances 0.000 claims abstract description 35
- 239000007788 liquid Substances 0.000 claims abstract description 32
- 238000010438 heat treatment Methods 0.000 claims abstract description 28
- 238000007791 dehumidification Methods 0.000 claims abstract description 22
- 238000001816 cooling Methods 0.000 claims abstract description 21
- 238000001704 evaporation Methods 0.000 claims abstract description 15
- 230000008020 evaporation Effects 0.000 claims abstract description 13
- 230000008569 process Effects 0.000 claims abstract description 9
- 238000009833 condensation Methods 0.000 claims abstract description 7
- 230000005494 condensation Effects 0.000 claims abstract description 6
- 238000005507 spraying Methods 0.000 claims abstract description 5
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/14—Treatment of water, waste water, or sewage by heating by distillation or evaporation using solar energy
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/043—Details
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
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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
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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
- Y02A20/138—Water desalination using renewable energy
- Y02A20/142—Solar thermal; Photovoltaics
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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
- Y02A20/20—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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Abstract
本发明公开了一种轻小型太阳能海水淡化装置及方法,装置包括料液加热系统、能源供给系统、空气加湿系统和空气除湿系统。其中:循环介质经太阳能集热器加热后进入换热器,海水与之热交换后进入加湿器,空气经由风机从底部进入加湿器,加湿升温后的空气从底部进入除湿器,与除湿器内上部喷淋的冷却水进行热质交换,冷凝产生淡水与冷却水混合落入除湿器底部,降温除湿后的空气经由风机进入加湿器,以此循环往复。本系统利用太阳能供热和供电,使用喷淋和填料相结合强化空气加湿过程,提高海水蒸发效率;在常压下运行,无需真空泵,可处理高盐度溶液,规模灵活,应用范围广,可用于沿海、海岛淡化海水,也可用于浓缩工业废水。
The invention discloses a light and small solar seawater desalination device and method. The device includes a feed liquid heating system, an energy supply system, an air humidification system and an air dehumidification system. Among them: the circulating medium enters the heat exchanger after being heated by the solar collector, the seawater enters the humidifier after heat exchange with it, the air enters the humidifier from the bottom through the fan, and the air after humidification and heating enters the dehumidifier from the bottom, and the inside of the dehumidifier The cooling water sprayed on the upper part performs heat and mass exchange, and the fresh water produced by condensation mixes with the cooling water and falls to the bottom of the dehumidifier. The air after cooling and dehumidification enters the humidifier through the fan, and the cycle repeats. This system uses solar energy for heating and power supply, and uses a combination of spraying and packing to strengthen the air humidification process and improve seawater evaporation efficiency; it operates under normal pressure without a vacuum pump, and can handle high-salinity solutions. It has flexible scale, wide application range, and available It can be used to desalinate seawater on coasts and islands, and can also be used to concentrate industrial wastewater.
Description
技术领域technical field
本发明属于太阳能海水淡化技术领域,特别涉及到一种在低温常压下运行的轻小型太阳能海水淡化装置及方法,并具备轻小型、便携式、模块化的特点。The invention belongs to the technical field of solar seawater desalination, and in particular relates to a light and small solar seawater desalination device and method operating under low temperature and normal pressure, and has the characteristics of light, small, portable and modular.
背景技术Background technique
海水淡化即利用海水脱盐生产淡水,是实现淡水资源利用的开源增量技术。目前常用的海水淡化方法有低温多效、反渗透法、多级闪蒸、热膜联产、电渗析法等。反渗透法是在高压泵的作用下,水分子通过反渗透膜实现盐与水的分离,需要持续的提供电能或机械能,且随着料液浓度的增加,所需泵功增加导致处理成本增加,产水品质也有所下降,膜的使用寿命缩短。传统的多效蒸发式(中国发明专利申请号201010509740.X)和多级闪蒸式(中国发明专利申请号201310411226.6)等技术往往因一些共同问题而难以商业化推广使用。一是装置庞大复杂、体积大、投资成本高,二是随着料液浓度的增加,蒸发器内部表面发生沉积结垢和腐蚀的风险大大增加,装置传热效率降低,处理和维护成本增加。Seawater desalination is the use of seawater desalination to produce fresh water, which is an open-source incremental technology to realize the utilization of fresh water resources. At present, the commonly used seawater desalination methods include low-temperature multi-effect, reverse osmosis, multi-stage flash evaporation, thermal membrane cogeneration, electrodialysis, etc. In the reverse osmosis method, under the action of a high-pressure pump, water molecules pass through the reverse osmosis membrane to achieve the separation of salt and water, which requires continuous supply of electrical energy or mechanical energy, and as the concentration of the feed liquid increases, the required pump work increases, resulting in an increase in processing costs. , the quality of the product water is also reduced, and the service life of the membrane is shortened. Traditional multi-effect evaporation (Chinese invention patent application No. 201010509740.X) and multi-stage flash evaporation (Chinese invention patent application No. 201310411226.6) are often difficult to be commercialized due to some common problems. First, the device is huge and complex, with large volume and high investment cost. Second, as the concentration of the feed liquid increases, the risk of deposition and corrosion on the internal surface of the evaporator increases greatly, the heat transfer efficiency of the device decreases, and the treatment and maintenance costs increase.
