CN2401538Y - Magnetic ion sieve sea water desalination device - Google Patents
Magnetic ion sieve sea water desalination device Download PDFInfo
- Publication number
- CN2401538Y CN2401538Y CN99240579U CN99240579U CN2401538Y CN 2401538 Y CN2401538 Y CN 2401538Y CN 99240579 U CN99240579 U CN 99240579U CN 99240579 U CN99240579 U CN 99240579U CN 2401538 Y CN2401538 Y CN 2401538Y
- Authority
- CN
- China
- Prior art keywords
- ion
- water
- reverse osmosis
- osmosis membrane
- base
- 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
- 239000013535 sea water Substances 0.000 title claims abstract description 33
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 102
- 239000012528 membrane Substances 0.000 claims abstract description 45
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 42
- 229910001172 neodymium magnet Inorganic materials 0.000 claims abstract description 8
- 230000005389 magnetism Effects 0.000 claims abstract 5
- 238000002955 isolation Methods 0.000 claims 6
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims 1
- 230000007797 corrosion Effects 0.000 abstract description 3
- 238000005260 corrosion Methods 0.000 abstract description 3
- 238000003487 electrochemical reaction Methods 0.000 abstract description 3
- 238000005194 fractionation Methods 0.000 abstract 6
- 238000001914 filtration Methods 0.000 abstract 2
- 150000002500 ions Chemical class 0.000 description 54
- 238000000926 separation method Methods 0.000 description 34
- 230000000694 effects Effects 0.000 description 8
- 238000009296 electrodeionization Methods 0.000 description 6
- 230000005484 gravity Effects 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 239000012535 impurity Substances 0.000 description 5
- 238000009434 installation Methods 0.000 description 5
- 230000003204 osmotic effect Effects 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- 239000000696 magnetic material Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000000909 electrodialysis Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000005381 potential energy Methods 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
Images
Classifications
-
- 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
- Y02A20/131—Reverse-osmosis
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
本实用新型属于海水淡化领域,具体地说涉及一种磁离子筛海水淡化装置。The utility model belongs to the field of seawater desalination, in particular to a magnetic ion sieve seawater desalination device.
目前世界范围内的海水淡化技术主要有以下几种:At present, the seawater desalination technologies in the world mainly include the following types:
1.反渗透 Reverse Osmosis (RO)1. Reverse Osmosis Reverse Osmosis (RO)
2.电去电离作用 Electrodeionization (EDI)2. Electrodeionization (EDI)
3.反电渗析 Electrodialysis Reversal (EDR)3. Electrodialysis Reversal (EDR)
运用上述海水淡化技术制造出来的海水淡化装置,主要有如下的不足:采用反渗透法,由于要克服渗透压,通常要较大的工作压力,如海水的渗透压约为2.7MPa,而工作压力则用10.5Mpa,要实现这样的压力就需耗费相当的能源,并对装置的密封性提出了较高的要求。电去电离作用和反电渗析以直流电作为动力,电去电离作用一般不直接处理海水,而是要先用反渗透法对海水进行预处理,否则能耗及对设备的损耗都较大,比较适用于高纯水的生产,而不适宜于大批量的海水处理。The seawater desalination device manufactured by using the above-mentioned seawater desalination technology mainly has the following deficiencies: the reverse osmosis method needs to overcome the osmotic pressure, usually requires a relatively high working pressure, such as the osmotic pressure of seawater is about 2.7MPa, and the working pressure Then use 10.5Mpa, to achieve such a pressure will consume a considerable amount of energy, and put forward higher requirements for the sealing of the device. Electrodeionization and reverse electrodialysis use direct current as power. Electrodeionization generally does not directly treat seawater, but first uses reverse osmosis to pretreat seawater. Otherwise, the energy consumption and equipment loss will be relatively large. It is suitable for the production of high-purity water, but not suitable for large-scale seawater treatment.
本实用新型的目的就是为了克服上述技术的不足,而提供一种磁离子筛海水淡化装置,该装置节省能源,使海水淡化的成本相比现有技术大幅降低,从而使海水淡化技术完全实用化。The purpose of this utility model is to overcome the deficiencies of the above-mentioned technologies, and provide a magnetic ion sieve seawater desalination device, which saves energy and greatly reduces the cost of seawater desalination compared with the existing technology, thereby making the seawater desalination technology fully practical .
