CN112239249B - Reverse osmosis sea water desalination system based on electric non-uniform concentration field - Google Patents
Reverse osmosis sea water desalination system based on electric non-uniform concentration field Download PDFInfo
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- 238000010612 desalination reaction Methods 0.000 title claims abstract description 67
- 238000001223 reverse osmosis Methods 0.000 title claims abstract description 43
- 239000013535 sea water Substances 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 65
- 239000013505 freshwater Substances 0.000 claims abstract description 49
- 239000012528 membrane Substances 0.000 claims abstract description 26
- 239000012267 brine Substances 0.000 claims abstract description 25
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims abstract description 25
- 230000005684 electric field Effects 0.000 claims description 6
- 150000003839 salts Chemical class 0.000 description 16
- 238000005516 engineering process Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 230000003204 osmotic effect Effects 0.000 description 6
- 150000001450 anions Chemical class 0.000 description 4
- 150000001768 cations Chemical class 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 2
- XZPVPNZTYPUODG-UHFFFAOYSA-M sodium;chloride;dihydrate Chemical compound O.O.[Na+].[Cl-] XZPVPNZTYPUODG-UHFFFAOYSA-M 0.000 description 2
- 241000282414 Homo sapiens Species 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
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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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
- C02F1/4698—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electro-osmosis
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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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- 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
- Y02A20/131—Reverse-osmosis
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Abstract
Description
技术领域technical field
本发明属于海水淡化设备技术领域,特别是一种基于电致不均匀浓度场的反渗透海水淡化系统。The invention belongs to the technical field of seawater desalination equipment, in particular to a reverse osmosis seawater desalination system based on an electrically inhomogeneous concentration field.
背景技术Background technique
在由于人口增长以及人类对水资源的浪费与污染,淡水资源危机正不断加剧,据专家估计,至2025年,全球将有近一半人口生活的地区面对严重缺水的问题。在地球约14.5亿立方米的总水量中,人类可直接利用的淡水资源仅占其中的0.26%,海水却占了97.5%,将储量丰富的海水(盐水)进行淡化,成为可利用的淡水,是解决水资源不足难题的可靠与重要途径。Due to population growth and human waste and pollution of water resources, the crisis of fresh water resources is intensifying. According to expert estimates, by 2025, nearly half of the world's population will face severe water shortages. Among the total water volume of about 1.45 billion cubic meters on the earth, the fresh water resources directly usable by human beings account for only 0.26%, while the seawater accounts for 97.5%. The abundant seawater (salt water) is desalinated and becomes usable fresh water. It is a reliable and important way to solve the problem of insufficient water resources.
众多海水淡化技术中,以反渗透原理为基础的反渗透海水淡化技术具有效率高、能耗低、设备紧凑美观等多方面优点,被认为是目前主导海水淡化市场领先的工艺。以我国为例,截至2015年底,全国应用反渗透技术的工程有106个,产水规模65.45万t/d,占全国总产水规模的64.88%。Among many seawater desalination technologies, the reverse osmosis seawater desalination technology based on the principle of reverse osmosis has many advantages such as high efficiency, low energy consumption, compact and beautiful equipment, etc., and is considered to be the leading technology in the seawater desalination market. Taking my country as an example, as of the end of 2015, there were 106 projects applying reverse osmosis technology nationwide, with a water production scale of 654,500 t/d, accounting for 64.88% of the total national water production scale.
自然状态下,将盐水与淡水用只有水分子得以透过而溶质(盐)分子无法透过的半透膜(反渗透膜)隔开时,淡水侧的水分子会流到盐水一侧,达到平衡状态后盐水侧的液面高于淡水侧,这个液位差形成的压差称为渗透压。在盐水侧施加超过渗透压的压力时,盐水中的水分子会向淡水侧流动,这一过程即为反渗透。渗透压的本质实际体现了盐水中溶质分子对水分子的吸引力:对于纯水,水分子可以自由的通过反渗透膜;对于盐水,溶质分子会对水分子有一定的吸引力,导致不仅溶质分子不能通过反渗透膜,被其吸引的水分子也无法自由透过反渗透膜,宏观上的体现就是渗透压了。对于盐水,要想使其中的水分子还能透过反渗透膜,只能靠外界加压来实现了,反渗透海水淡化就是利用这一原理实现淡水的制取,现有的反渗透海水淡化技术是用高压泵将盐水加压并输送到反渗透膜组件实现反渗透,用来制取淡水。In the natural state, when salt water and fresh water are separated by a semi-permeable membrane (reverse osmosis membrane) that only water molecules can pass through but solute (salt) molecules cannot pass through, the water molecules on the fresh water side will flow to the salt water side, reaching After the equilibrium state, the liquid level on the brine side is higher than that on the fresh water side, and the pressure difference formed by this liquid level difference is called osmotic pressure. When a pressure exceeding the osmotic pressure is applied on the salt water side, the water molecules in the salt water will flow to the fresh water side, and this process is called reverse osmosis. The essence of osmotic pressure actually reflects the attraction of solute molecules to water molecules in salt water: for pure water, water molecules can pass through the reverse osmosis membrane freely; for salt water, solute molecules will have a certain attraction to water molecules, resulting in not only solute Molecules cannot pass through the reverse osmosis membrane, and the water molecules attracted by it cannot freely pass through the reverse osmosis membrane. The macroscopic manifestation is osmotic pressure. For salt water, if the water molecules in it can pass through the reverse osmosis membrane, it can only be realized by external pressure. The reverse osmosis seawater desalination is to use this principle to realize the production of fresh water. The existing reverse osmosis seawater desalination The technology is to use a high-pressure pump to pressurize the brine and transport it to the reverse osmosis membrane module to achieve reverse osmosis, which is used to produce fresh water.