加湿除湿技术是一种新型的海水淡化和废水浓缩技术,该技术模拟自然界的降雨循环过程,以流动空气作为水蒸气的载体,空气在加湿器中被热料液加湿,携带一定量的水蒸气后进入除湿器除湿,利用空气的饱和湿度差,多余的水蒸气冷凝产生淡水。与其他海水淡化技术相比,加湿除湿技术具有结构设计简单、设备投资和操作成本较低、可利用低品位能源或可再生能源、使用寿命长等优点,被认为是海水淡化中最具应用前景的技术之一。Humidification and dehumidification technology is a new type of seawater desalination and wastewater concentration technology. This technology simulates the natural rainfall cycle process, using flowing air as the carrier of water vapor. The air is humidified by the hot liquid in the humidifier and carries a certain amount of water vapor. Finally, it enters the dehumidifier for dehumidification. Using the difference in saturated humidity of the air, the excess water vapor condenses to produce fresh water. Compared with other seawater desalination technologies, humidification and dehumidification technology has the advantages of simple structural design, low equipment investment and operation costs, low-grade energy or renewable energy, and long service life. It is considered to be the most promising in seawater desalination. one of the technologies.
目前,海水淡化装置基本都利用太阳能这种可再生能源作为系统的能量输入,但由于集热器温度低,蒸发效率低,装置结构复杂,耐腐蚀性能不高等原因而无法大规模地推广使用。At present, seawater desalination devices basically use renewable energy such as solar energy as the energy input of the system, but due to the low temperature of the collector, low evaporation efficiency, complex structure of the device, and low corrosion resistance, it cannot be widely used on a large scale.
经过对现有技术的检索发现,申请号201010509740.X公开了一种喷雾蒸发空气加湿除湿式太阳能海水淡化装置,装置采用空气作为循环工质,但海水和空气没有循环利用,加湿效率低,且布置有多个冷凝换热器,装置结构复杂,安装调试困难,不利于装置的商业化推广。After searching the prior art, it was found that the application number 201010509740.X discloses a spray evaporative air humidification and dehumidification solar seawater desalination device. The device uses air as a circulating working medium, but seawater and air are not recycled, and the humidification efficiency is low. There are multiple condensing heat exchangers arranged, the structure of the device is complex, and installation and debugging are difficult, which is not conducive to the commercial promotion of the device.
进一步检索发现,专利申请号为00109939.6的中国发明专利公开了一种喷雾推进通风蒸发-冷凝式海水淡化工艺及装置,专利申请号为03144279.X的中国发明专利公开了一种海水蒸发罐中鼓泡法的海水淡化方法。这些专利虽然在原理上可行,但实际上根本不可能实现循环。此外,大部分装置对高盐度溶液的处理没有很好的效果。Further searches found that the Chinese invention patent with the patent application number 00109939.6 disclosed a spray propulsion ventilation evaporation-condensation seawater desalination process and device, and the Chinese invention patent with the patent application number 03144279.X disclosed a seawater evaporation tank drum Seawater desalination method of bubble method. Although these patents are feasible in principle, it is impossible to realize circulation at all in practice. Furthermore, most devices do not work well with high salinity solutions.
发明内容Contents of the invention
针对上述现有技术的缺陷和不足,本发明的目的在于提出一种在低温常压下运行的轻小型太阳能海水淡化装置及方法,其利用太阳能集热器加热循环介质,通过换热器使海水温度提高,且装置采用无毒工程塑料制造,解决了太阳能集热器和加湿器易被海水腐蚀的问题;加湿器采用喷淋加湿和填料塔加湿相结合,不易结垢,且提高了热交换效率和淡水产量;采用太阳能供电装置用于驱动水泵、风机的运转;装置在常压下运行,无需真空泵和气液分离器,无易损耗部件,降低了制造和运行维护成本。Aiming at the defects and deficiencies of the above-mentioned prior art, the object of the present invention is to propose a light and small solar seawater desalination device and method operating at low temperature and normal pressure, which utilizes a solar heat collector to heat the circulating medium, and the seawater is desalinated by a heat exchanger. The temperature is raised, and the device is made of non-toxic engineering plastics, which solves the problem that the solar collector and humidifier are easily corroded by seawater; the humidifier uses a combination of spray humidification and packed tower humidification, which is not easy to scale and improves heat exchange. Efficiency and fresh water output; solar power supply device is used to drive the operation of water pumps and fans; the device operates under normal pressure, without vacuum pump and gas-liquid separator, and without consumable parts, which reduces manufacturing and operation and maintenance costs.