磁离子筛海水淡化装置,包括进水储水箱、淡化水储存箱,其特征在于:还包括离子分离箱,离子分离箱由NdFeB永磁磁极对、装有反渗透膜的过滤管和有过滤管安插孔的底座组成;NdFeB永磁磁极对相对安装在离子分离箱的侧壁上,装有反渗透膜的过滤管固定于底座过滤管安插孔上,其上端装有反渗透膜部分插入磁场空间的下端;进水储水箱与离子分离箱相接,淡化水储存箱与离子分离箱相接。The magnetic ion sieve seawater desalination device includes an inlet water storage tank and a desalinated water storage tank, and is characterized in that it also includes an ion separation box. The base of the installation hole is composed of; the NdFeB permanent magnet pole pair is relatively installed on the side wall of the ion separation box, the filter tube equipped with the reverse osmosis membrane is fixed on the installation hole of the filter tube of the base, and the upper end of the reverse osmosis membrane is partially inserted The lower end of the magnetic field space; the water inlet storage tank is connected with the ion separation box, and the desalinated water storage tank is connected with the ion separation box.
由于本实用新型采用NdFeB永磁磁极对,将分子运动的动能作为主要的离子分离的动力,只借助水压差来驱动水分子透过反渗透膜而消耗了一些能量,所利用的外部能源就是这很小的水的势能差,大大低于反渗透中制造克服渗透压的外加高压力所耗费的能源;不需要电能和电极,从而极大缓解了电化学反应所产生的腐蚀作用。Since the utility model adopts NdFeB permanent magnet pole pairs, the kinetic energy of molecular motion is used as the main power of ion separation, and some energy is consumed by driving water molecules through the reverse osmosis membrane only by water pressure difference, and the external energy used is The potential energy difference of this small water is much lower than the energy consumed in reverse osmosis to create an additional high pressure to overcome the osmotic pressure; no electric energy and electrodes are needed, thus greatly alleviating the corrosion caused by the electrochemical reaction.
图1是本实用新型结构的正面示意图;Fig. 1 is the front schematic diagram of structure of the present utility model;
图2是本实用新型结构的侧面示意图;Fig. 2 is the side schematic diagram of structure of the present utility model;
图3是离子分离箱的俯视图。Fig. 3 is a top view of the ion separation box.
下面结合附图详细说明。Describe in detail below in conjunction with accompanying drawing.
如图所示,1是进水管,2是水箱,3是进水过滤板,4是离子分离箱,5是永磁磁极对N极,6是永磁磁极对S极,7是软磁材料板,8是装有反渗透膜套的过滤管,9是浓缩水排放口,10是淡化水储存箱,11是淡化水出水管,12是支架。As shown in the figure, 1 is the water inlet pipe, 2 is the water tank, 3 is the water inlet filter plate, 4 is the ion separation box, 5 is the permanent magnet pole pair N pole, 6 is the permanent magnet pole pair S pole, 7 is the soft magnetic material Plate, 8 is a filter tube equipped with a reverse osmosis membrane cover, 9 is a concentrated water discharge outlet, 10 is a desalinated water storage tank, 11 is a desalinated water outlet pipe, and 12 is a support.
磁离子筛海水淡化装置,包括进水储水箱、淡化水储存箱,其特征在于:还包括离子分离箱,离子分离箱由NdFeB永磁磁极对、装有反渗透膜的过滤管和有过滤管安插孔的底座组成;NdFeB永磁磁极对相对安装在离子分离箱的侧壁上,装有反渗透膜的过滤管固定于底座过滤管安插孔上,其上端装有反渗透膜部分插入磁场空间的下端;进水储水箱与离子分离箱相接,淡化水储存箱与离子分离箱相接。The magnetic ion sieve seawater desalination device includes an inlet water storage tank and a desalinated water storage tank, and is characterized in that it also includes an ion separation box. The base of the installation hole is composed of; the NdFeB permanent magnet pole pair is relatively installed on the side wall of the ion separation box, the filter tube equipped with the reverse osmosis membrane is fixed on the installation hole of the filter tube of the base, and the upper end of the reverse osmosis membrane is partially inserted The lower end of the magnetic field space; the water inlet storage tank is connected with the ion separation box, and the desalinated water storage tank is connected with the ion separation box.