现有技术存在的问题是:为了使用反渗透膜进行盐水淡化,必须将盐水源与高压泵想连接,要使用高压泵将盐水侧加到很高的压力,这会耗费巨大能量;高压泵产生的高压液体会对反渗透膜造成伤害,使膜破裂;高压泵造价昂贵,加之预处理和基本建设等诸多费用加大了反渗透技术淡化成本;高压泵运行维护难度高,系统结构复杂。。The problem existing in the prior art is: in order to use the reverse osmosis membrane to desalinate the brine, the brine source must be connected with the high-pressure pump, and the high-pressure pump is used to add the brine side to a very high pressure, which will consume huge energy; the high-pressure pump produces The high-pressure liquid will cause damage to the reverse osmosis membrane and cause the membrane to rupture; the high-pressure pump is expensive, and many costs such as pretreatment and capital construction have increased the desalination cost of the reverse osmosis technology; the operation and maintenance of the high-pressure pump is difficult and the system structure is complex. .
发明内容Contents of the invention
本发明的目的在于提供一种基于电致不均匀浓度场的反渗透海水淡化系统,成本低、性能系数高、结构简单。The object of the present invention is to provide a reverse osmosis seawater desalination system based on the electro-inhomogeneous concentration field, which has low cost, high coefficient of performance and simple structure.
实现本发明目的的技术解决方案为:The technical solution that realizes the object of the present invention is:
一种基于电致不均匀浓度场的反渗透海水淡化系统,包括淡化室1、淡水池2、浓水池3,所述淡化室盐水入口11与外界盐水水源相连,淡化室淡水出口12与淡水池2淡水入口21相连,淡化室浓水出口13与浓水池3浓水入口31相连;还包括不均匀浓度场淡化功能单元;所述不均匀浓度场淡化功能单元包括至少一个电极对101和反渗透膜102;所述电极对101置于淡化室1内,反渗透膜102置于淡化室淡水出口12处。A reverse osmosis seawater desalination system based on an electro-induced non-uniform concentration field, comprising a
本发明与现有技术相比,其显著优点为:Compared with the prior art, the present invention has the remarkable advantages of:
1、成本低,性能系数高:本发明用电致不均匀浓度场进行反渗透盐水淡化,电极产生电场将溶质分子阴、阳离子吸引到电极表面及电极附近,在淡化室中产生了浓度不均匀的区域,盐水中浓度低至0的区域可视为淡水区域,该区域不存在渗透压,水分子可自由透过反渗透膜,起到盐溶质分子与水分子相分离的效果。在此过程中,无需要高压水泵对盐水进行加压,大大降低了成本;减少了产生高压的能耗,产生节能效果,性能系数高。1. Low cost and high coefficient of performance: the present invention uses an electro-inhomogeneous concentration field to desalinate reverse osmosis brine, and the electrode generates an electric field to attract solute molecules anions and cations to the surface of the electrode and near the electrode, resulting in uneven concentration in the desalination chamber The area where the concentration of salt water is as low as 0 can be regarded as a fresh water area. There is no osmotic pressure in this area, and water molecules can freely pass through the reverse osmosis membrane, which has the effect of separating salt solute molecules from water molecules. In this process, there is no need for a high-pressure water pump to pressurize the brine, which greatly reduces the cost; reduces the energy consumption for generating high pressure, produces energy-saving effects, and has a high performance coefficient.
2、结构简单:除去了高压水泵,减少了系统相关的部件,降低了能耗,使结构更为简单,维护更加便利,也提高了系统的寿命。。2. Simple structure: The high-pressure water pump is removed, system-related components are reduced, energy consumption is reduced, the structure is simpler, maintenance is more convenient, and the life of the system is also improved. .
下面结合附图和具体实施方式对本发明作进一步的详细描述。The present invention will be further described in detail below in conjunction with the accompanying drawings and specific embodiments.
附图说明Description of drawings
图1为本发明基于电致不均匀浓度场的反渗透盐水淡化系统的结构示意图。Fig. 1 is a structural schematic diagram of a reverse osmosis brine desalination system based on an electrically non-uniform concentration field according to the present invention.