为达到以上发明目的,本发明是通过以下技术方案实现的:In order to achieve the above object of the invention, the present invention is achieved through the following technical solutions:
一种轻小型太阳能海水淡化装置,包括料液加热系统、能源供给系统、空气加湿系统和空气除湿系统;A light and small solar seawater desalination device, including a feed liquid heating system, an energy supply system, an air humidification system and an air dehumidification system;
所述料液加热系统包括太阳能集热器、换热器、集热循环泵及储油箱,储油箱用于盛装加热循环介质,储油箱出口与集热循环泵进口相连,集热循环泵出口与换热器循环介质进口相连,换热器循环介质出口与太阳能集热器进口相连,太阳能集热器出口与储油箱进口相连;The feed liquid heating system includes a solar heat collector, a heat exchanger, a heat collecting circulation pump and an oil storage tank. The oil storage tank is used to hold the heating circulation medium. The inlet of the heat exchanger circulating medium is connected, the outlet of the circulating medium of the heat exchanger is connected with the inlet of the solar collector, and the outlet of the solar collector is connected with the inlet of the oil storage tank;
所述能源供给系统包括太阳能电池板、蓄电池和逆变器,所述太阳能电池板与蓄电池相连,所述蓄电池与逆变器相连,用于将直流电转换为交流电,所述逆变器分别与集热循环泵、料液泵、冷却水泵、风机、电加热器和其它用电设备相连接;The energy supply system includes a solar panel, a storage battery and an inverter, the solar panel is connected to the storage battery, the storage battery is connected to the inverter, and is used to convert direct current into alternating current, and the inverter is respectively connected to the set Heat circulation pump, material liquid pump, cooling water pump, fan, electric heater and other electrical equipment are connected;
所述空气加湿系统包括加湿器、蒸发喷淋器、壳体A、填料A、筛板A、流量控制器A、料液泵、电加热器、排水阀A和浓海水槽;所述加湿器的海水循环出口与料液泵入口相连,料液泵出口与换热器海水入口相连,连接管路上设置有流量控制器A,换热器海水出口与蒸发喷淋器相连,蒸发喷淋器位于加湿器内的上部,用于将加热后的海水喷淋至加湿器内;所述筛板A位于加湿器内的下部,且在海水液面上方,与加湿器内表面固定连接;所述填料A置于筛板A上方,海水在填料A表面铺展成膜,以增加换热面积;冷空气经由风机驱动进入加湿器内,冷空气向上流动的过程中与海水进行直接接触式热质交换,加热加湿后的热湿空气由加湿器顶部的热湿空气出口流出,并通过管路与除湿器热湿空气入口相连;经热质交换后的海水到达加湿器底部,进行下一次循环,海水到达一定浓度后经排水阀A排出,收集至浓海水槽中;所述电加热器位于加湿器下部,且在海水液面以下,用于在阴雨天情况下对海水进行加热;The air humidification system includes a humidifier, an evaporative sprinkler, a shell A, a filler A, a sieve plate A, a flow controller A, a material liquid pump, an electric heater, a drain valve A and a concentrated seawater tank; the humidifier The outlet of the seawater circulation is connected to the inlet of the feed liquid pump, the outlet of the feed liquid pump is connected to the seawater inlet of the heat exchanger, a flow controller A is installed on the connecting pipeline, and the seawater outlet of the heat exchanger is connected to the evaporation sprayer, which is located at The upper part of the humidifier is used to spray the heated seawater into the humidifier; the sieve plate A is located at the lower part of the humidifier and is fixedly connected to the inner surface of the humidifier above the seawater liquid level; the filler A is placed above the sieve plate A, and the seawater spreads to form a film on the surface of the filler A to increase the heat transfer area; the cold air is driven into the humidifier by the fan, and the cold air performs direct contact heat and mass exchange with the seawater during the upward flow. The hot and humid air after heating and humidification flows out from the hot and humid air outlet on the top of the humidifier, and is connected to the hot and humid air inlet of the dehumidifier through a pipeline; the seawater after heat and mass exchange reaches the bottom of the humidifier for the next cycle, and the seawater reaches the bottom of the humidifier. After a certain concentration, it is discharged through the drain valve A and collected in the concentrated seawater tank; the electric heater is located at the lower part of the humidifier and below the seawater liquid level, and is used to heat the seawater in rainy days;