进水储水箱由进水管、水箱和进水过滤板组成,进水过滤板上有均匀密布口径很小的小孔,能对不溶性杂质进行了一次过滤,以免杂质进入装置中污染反渗透膜;水箱是一个由PVC板焊接而成,其上接进水管,其下通过进水过滤板与离子分离箱相连,水箱的主要作用就是储存待处理水,并使待处理水在进入离子分离箱前处于一个相对稳定的状态而避免在离子分离箱中引起湍流。The water inlet storage tank is composed of the water inlet pipe, the water tank and the water inlet filter plate. The water inlet filter plate has evenly distributed small holes with small diameters, which can filter the insoluble impurities once, so as to prevent impurities from entering the device and contaminating the reverse osmosis membrane; The water tank is welded by PVC board, the upper part is connected to the water inlet pipe, and the lower part is connected to the ion separation box through the water inlet filter plate. The main function of the water tank is to store the water to be treated, and make the water to be treated In a relatively stable state to avoid turbulent flow in the ion separation chamber.
离子分离箱,是一个由PVC板焊接而成的长方体水箱,其四侧面的上端与进水储水箱四侧面下端焊接相连,而其顶部通过进水过滤板与进水储水箱底部相连,其下部的底座直接焊接在淡化水储存箱上。The ion separation box is a cuboid water tank welded by PVC board. The upper end of its four sides is welded and connected with the lower end of the four sides of the water inlet storage tank, and its top is connected with the bottom of the water inlet storage tank through the water inlet filter plate. The base is directly welded on the desalinated water storage tank.
为便于安装永磁磁极对,特设计一安装夹,安装夹是一个侧壁用PVC板焊接而成的长方体,其内部尺寸与永磁磁极的尺寸完全一致,其内部焊接一软磁材料板,安装夹直接焊接与离子分离箱侧壁中,永磁磁极在其后再装入安装夹中。在软磁材料板前是夹于两PVC板之间的空白空间,其目的是为了减少磁场的发散。In order to facilitate the installation of permanent magnet pole pairs, a mounting clip is specially designed. The mounting clip is a cuboid whose side wall is welded with PVC plates. Its internal dimensions are exactly the same as those of permanent magnetic poles. A soft magnetic material plate is welded inside. The mounting clip is directly welded to the side wall of the ion separation box, and the permanent magnet poles are then loaded into the mounting clip. Before the soft magnetic material board is a blank space sandwiched between two PVC boards, the purpose of which is to reduce the divergence of the magnetic field.
装有反渗透膜的过滤管在本装置中起了非常重要的作用:1.它将磁场空间中的含离子浓度低的海水引出,而实现磁场空间内外的海水实现分离;2.由于过滤管的入水口处装有反渗透膜,可以让水分子透过膜进入过滤管中流出,离子则不能透过反渗透膜而仍留在离子分离箱中,从而最终实现海水淡化。The filter tube equipped with reverse osmosis membrane plays a very important role in this device: 1. It leads out the seawater with low ion concentration in the magnetic field space, and realizes the separation of seawater inside and outside the magnetic field space; 2. Because the filter tube The reverse osmosis membrane is installed at the water inlet of the water tank, which allows water molecules to pass through the membrane and enter the filter tube to flow out, while ions cannot pass through the reverse osmosis membrane and remain in the ion separation box, thereby finally realizing seawater desalination.
在过滤管中间插入底座的部分的外侧要紧密套上与底座中的螺栓相应的螺丝环。螺丝环上端还要装上防渗水的密封圈,而长度比底座厚度长20cm-30cm,这主要是为了方便安装和更换反渗透膜及过滤管。过滤管通过螺栓固定于底座上,其上端装有反渗透膜部分插入磁场空间的下端,而其下端应从底座出来后还有较长一段,并在其下端装上一个出水开关。The outside of the part inserted into the base in the middle of the filter tube should be tightly fitted with a screw ring corresponding to the bolt in the base. The upper end of the screw ring should also be equipped with an anti-seepage sealing ring, and the length is 20cm-30cm longer than the thickness of the base. This is mainly for the convenience of installing and replacing the reverse osmosis membrane and filter tube. The filter tube is fixed on the base by bolts, and its upper end is equipped with a reverse osmosis membrane part inserted into the lower end of the magnetic field space, and its lower end should have a longer section after coming out of the base, and a water outlet switch is installed at its lower end.