图中,1淡化室,11淡化室盐水入口,12淡化室淡水出口,101电极对,102反渗透膜,13淡化室浓水出口,In the figure, 1 desalination chamber, 11 brine inlet of desalination chamber, 12 fresh water outlet of desalination chamber, 101 electrode pair, 102 reverse osmosis membrane, 13 concentrated water outlet of desalination chamber,
2淡水池,21淡水池淡水入口,2 fresh water pools, 21 fresh water pool fresh water inlets,
3浓水池,31浓水池浓水入口。3 thick water pools, 31 thick water pool thick water inlets.
具体实施方式Detailed ways
如图1所示,本发明基于电致不均匀浓度场的反渗透海水淡化系统,包括淡化室1、淡水池2、浓水池3,所述淡化室盐水入口11与外界盐水水源相连,淡化室淡水出口12与淡水池2淡水入口21相连,淡化室浓水出口13与浓水池3浓水入口31相连。As shown in Figure 1, the reverse osmosis seawater desalination system based on the electro-inhomogeneous concentration field of the present invention includes a
还包括不均匀浓度场淡化功能单元;It also includes a functional unit for inhomogeneous concentration field desalination;
所述不均匀浓度场淡化功能单元包括至少一个电极对101和反渗透膜102;The non-uniform concentration field desalination functional unit includes at least one
所述电极对101置于淡化室1内,反渗透膜102置于淡化室淡水出口12处。The
优选地,Preferably,
所述反渗透膜102全覆盖淡化室淡水出口12与淡水池2淡水入口21的水通路。The
反渗透膜102覆盖全部或部分的淡化室淡水出口12,未覆盖部分盐水无法通过。从而保证淡水的纯度。The
优选地,Preferably,
所述电极对101电场方向与淡化室盐水入口11与淡水出口12的连线垂直。The direction of the electric field of the
电极对101可以是一对,也可以是多对。电极对外接可再生能源发电装置。The
本发明基于电致不均匀浓度场的反渗透盐水淡化系统的工作原理为:The working principle of the reverse osmosis brine desalination system based on the electro-inhomogeneous concentration field of the present invention is as follows:
电极通电后产生电场将溶质分子阴、阳离子吸引到电极表面及电极附近,在淡化室中产生了浓度不均匀的区域,盐水中浓度低至0的区域可视为淡水区域,该区域不存在渗透压,水分子可自由透过反渗透膜,起到盐溶质分子与水分子相分离的效果。在此过程中,无需要高压水泵对盐水进行加压,大大降低了成本;减少了产生高压的能耗,产生节能效果,其详细工作过程如下:After the electrode is energized, an electric field is generated to attract the anion and cation of the solute molecules to the surface of the electrode and near the electrode, resulting in an area of uneven concentration in the desalination chamber. The area with a concentration as low as 0 in the brine can be regarded as a fresh water area, and there is no penetration in this area. Under pressure, water molecules can freely pass through the reverse osmosis membrane, which has the effect of separating salt solute molecules from water molecules. In this process, there is no need for a high-pressure water pump to pressurize the brine, which greatly reduces the cost; reduces the energy consumption for generating high pressure, and produces energy-saving effects. The detailed working process is as follows:
淡化室盐水入口与外界盐水水源相连,根据水位的高低,盐水可在重力作用下或采用普通低压水泵将盐水注入淡化室中。淡化室中放置有一对或多对电极,电极对于外界电源相连,如太阳能电池等。电极通电后在淡化室内产生电场。盐水中的溶质电解质的阳离子和阴离子在电场作用下运动,阳离子向阴极迁移,阴离子向阳极迁移;迁移使淡化室中盐水浓度不再均匀,电极表面及附近浓度较高,离电极距离较远处浓度较低,甚至出现盐水浓度为0的区域;浓度低至0的区域渗透压为0,在没有高压泵加压的情况下此处的水分子也可自由透过反渗透膜;淡化室淡水出口12与淡水池2的淡水入口21相连,纯水通过反渗透膜进入淡水池中,实现了盐水的淡化与纯水的获取;无法通过反渗透膜的盐水浓度变高,淡化室浓水出口13与浓水池3的浓水入口31相连,浓盐水进入浓水池中可作为其他回收利用的材料。此过程可持续进行。The brine inlet of the desalination chamber is connected with the external brine water source. According to the water level, the brine can be injected into the desalination chamber under the action of gravity or by ordinary low-pressure water pump. One or more pairs of electrodes are placed in the desalination chamber, and the electrodes are connected to external power sources, such as solar cells. After the electrodes are energized, an electric field is generated in the desalination chamber. The cations and anions of the solute electrolyte in the brine move under the action of the electric field, the cations migrate to the cathode, and the anions migrate to the anode; the migration makes the concentration of the brine in the desalination chamber no longer uniform, the concentration of the electrode surface and nearby is higher, and the distance from the electrode is farther away The concentration is low, and even the area where the concentration of brine is 0; the osmotic pressure of the area where the concentration is as low as 0 is 0, and the water molecules here can freely pass through the reverse osmosis membrane without the pressure of the high-pressure pump; fresh water in the desalination room The
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