所述空气除湿系统包括除湿器、冷却水喷淋器、壳体B、填料B、筛板B、冷却水泵、流量控制器B、排水阀B和淡水槽;所述除湿器的冷却水循环出口与冷却水泵入口相连,所述冷却水泵出口与冷却水喷淋器相连,连接管路上设有流量控制器B,冷却水喷淋器置于除湿器的上部,用于将冷却水喷淋至除湿器内;所述筛板B位于除湿器内的下部,且在海水液面上方,与除湿器内表面固定连接;所述填料B置于筛板B上方,冷却水在填料B表面铺展成膜,以增加换热面积;热湿空气通过管路进入除湿器内,热湿空气向上流动的过程中与冷却水进行直接接触式热质交换,降温除湿后的冷空气由除湿器顶部的冷空气出口流出,并通过管路与风机入口相连,进行下一次循环;冷凝产生的淡水流至除湿器底部,多余的淡水经排水阀B排出,收集至淡水槽中;The air dehumidification system includes a dehumidifier, a cooling water sprayer, a shell B, a filler B, a sieve plate B, a cooling water pump, a flow controller B, a drain valve B and a fresh water tank; the cooling water circulation outlet of the dehumidifier is connected to the The inlet of the cooling water pump is connected, and the outlet of the cooling water pump is connected to the cooling water sprayer. The connecting pipeline is provided with a flow controller B, and the cooling water sprayer is placed on the upper part of the dehumidifier for spraying the cooling water to the dehumidifier. Inside; the sieve plate B is located at the lower part of the dehumidifier, and is fixedly connected to the inner surface of the dehumidifier above the seawater liquid level; the filler B is placed above the sieve plate B, and the cooling water spreads on the surface of the filler B to form a film, In order to increase the heat exchange area; the hot and humid air enters the dehumidifier through the pipeline, and performs direct contact heat and mass exchange with the cooling water during the upward flow of the hot and humid air. It flows out and connects with the fan inlet through the pipeline for the next cycle; the fresh water generated by condensation flows to the bottom of the dehumidifier, and the excess fresh water is discharged through the drain valve B and collected in the fresh water tank;
所述风机位于除湿器外侧,用于将除湿器内的冷空气输送至加湿器内,且其与风量调节器相连接,用于控制入口风量,调节系统淡水生产速率;The fan is located outside the dehumidifier and is used to transport the cold air in the dehumidifier to the humidifier, and it is connected with the air volume regulator to control the inlet air volume and adjust the fresh water production rate of the system;
所述浓海水槽位于加湿器排水阀A下方,用于盛放浓海水;所述淡水槽位于除湿器排水阀B下方,用于盛放生产淡水。The concentrated seawater tank is located below the drain valve A of the humidifier, and is used to hold concentrated seawater; the fresh water tank is located below the drain valve B of the dehumidifier, and is used to hold fresh water for production.
进一步地,上述的轻小型太阳能海水淡化装置,还包括冷却盘管和冷却水槽;所述冷却盘管与冷却水泵出口相连,冷却盘管放置于冷水槽中,用于对冷却水降温,冷却盘管出口与冷却水喷淋器相连,连接管路上设有流量控制器B。Further, the light and small solar seawater desalination device described above also includes a cooling coil and a cooling water tank; the cooling coil is connected to the outlet of the cooling water pump, and the cooling coil is placed in the cold water tank for cooling the cooling water. The outlet of the pipe is connected with the cooling water sprayer, and a flow controller B is arranged on the connecting pipe.
进一步地,上述冷却盘管的材料为铜管、铝管、不锈钢管中的一种或两种以上的组合。Further, the material of the above-mentioned cooling coil is one or a combination of two or more of copper tubes, aluminum tubes, and stainless steel tubes.
进一步地,上述冷却盘管的表面增加有肋片,肋片的形式为绕片式、轧片式、串片式中的一种或两种以上的组合。Further, fins are added to the surface of the above-mentioned cooling coil, and the fins are in the form of winding sheet type, rolled sheet type, serial sheet type or a combination of two or more.
进一步地,上述太阳能集热器为平板型太阳能集热器、真空管太阳能集热器和热管型太阳能集热器中的一种或两种以上的组合。Further, the above-mentioned solar heat collector is one or a combination of two or more of flat plate solar heat collectors, vacuum tube solar heat collectors and heat pipe type solar heat collectors.
进一步地,上述太阳能集热器中的循环介质为导热油。Further, the circulating medium in the above solar heat collector is heat transfer oil.
进一步地,上述加湿器、除湿器的壳体为聚丙烯、聚乙烯、聚氯乙烯或玻璃钢材料中的一种或两种以上的组合,壳体外部包裹有保温材料,具有保温且防止被海水腐蚀的作用。Further, the shells of the above-mentioned humidifiers and dehumidifiers are made of polypropylene, polyethylene, polyvinyl chloride, or a combination of two or more materials, and the shells are wrapped with heat-insulating materials, which have the function of heat preservation and prevent seawater The role of corrosion.