为方便更换反渗透膜,特制造一膜套,膜套内径比过滤管稍大一点,其上表面安装和固定一块渗透膜,下端装有密封圈,膜套直接套在过滤管的上端。反渗透膜的选择醋酸纤维素膜(简称CA膜)膜的表层的孔隙大小在(10--20)×10-10M,膜厚100--250μm。In order to facilitate the replacement of the reverse osmosis membrane, a membrane sleeve is specially manufactured. The inner diameter of the membrane sleeve is slightly larger than that of the filter tube. A permeable membrane is installed and fixed on the upper surface, and a sealing ring is installed at the lower end. The membrane sleeve is directly placed on the upper end of the filter tube. The choice of reverse osmosis membrane The pore size of the surface layer of the cellulose acetate membrane (abbreviated as CA membrane) is (10-20)×10-10M, and the membrane thickness is 100-250μm.
离子分离箱底座上有过滤管安插孔,底座的底部为三角锥型,中间高,两侧底,这主要是为了利用重力的作用以及水的压力使高离子浓度的浓缩水和杂质向两侧的排放口处集中而提出。There is a filter tube insertion hole on the base of the ion separation box. The bottom of the base is triangular cone-shaped, high in the middle, and bottom on both sides. The side discharge port is centered and raised.
淡化水储存箱由淡化水出水管、水箱和支架组成,淡化水储存箱用PVC板焊接而成,其上端四侧壁与离子分离箱底座下端四侧壁焊接,从过滤管中出来的淡化水直接流入此箱内储存并通过淡化水出水管排出。在淡化水储存箱的下端四个角上和中部焊接上金属支架,其下端用螺栓固定在地面上,金属支架的作用就是稳固支撑整个装置并使装置处于竖直状态。The desalinated water storage tank is composed of a desalinated water outlet pipe, a water tank and a bracket. The desalinated water storage tank is welded with PVC boards. The four side walls at the upper end are welded with the four side walls at the lower end of the base of the ion separation box. The desalinated water coming out of the filter tube It flows directly into this tank for storage and is discharged through the desalinated water outlet pipe. On the four corners of the lower end of the desalinated water storage tank and the middle part, a metal support is welded, and its lower end is fixed on the ground with bolts. The effect of the metal support is exactly to firmly support the whole device and make the device in a vertical state.
待处理海水通过进水管1进入到水箱2中,然后在重力的作用下向下流动,通过进水过滤板3进入离子分离箱4。离子分离箱中有由NdFeB永磁磁极对5、6构成的磁场空间和其外的非磁场空间。在磁场空间中,由于海水中的离子如Na+,Cl-,Mg2+,Ca2+等作分子热运动,受到磁场的洛伦兹的作用而使相对更多的离子从磁场空间中逸出而进入非磁场空间中,从而使磁场空间中的海水的离子浓度降低,而非磁场空间中的海水的离子浓度升高。同时,水合水分子在磁场空间中作分子热运动,水分子之间的氢键将会受到破坏,而是水分子更多地以游离水分子形式存在,从而更容易与过滤管8上端的反渗透膜缔合。磁场空间中的水分子与反渗透膜缔合,在重力作用制造的水压差推动下,以及膜的下端的水分子的拉动下,透过反渗透膜。水分子透过反渗透膜后,在重力作用下和水分子本身与过滤管壁的浸润作用下,迅速离开反渗透膜而沿过滤圆柱管壁向下流动,并反过来对膜中的水分子产生拉力。由于只有水分子能透过反渗透膜,而离子无法通过反渗透膜,因此从过滤管中流出的水已经是淡化水。淡化水从过滤管中流出后就进入到淡化水储存箱10中,并最终从淡化水出水管11中排出。Seawater to be treated enters the
由于离子无法透过反渗透膜,被留在离子分离箱中,而使离子分离箱中的海水离子浓度不断升高,如不及时处理将影响海水淡化的影响并可能污染反渗透膜。由于磁场作用,非磁场空间的海水的离子浓度高于磁场空间中海水的离子浓度。由于待处理水由离子分离箱的最上端流入并向下流动,同时由于重力的作用,使处于离子分离箱最低处的浓缩水排放口9附近的海水离子浓度相对最高。通过对单位时间的淡化水产量,待处理水离子浓度,要求水的收率的综合计算,每隔一定时间打开浓缩水排放口将其附近的高浓缩海水排出一定量,从而使离子分离箱中的海水的离子浓度大大降低,再关闭浓缩水排放口,如此反复。Because the ions cannot pass through the reverse osmosis membrane, they are left in the ion separation box, and the concentration of seawater ions in the ion separation box continues to rise. If it is not treated in time, it will affect the impact of seawater desalination and may pollute the reverse osmosis membrane. Due to the effect of the magnetic field, the ion concentration of seawater in the non-magnetic field space is higher than that in the magnetic field space. Since the water to be treated flows in from the uppermost end of the ion separation box and flows downward, and at the same time due to the effect of gravity, the seawater ion concentration near the concentrated
本装置与现有技术的对比具有如下优点:Compared with the prior art, this device has the following advantages:
1.本装置运行能耗很低。本装置创造性地将分子运动的动能作为主要的离子分离的动力,只是借助水压差来驱动水分子透过反渗透膜而消耗了一些能量,所利用的外部能源就是这很小的水的势能差,大大低于反渗透中制造克服渗透压的外加高压力所耗费的能源;更大大低于EDI和EDR中所消耗的电能和动力能源;尤其远远低于蒸发和结晶所需的巨大能源;1. The energy consumption of this device is very low. This device creatively uses the kinetic energy of molecular motion as the main driving force for ion separation. It only uses the water pressure difference to drive water molecules through the reverse osmosis membrane and consumes some energy. The external energy used is the small potential energy of water. Poor, much lower than the energy consumed in reverse osmosis to create an additional high pressure to overcome the osmotic pressure; much lower than the electrical energy and power energy consumed in EDI and EDR; especially far lower than the huge energy required for evaporation and crystallization ;
2.本装置易于维护。由于本装置采用的水压较低,从而避免了因制造高压对装置密封性能和制造工艺提出的高要求;2. The device is easy to maintain. Due to the low water pressure used in this device, high requirements on the sealing performance and manufacturing process of the device due to high pressure are avoided;
3.淡化水质量较高。本装置中不但有反渗透膜的分离效能,利用强磁场对离子的分离作用进行了有效的补充,尤其是强磁场对于反渗透膜不易分离的小离子反而分离作用较好,使得水的淡化效果比一般反渗透好,又不象EDR、EDI虽淡化水质量高但必须借助反渗透进行预处理;3. The quality of desalinated water is high. This device not only has the separation efficiency of the reverse osmosis membrane, but also effectively supplements the separation effect of ions by using a strong magnetic field. In particular, the strong magnetic field has a better separation effect on small ions that are not easily separated by the reverse osmosis membrane, making the water desalination effect It is better than ordinary reverse osmosis, and unlike EDR and EDI, although the quality of desalinated water is high, it must be pretreated by reverse osmosis;
4.水的收率较高。本装置采用了几个方面的作用使浓缩水的浓度提高:a.通过磁场的作用,使离子更多地留在非磁场空间内;b.反渗透膜的充分的选择性使离子只可能留在离子分离箱内而从浓缩水排放口排出;c.本装置采用立式作业,且底部有沿中央向两侧浓缩水排放口倾斜的斜坡,则能充分利用重力的作用是离子和杂质在浓缩水排放口处富集,从而该处的离子和杂质浓度最高;d.本装置中水从上向下流,可有效的遏制离子从离子分离箱底部向上的扩散;e.可延长浓缩水排放口相对关闭时间而使浓缩水浓度升高。浓缩水浓度的升高,即意味着在总进水和淡化水质量不变时,排放的浓缩水总量减少,而淡化水产量升高,即水的收率提高了。4. The yield of water is higher. This device uses several functions to increase the concentration of concentrated water: a. Through the action of a magnetic field, more ions are left in the non-magnetic space; b. The sufficient selectivity of the reverse osmosis membrane makes it possible for ions to stay only In the ion separation box, it is discharged from the concentrated water discharge port; c. This device adopts vertical operation, and the bottom has a slope inclined from the center to the concentrated water discharge port on both sides, so that the effect of gravity can be fully utilized to keep the ions and impurities in Concentrated water is enriched at the discharge port, so that the concentration of ions and impurities is the highest; d. The water in this device flows from top to bottom, which can effectively prevent the diffusion of ions from the bottom of the ion separation box; e. It can extend the discharge of concentrated water The concentration of concentrated water increases relative to the closing time of the port. The increase of concentrated water concentration means that when the quality of total influent water and desalinated water remains unchanged, the total amount of concentrated water discharged decreases, while the output of desalinated water increases, that is, the water yield increases.