进一步地,上述连接管路为聚丙烯、聚乙烯或聚氯乙烯材料的一种或两种以上的组合,管路外部包裹有保温材料。Further, the above-mentioned connecting pipeline is made of one or a combination of two or more materials of polypropylene, polyethylene or polyvinyl chloride, and the outside of the pipeline is wrapped with an insulating material.
进一步地,上述填料为塑料填料、陶瓷填料、玻璃钢填料中的一种或两种以上的组合,易清洗且不易被海水腐蚀。Further, the above-mentioned filler is one or a combination of two or more of plastic fillers, ceramic fillers, and fiberglass fillers, which are easy to clean and difficult to be corroded by seawater.
进一步地,上述填料的形状为拉西环、鲍尔环、阶梯环、弧鞍形、矩鞍形、环矩鞍形、球形中的一种或两种以上的组合。Further, the shape of the packing is one of Raschig ring, Pall ring, stepped ring, arc saddle, rectangular saddle, ring rectangular saddle, spherical, or a combination of two or more.
所述的轻小型太阳能海水淡化装置,其所处理的溶液包括但不局限于雨水、海水、苦咸水、工业废水、生活污水、垃圾渗滤液。The light and small solar seawater desalination device can treat solutions including but not limited to rainwater, seawater, brackish water, industrial waste water, domestic sewage, and landfill leachate.
所述的轻小型太阳能海水淡化装置,其处理溶液的盐浓度范围为0g/L至近饱和溶液对应盐浓度。In the light and small solar seawater desalination device, the salt concentration of the treatment solution ranges from 0 g/L to the corresponding salt concentration of a nearly saturated solution.
采用上述轻小型太阳能海水淡化装置进行海水淡化的方法,包括以下步骤:The method for desalinating seawater by using the light and small solar seawater desalination device described above comprises the following steps:
步骤1,高温循环介质经集热循环泵输送至换热器中,对待处理海水进行加热,然后进入太阳能集热器吸收太阳辐射能,升温后输送至储油箱,进行下一次循环;Step 1, the high-temperature circulating medium is transported to the heat exchanger by the heat collecting circulation pump, and the seawater to be treated is heated, and then enters the solar heat collector to absorb solar radiation energy, and is transported to the oil storage tank after heating up for the next cycle;
步骤2,待处理海水依次经过料液泵、流量控制器进入换热器,与高温循环介质进行换热,然后经蒸发喷淋器进入加湿器内,与加湿器内的填料A发生碰撞、铺展、破碎、飞溅;Step 2, the seawater to be treated enters the heat exchanger through the feed liquid pump and the flow controller in turn, exchanges heat with the high-temperature circulating medium, and then enters the humidifier through the evaporating sprayer, where it collides with the filler A in the humidifier and spreads , broken, splashed;
步骤3,不饱和冷空气经风机驱动进入加湿器下部,冷空气在加湿器内向上流动的过程中与海水进行直接接触式热质交换,空气被升温加湿,剩余的海水到达加湿器底部进行下一次循环,浓海水达到一定浓度后经排水阀A进入浓海水槽;Step 3, the unsaturated cold air is driven by the fan and enters the lower part of the humidifier. During the upward flow of the cold air in the humidifier, it conducts direct contact heat and mass exchange with seawater. The air is heated and humidified, and the remaining seawater reaches the bottom of the humidifier for down-flow In one cycle, the concentrated seawater enters the concentrated seawater tank through the drain valve A after reaching a certain concentration;
步骤4,升温加湿后的热湿空气经由管路输送至除湿器底部,在除湿器内向上流动的过程中与冷却水喷淋器喷淋的冷却水进行直接接触式热质交换,空气被降温除湿,之后从除湿器顶端冷空气出口排出,经由管路经风机驱动进入加湿器,进行下一次循环;Step 4: The heated and humidified hot and humid air is transported to the bottom of the dehumidifier through the pipeline, and in the process of flowing upwards in the dehumidifier, it conducts direct contact heat and mass exchange with the cooling water sprayed by the cooling water sprayer, and the air is cooled After dehumidification, it is discharged from the cold air outlet at the top of the dehumidifier, and enters the humidifier through the pipeline through the fan drive for the next cycle;
步骤5,除湿过程冷凝产生的淡水流至除湿器底部,经淡水循环出口进入冷却盘管,与冷却水槽中的冷却水进行换热,淡水被冷却后经流量控制器B、冷却水喷淋器进入除湿器,进行下一次除湿过程,多余的淡水经排水阀B进入淡水槽。Step 5, the fresh water generated by condensation in the dehumidification process flows to the bottom of the dehumidifier, enters the cooling coil through the fresh water circulation outlet, and exchanges heat with the cooling water in the cooling water tank. After the fresh water is cooled, it passes through the flow controller B and the cooling water sprayer Enter the dehumidifier for the next dehumidification process, and the excess fresh water enters the fresh water tank through the drain valve B.
本发明的有益效果为:The beneficial effects of the present invention are:
本发明所述装置利用太阳能集热器将辐射能转换为热能,储存在储油箱中,用于加热待处理海水;采用电加热作为备用方案,确保装置可在阴雨天正常运行。The device of the present invention converts radiant energy into thermal energy by using a solar heat collector and stores it in an oil storage tank for heating seawater to be treated; electric heating is used as a backup solution to ensure that the device can operate normally in rainy days.
本发明所述装置利用太阳能电池板将辐射能转换为电能,储存在蓄电池中,供装置中的水泵、风机或其它用电设备运行使用,无额外消耗电能。The device of the present invention converts radiant energy into electric energy by using solar panels, and stores it in a storage battery for operation of water pumps, fans or other electric equipment in the device without additional consumption of electric energy.
本发明所述装置采用喷淋和填料塔相结合,辅之以空气强制加湿循环流动溶液的工艺方法进行空气加湿除湿,提高了装置的运行效率。The device of the invention adopts the combination of spraying and packing tower, supplemented by the technological method of forced air humidification and circulation flow solution to carry out air humidification and dehumidification, which improves the operating efficiency of the device.
本发明所述装置在溶液温度较低(<45℃)时也可稳定运行,且产水量和产水品质稳定可靠。The device of the invention can operate stably even when the temperature of the solution is low (<45° C.), and the water production volume and water quality are stable and reliable.
本发明所述装置在常压下运行,无需真空泵和气液分离器,填料、壳体材质采用无毒非金属材料,无消耗易损部件,使用寿命长,装置制造成本和后期运行维护成本低,提高了产品竞争力。The device of the present invention operates under normal pressure without the need for a vacuum pump and a gas-liquid separator. The material of the filler and the shell is non-toxic and non-metallic, and there are no consumable and vulnerable parts. The service life is long, and the manufacturing cost of the device and the cost of later operation and maintenance are low. Improve product competitiveness.
本发明所述装置结构简单紧凑,小型化、模块化,运输方便,规模可调,可多级串联使用,能够全自动化运行控制,无人值守,使用方便,拓宽了装置的应用场所。The device of the present invention is simple and compact in structure, miniaturized and modularized, convenient to transport, adjustable in scale, can be used in series in multiple stages, capable of fully automatic operation control, unattended, easy to use, and broadens the application field of the device.
附图说明Description of drawings
图1是本发明所述轻小型太阳能海水淡化装置示意图。Fig. 1 is a schematic diagram of a light and small solar seawater desalination device according to the present invention.
图2是本发明所述轻小型太阳能海水淡化装置长时间运行结果图。Fig. 2 is a long-term operation result diagram of the light and small solar seawater desalination device of the present invention.
图中:1料液加热系统;2太阳能集热器;3换热器;4集热循环泵;5储油箱;6空气加湿系统;7加湿器;8蒸发喷淋器;9壳体A;10填料A;11筛板A;12流量控制器A;13料液泵;14排水阀A;15浓海水槽;16能源供给系统;17太阳能电池板;18蓄电池;19逆变器;20风量调节器;21风机;22电加热器;23空气除湿系统;24除湿器;25冷却水喷淋器;26壳体B;27填料B;28筛板B;29冷却水泵;30流量控制器B;31排水阀B;32淡水槽;33冷却盘管;34冷却水槽。In the figure: 1 material liquid heating system; 2 solar heat collector; 3 heat exchanger; 4 heat collecting circulation pump; 5 oil storage tank; 6 air humidification system; 7 humidifier; 10 filler A; 11 sieve plate A; 12 flow controller A; 13 liquid pump; 14 drain valve A; 15 concentrated seawater tank; 16 energy supply system; 17 solar panel; 18 battery; Regulator; 21 fan; 22 electric heater; 23 air dehumidification system; 24 dehumidifier; 25 cooling water sprayer; 26 shell B; ; 31 drain valve B; 32 fresh water tank; 33 cooling coil; 34 cooling water tank.
具体实施方式Detailed ways
下面结合附图对本发明的具体实施例作详细说明。应当说明的是,本实施例仅为以本发明技术方案为前提下的详细实施方案和具体操作过程,并非用于限定本发明的保护范围。凡在本发明的精神和原则内所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。Specific embodiments of the present invention will be described in detail below in conjunction with the accompanying drawings. It should be noted that this embodiment is only a detailed implementation and specific operation process based on the technical solution of the present invention, and is not intended to limit the protection scope of the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.
实施例1Example 1
如图1,轻小型太阳能海水淡化装置由料液加热系统1、能源供给系统16、空气加湿系统6和空气除湿系统23四部分组成。As shown in Figure 1, the light and small solar seawater desalination device is composed of four parts: feed liquid heating system 1, energy supply system 16, air humidification system 6 and air dehumidification system 23.
所述料液加热系统1包括太阳能集热器2、换热器3、集热循环泵4及储油箱5,将太阳的辐射能转换为热能,对循环介质加热以提供热源,然后用于待处理海水的加热;储油箱用于盛装加热循环介质,储油箱出口与集热循环泵进口相连,集热循环泵出口与太阳能集热器进口相连,循环介质经集热循环泵输送进入太阳能集热器,通过吸收太阳辐射能而提高温度;太阳能集热器出口与换热器循环介质进口相连,用于循环介质和待加热的海水进行热量传递;换热器循环介质出口与储油箱相连。The feed liquid heating system 1 includes a solar heat collector 2, a heat exchanger 3, a heat collecting circulation pump 4 and an oil storage tank 5, which convert the sun's radiant energy into heat energy, heat the circulating medium to provide a heat source, and then use it for the Heating of seawater; the oil storage tank is used to hold the heating circulation medium, the outlet of the oil storage tank is connected to the inlet of the collector circulation pump, the outlet of the collector circulation pump is connected to the inlet of the solar collector, and the circulation medium is transported into the solar collector through the collector circulation pump The solar collector increases the temperature by absorbing solar radiation energy; the outlet of the solar collector is connected to the inlet of the circulating medium of the heat exchanger for heat transfer between the circulating medium and the seawater to be heated; the outlet of the circulating medium of the heat exchanger is connected to the oil storage tank.
所述能源供给系统16包括:太阳能电池板17、蓄电池18和逆变器19,用于将太阳的辐射能转换为电能,储存在蓄电池中,供装置中的用电设备运行使用;所述太阳能电池板与蓄电池相连,所述蓄电池与逆变器相连,用于将直流电转换为交流电,所述逆变器与集热循环泵4、料液泵13、冷却水泵29、风机21、电加热器22和其它用电设备相连接。The energy supply system 16 includes: a solar panel 17, a storage battery 18 and an inverter 19, which are used to convert the sun's radiant energy into electrical energy, which is stored in the storage battery and used for the operation of electrical equipment in the device; The battery board is connected with the storage battery, and the storage battery is connected with the inverter for converting direct current into alternating current. The inverter is connected with the heat collection circulation pump 4, the material liquid pump 13, the cooling water pump 29, the blower fan 21, and the electric heater 22 is connected with other electrical equipment.
所述空气加湿系统6包括:加湿器7、蒸发喷淋器8、壳体A9、填料A10、筛板A11、流量控制器A12、料液泵13、电加热器22、排水阀14和浓海水槽15;所述加湿器的海水循环出口与料液泵入口相连,料液泵出口与换热器海水入口相连,连接管路上设有流量控制器A,换热器海水出口与蒸发喷淋器相连,蒸发喷淋器位于加湿器内的上部,用于将加热后的海水喷淋至加湿器内;所述筛板A位于加湿器内的下部,且在海水液面上方,与加湿器内表面固定连接;所述填料A置于筛板A上方,海水在填料A表面铺展成膜,以增加换热面积;冷空气经由风机21驱动进入加湿器内,冷空气向上流动的过程中与海水进行直接接触式热质交换,加热加湿后的热湿空气由加湿器顶部的热湿空气出口流出,并通过管路与除湿器24热湿空气入口相连;所述海水经热质交换后到达加湿器底部,进行下一次循环,海水到达一定浓度后经排水阀A排出,收集至浓海水槽中;所述电加热器位于加湿器下部,且在海水液面以下,用于在阴雨天情况下对海水进行加热。The air humidification system 6 includes: a humidifier 7, an evaporative sprayer 8, a housing A9, a filler A10, a sieve plate A11, a flow controller A12, a material liquid pump 13, an electric heater 22, a drain valve 14 and a dense sea Water tank 15; the seawater circulation outlet of the humidifier is connected to the inlet of the feed liquid pump, the outlet of the feed liquid pump is connected to the seawater inlet of the heat exchanger, a flow controller A is arranged on the connecting pipeline, and the seawater outlet of the heat exchanger is connected to the evaporation sprayer Connected, the evaporation sprayer is located in the upper part of the humidifier, used to spray the heated seawater into the humidifier; the sieve plate A is located in the lower part of the humidifier, and above the seawater liquid level, and the humidifier The surface is fixedly connected; the filler A is placed above the sieve plate A, and the seawater spreads on the surface of the filler A to form a film to increase the heat exchange area; the cold air is driven into the humidifier by the fan 21, and the cold air flows upwards with the seawater Carry out direct contact heat and mass exchange, the hot and humid air after heating and humidification flows out from the hot and humid air outlet on the top of the humidifier, and is connected with the hot and humid air inlet of the dehumidifier 24 through a pipeline; the seawater reaches the humidification after heat and mass exchange At the bottom of the humidifier, the next cycle will be carried out. After the seawater reaches a certain concentration, it will be discharged through the drain valve A and collected in the concentrated seawater tank; Seawater is heated.
所述空气除湿系统23包括:除湿器24、冷却水喷淋器25、壳体B26、填料B27、筛板B28、冷却水泵29、流量控制器B30、排水阀B31、淡水槽32、冷却盘管33和冷却水槽34;所述除湿器的冷却水循环出口与冷却水泵入口相连,所述冷却水泵出口与冷却盘管入口相连,冷却盘管置于冷水槽中,用于对冷却水降温,冷却盘管出口与冷却水喷淋器相连,连接管路上设有流量控制器B,冷却水喷淋器置于除湿器的上部,用于将冷却水喷淋至除湿器内;所述筛板B位于除湿器内的下部,且在海水液面上方,与除湿器内表面固定连接;所述填料B置于筛板B上方,冷却水在填料B表面铺展成膜,以增加换热面积;热湿空气通过管路进入加湿器内,热湿空气向上流动的过程中与冷却水进行直接接触式热质交换,降温除湿后的冷空气由除湿器顶部的冷空气出口流出,并通过管路与风机21入口相连,进行下一次循环;冷凝产生的淡水流至除湿器底部,多余的淡水经排水阀B排出,收集至淡水槽中。The air dehumidification system 23 includes: a dehumidifier 24, a cooling water sprayer 25, a housing B26, a filler B27, a sieve plate B28, a cooling water pump 29, a flow controller B30, a drain valve B31, a fresh water tank 32, and a cooling coil 33 and cooling water tank 34; the cooling water circulation outlet of the dehumidifier is connected with the cooling water pump inlet, and the cooling water pump outlet is connected with the cooling coil inlet, and the cooling coil is placed in the cold water tank for cooling the cooling water, and the cooling plate The outlet of the pipe is connected to the cooling water sprayer, and a flow controller B is installed on the connecting pipeline. The cooling water sprayer is placed on the upper part of the dehumidifier for spraying cooling water into the dehumidifier; the sieve plate B is located at The lower part of the dehumidifier is fixedly connected to the inner surface of the dehumidifier above the seawater liquid level; the filler B is placed above the sieve plate B, and the cooling water spreads on the surface of the filler B to increase the heat exchange area; The air enters the humidifier through the pipeline, and the hot and humid air conducts direct contact heat and mass exchange with the cooling water during the upward flow. The cold air after cooling and dehumidification flows out from the cold air outlet on the top of the dehumidifier, and passes through the pipeline and the fan. The 21 inlets are connected for the next cycle; the fresh water produced by condensation flows to the bottom of the dehumidifier, and the excess fresh water is discharged through the drain valve B and collected into the fresh water tank.
所述风机21位于除湿器外侧,用于将除湿器内的冷空气输送至加湿器内,且其与风量调节器20相连接,用于控制入口风量,调节系统淡水生产速率。The fan 21 is located outside the dehumidifier and is used to transport the cold air in the dehumidifier to the humidifier, and it is connected with the air volume regulator 20 to control the inlet air volume and adjust the fresh water production rate of the system.
实施例2Example 2
在本实施例中,选用实施例1中的轻小型太阳能海水淡化装置作为实验装置,以进行装置长时间稳定运行测试实验。本实施例中选用盐浓度为3.5wt%的海水作为待处理溶液,蒸发喷淋器中溶液温度设定为55℃,调节流量控制器使溶液的循环流量为60L/h,冷却水的循环流量为50L/h,冷却水温度控制在20~25℃。调节风量调节器使系统循环风速为2.5m/s(2.65m3/min),装置连续运行8小时。系统产水量和脱盐率结果如图2所示。可以看出,系统单位时间产水量保持相对稳定的状态,在1600g/h左右。脱盐率也一直保持在99.98%以上。该结果表明,本发明所述的轻小型太阳能海水淡化装置可以长时间稳定运行,装置使用寿命长。In this embodiment, the light and small solar seawater desalination device in Embodiment 1 is selected as the experimental device to conduct a long-term stable operation test experiment of the device. In this embodiment, the seawater with a salt concentration of 3.5wt% is selected as the solution to be treated, the temperature of the solution in the evaporation shower is set at 55°C, the flow controller is adjusted to make the circulation flow of the solution 60L/h, and the circulation flow of the cooling water It is 50L/h, and the cooling water temperature is controlled at 20-25°C. Adjust the air volume regulator to make the circulating wind speed of the system 2.5m/s (2.65m 3 /min), and the device runs continuously for 8 hours. The results of water production and desalination rate of the system are shown in Figure 2. It can be seen that the water production per unit time of the system remains relatively stable at around 1600g/h. The desalination rate has also been maintained above 99.98%. The result shows that the light and small solar seawater desalination device of the present invention can run stably for a long time, and the device has a long service life.
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