5.水的预处理费用降低。由于本装置采用立体式分离方式,使得离子和杂质在重力作用下更易在离子分离箱的底部沉积、浓缩,并从浓缩水排放口排出,因此预处理不需特别严格;b、由于强磁场本身具有相当的杀菌效用,可不用先对进水进行杀菌处理;c、由于对反渗透膜的使用已化整为零,使得反渗透膜相对不易被污染和损坏;5. The cost of water pretreatment is reduced. Since the device adopts a three-dimensional separation method, ions and impurities are easier to deposit and concentrate at the bottom of the ion separation box under the action of gravity, and are discharged from the concentrated water discharge port, so the pretreatment does not need to be particularly strict; b, due to the strong magnetic field itself It has a considerable bactericidal effect, and it is not necessary to sterilize the influent water first; c. Since the use of the reverse osmosis membrane has been broken down into pieces, the reverse osmosis membrane is relatively difficult to be polluted and damaged;
6.本装置中不需要电能和电极,从而极大缓解了电化学反应所产生的腐蚀作用。6. The device does not require electric energy and electrodes, thereby greatly alleviating the corrosion effect caused by the electrochemical reaction.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99240579U CN2401538Y (en) | 1999-10-22 | 1999-10-22 | Magnetic ion sieve sea water desalination device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99240579U CN2401538Y (en) | 1999-10-22 | 1999-10-22 | Magnetic ion sieve sea water desalination device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2401538Y true CN2401538Y (en) | 2000-10-18 |
Family
ID=34027598
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN99240579U Expired - Fee Related CN2401538Y (en) | 1999-10-22 | 1999-10-22 | Magnetic ion sieve sea water desalination device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2401538Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1303003C (en) * | 2004-10-28 | 2007-03-07 | 王建中 | Pretreating method for reversing asmose seawater desalinating pulsing electromagnetic field |
-
1999
- 1999-10-22 CN CN99240579U patent/CN2401538Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1303003C (en) * | 2004-10-28 | 2007-03-07 | 王建中 | Pretreating method for reversing asmose seawater desalinating pulsing electromagnetic field |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100581640C (en) | Electro-deionization method and device for synchronously concentrating and purifying heavy metal wastewater | |
| US9193612B2 (en) | Concentric layer electric double layer capacitor cylinder, system, and method of use | |
| CN207478339U (en) | A kind of energy-saving electrical electrodialysis apparatus | |
| CN104709980A (en) | Clamping-groove multistage series-capacitor deionizer | |
| CN112159902A (en) | A co-production system for lithium extraction with electric water based on capacitive method | |
| CN201099635Y (en) | capacitive desalter | |
| CN106676572B (en) | The extracting method and device of black liquid rugose wood element based on woodceramics electrode | |
| CN111320243A (en) | Membrane-free electrodeionization method and device with current perpendicular to water flow direction | |
| CN101293181A (en) | Metal base-metallic oxide separation film and preparation method thereof | |
| CN103482728A (en) | Desalination technology for utilizing microbial fuel cell to drive capacitive deionization | |
| CN210065421U (en) | Water treatment system | |
| CN106396211A (en) | Electrocoagulation and ceramic micro-filtration membrane coupling device for purifying micro-polluted source water as well as process | |
| CN2401538Y (en) | Magnetic ion sieve sea water desalination device | |
| CN117069195A (en) | Electric field enhanced fluorine removal device and fluorine removal method for fluorine-containing wastewater | |
| CN107244720A (en) | The device of electro-adsorption demineralization and salinity | |
| CN102115292B (en) | Sewage/waste water treating system | |
| CN219098939U (en) | Low-energy-consumption wastewater treatment device | |
| CN105906000A (en) | High-efficiency detachable multistage electric-adsorption water treatment module | |
| CN212174544U (en) | A membraneless electrodeionization device with current perpendicular to the direction of water flow | |
| CN204550236U (en) | A micro-waste water purifier | |
| CN206970371U (en) | A kind of casing processes sewage-treatment plant | |
| CN203866079U (en) | Nano titanium carburization electrode CDI (capacitive deionization) device | |
| CN201704110U (en) | Sewage treatment system with matching of magnetic activation and membrane bioreactor | |
| CN206308183U (en) | The coupling device of electric flocculation ceramic micro filter film purifying slightly polluted water source water | |
| CN207659238U (en) | A kind of film electricity combination water treatment facilities |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |