CN103803736B - Strong-pulse micro-wastewater emission and purification system - Google Patents
Strong-pulse micro-wastewater emission and purification system Download PDFInfo
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Abstract
本发明公开了一种强脉冲微废水排放净水系统,包括:依次通过管道连接的进水三通(1)、前置过滤器组、增压泵(13)、反渗透膜过滤器(15)、后置活性炭过滤器(19),后置活性炭过滤器出口通过高压开关(18)与出水口(20)连接,反渗透膜过滤器的出口同时通过管道与一储水压力桶(4)连接,其中,所述的反渗透膜过滤器出口设有废水排放管道,该管道上设有一脉冲电磁阀(14);所述的储水压力桶通过一管道和单向阀(22)回流微量纯水至反渗透膜过滤器(15)的前端用于在制水完毕后,浸泡反渗透膜。本发明通过急速瞬时脉冲排污冲洗反渗透膜、纯水回流冲洗浸泡保护反渗透膜两项措施,使原水利用率大幅提高到75%以上。
The invention discloses a strong pulse micro-wastewater discharge water purification system, comprising: a water inlet tee (1), a pre-filter group, a booster pump (13), a reverse osmosis membrane filter (15) connected sequentially through pipelines ), a rear activated carbon filter (19), the outlet of the rear activated carbon filter is connected to the water outlet (20) through a high-pressure switch (18), and the outlet of the reverse osmosis membrane filter is connected to a water storage pressure tank (4) through a pipeline at the same time connection, wherein, the outlet of the reverse osmosis membrane filter is provided with a waste water discharge pipe, and a pulse solenoid valve (14) is provided on the pipe; The front end of the pure water to the reverse osmosis membrane filter (15) is used for soaking the reverse osmosis membrane after water production is completed. In the present invention, the utilization rate of raw water is greatly increased to more than 75% through the two measures of fast instantaneous pulse blowdown flushing of the reverse osmosis membrane and pure water reflux flushing and immersion protection of the reverse osmosis membrane.
Description
技术领域 technical field
本发明涉及净水机,尤其涉及一种强脉冲微废水排放净水系统。 The invention relates to a water purifier, in particular to a strong pulse micro-wastewater discharge water purification system.
背景技术 Background technique
我国大多数城市以Ⅲ类地表水、农村地区主要以Ⅳ类地下水为饮用水源,随着污染的加剧,两虫(贾第鞭毛虫、隐孢子虫)、蓝绿藻、重金属超标等问题,严重威胁着城乡饮用水安全。因此,地表水、地下水必须经过净化才能作为饮用水使用。现在家用、商用饮用水处理技术核心主要是膜过滤技术。其中一种是超滤膜过滤,过滤孔径为0.01微米,可以去除全部的浑浊物(如泥沙、铁锈等),致病微生物(如寄生虫、细菌、病毒等),也能去除大部分的大分子有机物,同时不需用电,不产生废水,比较适合中国南方水质比较好的城市,但因无法去除水中的有机化合物、放射性氡、砷等多种有害或致癌物质以及铅、汞等重金属离子,在水质比较差的北方地区以及广大的农村,就无法满足安全健康的饮用水处理需求。另一种是反渗透膜过滤,过滤滤孔径为0.0001微米,可以完全去除水中的所有有害物质,只保留水分子产出纯水,适用性广,在中国广大城乡地区是水处理的主力。但是用反渗透膜的纯水机因为反渗透膜的工作原理,在产纯水的过程中需要排放大量的废水(浓缩水),受水温、水质的影响,产出一份纯水需要排放掉3-5份废水。这种产出惊人废水的现状是与国内倡导的科学发展和建设节约型社会的“节能、降耗”要求是相背离的。 Most cities in my country use Class III surface water, and rural areas mainly use Class IV groundwater as their drinking water source. With the intensification of pollution, problems such as two insects (Giardia flagella, Cryptosporidium), blue-green algae, and heavy metals exceeding the standard, etc., Serious threat to urban and rural drinking water safety. Therefore, surface water and groundwater must be purified before they can be used as drinking water. At present, the core of domestic and commercial drinking water treatment technology is mainly membrane filtration technology. One of them is ultrafiltration membrane filtration, with a filter pore size of 0.01 microns, which can remove all turbid substances (such as sediment, rust, etc.), pathogenic microorganisms (such as parasites, bacteria, viruses, etc.), and can also remove most of the Macromolecular organic matter does not require electricity and does not produce waste water. It is more suitable for cities with better water quality in southern China, but it cannot remove organic compounds, radioactive radon, arsenic and other harmful or carcinogenic substances in water, as well as heavy metals such as lead and mercury. Ions, in the northern regions and vast rural areas where the water quality is relatively poor, cannot meet the needs of safe and healthy drinking water treatment. The other is reverse osmosis membrane filtration, with a filter pore size of 0.0001 micron, which can completely remove all harmful substances in water, and only retain water molecules to produce pure water. It has wide applicability and is the main force of water treatment in China's vast urban and rural areas. However, due to the working principle of the reverse osmosis membrane, the pure water machine with reverse osmosis membrane needs to discharge a large amount of waste water (concentrated water) in the process of producing pure water. Affected by water temperature and water quality, a piece of pure water needs to be discharged. 3-5 parts of waste water. The current situation of producing astonishing waste water deviates from the domestically advocated scientific development and the "energy saving and consumption reduction" requirements of building a conservation-oriented society.
尽管国内很多人把传统纯水机排放的废水进行二次回用,但这种回收的水质和回收的方式始终不能尽如人意。近两年也有部分净水器厂家推出“少废水”纯水机,原理是将制水过程排放的废水流回到反渗透膜前端循环使用,使反渗透膜长期在高浓度废水环境下运行,降低了纯水产出的质量同时也加快了反渗透膜的污堵速度,使反渗透膜的使用寿命大为缩短。实践使我们认识到:“省水”的普通超滤机因为使用局限性使它很难覆盖中国复杂水质的各个地区,而“费水”的RO纯水机更不适宜在“缺水”的中国大面积推广。因此,必须进行“节水技术”创新和产品创新。 Although many people in China reuse the wastewater discharged from traditional water purifiers for a second time, the water quality and recycling methods of this recycling are still not satisfactory. In the past two years, some water purifier manufacturers have also launched "less waste water" pure water machines. The principle is to return the waste water discharged from the water production process to the front end of the reverse osmosis membrane for recycling, so that the reverse osmosis membrane can operate in a high-concentration waste water environment for a long time. The quality of the pure water output is reduced, and the fouling speed of the reverse osmosis membrane is also accelerated, so that the service life of the reverse osmosis membrane is greatly shortened. Practice has made us realize that the "water-saving" ordinary ultrafiltration machine is difficult to cover various areas of China with complex water quality due to its use limitations, and the "water-consuming" RO pure water machine is even less suitable for "water-scarce" areas. Widespread promotion in China. Therefore, "water-saving technology" innovation and product innovation must be carried out.
发明内容 Contents of the invention
本发明的目的是针对上述现有技术存在的缺陷,提供一种强脉冲微废水排放净水系统。 The purpose of the present invention is to provide a strong pulse micro-wastewater discharge water purification system aiming at the defects in the above-mentioned prior art.
本发明设计的强脉冲微废水排放净水系统包括:依次通过管道连接的进水三通、前置过滤器组、增压泵、反渗透膜过滤器和后置活性炭过滤器,所述的后置活性炭过滤器出口通过高压开关与出水口连接,进口通过管道与一储水压力桶连接,其中,所述的反渗透膜过滤器出口设有废水排放管道,该管道上设有一脉冲电磁阀;所述的储水压力桶通过一管道和单向阀回流微量纯水至反渗透膜过滤器的前端用于在制水完毕后,浸泡反渗透膜。 The strong pulse micro-wastewater discharge water purification system designed by the present invention includes: a water inlet tee, a pre-filter group, a booster pump, a reverse osmosis membrane filter and a post-installed activated carbon filter connected by pipelines sequentially. The outlet of the active carbon filter is connected to the water outlet through a high-pressure switch, and the inlet is connected to a water storage pressure barrel through a pipeline, wherein the outlet of the reverse osmosis membrane filter is provided with a waste water discharge pipeline, and the pipeline is provided with a pulse solenoid valve; The water storage pressure barrel returns a small amount of pure water to the front end of the reverse osmosis membrane filter through a pipeline and a one-way valve for soaking the reverse osmosis membrane after the water production is completed.
所述的前置过滤器组包括依次连接的PPF滤芯过滤器、活性炭滤芯过滤器和PPF滤芯过滤器。 The pre-filter group includes a PPF filter element filter, an activated carbon filter element filter and a PPF filter element filter connected in sequence.
在一实施例中,所述的高压开关前端设置一个单向阀。所述的反渗透膜过滤器和后置活性炭过虑器之间设有一水流传感器。所述的增压泵和反渗透膜过滤器之间设有一四面阀。所述的PPF过滤器和活性炭过滤器之间设有一进水电磁阀。 In one embodiment, a check valve is provided at the front end of the high pressure switch. A water flow sensor is arranged between the reverse osmosis membrane filter and the post activated carbon filter. A four-way valve is arranged between the booster pump and the reverse osmosis membrane filter. A water inlet electromagnetic valve is arranged between the PPF filter and the active carbon filter.
与现有技术相比,本发明具有以下有益效果: Compared with the prior art, the present invention has the following beneficial effects:
1、本发明通过急速瞬时脉冲排污冲洗反渗透膜、纯水回流冲洗浸泡保护反渗透膜两项措施,在保证纯水高质量产出同时又不损伤反渗透膜的情况下,使纯水机的废水与纯水的比率可由普通纯水机的废水3:纯水1大幅提高到废水1:纯水3以上(根据水质不同可以做到废水1:纯水6以上),原水利用率从不到25%的大幅提高到75%以上。 1. The present invention adopts the two measures of rapid and instantaneous pulse blowdown flushing of the reverse osmosis membrane and pure water reflux flushing and soaking protection of the reverse osmosis membrane to ensure the high-quality output of pure water without damaging the reverse osmosis membrane. The ratio of waste water to pure water can be greatly increased from waste water 3: pure water 1 of ordinary pure water machines to waste water 1: pure water 3 or more (according to different water quality, waste water 1: pure water 6 or more can be achieved), and the utilization rate of raw water has never been higher. From 25% to over 75%.
2、本发明通过采用不耗电的双稳态脉冲电磁阀以及大流量反渗透膜,在自来水水压高于0.2兆帕的城乡地区,可以不用市政电源、不用增压泵,实现纯水机无电条件下微废水排放产出纯水,在保障水质安全的情况下,更加做到节能减排,符合我国建设节约型社会的要求。 2. The present invention adopts a bistable pulse solenoid valve that does not consume electricity and a large-flow reverse osmosis membrane. In urban and rural areas where the water pressure of tap water is higher than 0.2 MPa, the pure water machine can be realized without municipal power supply or booster pump. Under the condition of no electricity, the discharge of micro-wastewater produces pure water. Under the condition of ensuring the safety of water quality, it can achieve energy saving and emission reduction, which meets the requirements of building a conservation-oriented society in my country.
附图说明 Description of drawings
图1是普通纯水机制水流程图; Fig. 1 is the water flowchart of common pure water mechanism;
图2是部分废水回流纯水机的制水流程图; Fig. 2 is the flow chart of water production of part of the waste water backflow pure water machine;
图3是本发明一实施例的系统示意图; Fig. 3 is a system schematic diagram of an embodiment of the present invention;
图4是本发明第二实施例的系统示意图。 Fig. 4 is a schematic diagram of the system of the second embodiment of the present invention.
具体实施方式 Detailed ways
下面结合附图和实施例对本发明进行详细的说明。 The present invention will be described in detail below in conjunction with the accompanying drawings and embodiments.
反渗透膜(RO膜)净水技术的过滤精度高达0.0001微米,几乎能滤除水以外的一切杂质和盐。但高精度RO膜的负面效应是其极易被污堵,为防止RO膜被污堵,保证RO膜产水过程中膜的通畅性,RO纯水机的RO膜在生产纯水的同时必须保证足量的原水冲洗RO膜表面,所以会产生大量的废水。美国著名的陶氏公司生产的RO膜原水利用率推荐值为15%。在国内,纯水机厂家使用较多的韩国“世韩膜”、日本“东丽膜”以及国产“汇通膜”等,推荐的原水利用率也在25%左右。 The filtration accuracy of reverse osmosis membrane (RO membrane) water purification technology is as high as 0.0001 micron, which can filter out almost all impurities and salts except water. However, the negative effect of the high-precision RO membrane is that it is extremely easy to be fouled. In order to prevent the RO membrane from being fouled and ensure the smoothness of the membrane during the water production process of the RO membrane, the RO membrane of the RO pure water machine must be produced while producing pure water. Ensure sufficient raw water to flush the surface of the RO membrane, so a large amount of waste water will be generated. The recommended value of the raw water utilization rate of the RO membrane produced by the famous American Dow Company is 15%. In China, pure water machine manufacturers use more Korean "Sehan membrane", Japan "Toray membrane" and domestic "Huitong membrane", etc., and the recommended raw water utilization rate is also about 25%.
图1显示现有技术中的净水系统,包括:依次通过管道连接的进水三通1、前置过滤器组(由依次连接的PPF滤芯过滤器8、活性炭滤芯过滤器10和PPF滤芯过滤器11组成)、增压泵13、反渗透膜过滤器15、高压开关18、后置活性炭过滤器19,后置活性炭过滤器出口与出水口20,例如龙头连接,高压开关18出口同时通过管道与一储水压力桶4连接。 Fig. 1 shows the water purification system in the prior art, comprising: water inlet tee 1, pre-filter group (by successively connected PPF cartridge filter 8, active carbon filter cartridge filter 10 and PPF cartridge filter connected by pipeline) device 11), booster pump 13, reverse osmosis membrane filter 15, high pressure switch 18, rear activated carbon filter 19, the outlet of the rear activated carbon filter is connected to the water outlet 20, such as a faucet connection, and the outlet of the high pressure switch 18 passes through the pipeline at the same time Connect with a water storage pressure barrel 4.
如图1所示,普通纯水机的制水流程是加压后的水经过反渗透膜过滤后由膜的中心管经过反渗透膜过滤器的纯水端流出,废水端保持不间断废水排放,由一个恒定流量的废水比例阀16来排出废水,在累积一段时间废水比排放后再加上废水电磁阀17排放,以保证清除膜上污垢的积淀。这种制水流程,原水利用率在25%左右。 As shown in Figure 1, the water production process of an ordinary pure water machine is that the pressurized water is filtered by the reverse osmosis membrane, and then flows out from the central tube of the membrane through the pure water end of the reverse osmosis membrane filter, and the waste water end maintains uninterrupted discharge of waste water , the waste water is discharged by a waste water proportional valve 16 with a constant flow rate, and the waste water solenoid valve 17 is discharged after accumulating a period of waste water ratio discharge to ensure the removal of dirt deposits on the membrane. In this water production process, the utilization rate of raw water is about 25%.
如图2所示,国内部分厂家的“少废水”纯水机制水流程是在普通纯水机的流程上增加了一个废水回流装置,将部分废水引入反渗透膜过滤器15的入口,去掉了恒定流量的废水比例阀16,用电磁阀17进行间断式排污,使排放的废水循环利用,减少了废水排放,原水利用率提高到50%甚至更高,但反渗透膜在越来越高的高浓度废水环境下不能保证纯水的产出质量,同时对反渗透膜的损伤很大,膜的污堵加重,使用寿命大大缩短。 As shown in Figure 2, the water process of the "less waste water" pure water mechanism of some domestic manufacturers adds a waste water backflow device to the process of ordinary pure water machines, and introduces part of the waste water into the inlet of the reverse osmosis membrane filter 15, removing the Constant flow of wastewater proportional valve 16, electromagnetic valve 17 is used for intermittent sewage discharge, so that the discharged wastewater can be recycled, reducing wastewater discharge, and the utilization rate of raw water is increased to 50% or even higher, but the reverse osmosis membrane is getting higher and higher In the environment of high-concentration wastewater, the output quality of pure water cannot be guaranteed, and at the same time, the damage to the reverse osmosis membrane is great, the fouling of the membrane is aggravated, and the service life is greatly shortened.
图3是本发明一实施例显示的净水系统,包括:依次通过管道连接的进水三通1、前置过滤器组、增压泵13、反渗透膜过滤器15、后置活性炭过滤器19,后置活性炭过滤器出口通过高压开关18与出水口20连接,反渗透膜过滤器的出口同时通过管道与一储水压力桶4连接。其中,反渗透膜过滤器出口设有废水排放管道,该管道上设有一脉冲电磁阀14;储水压力桶4通过一管道和单向阀22回流微量纯水至反渗透膜过滤器15的前端用于在制水完毕后,浸泡反渗透膜。 Fig. 3 is a water purification system shown in an embodiment of the present invention, comprising: a water inlet tee 1, a pre-filter group, a booster pump 13, a reverse osmosis membrane filter 15, and a rear activated carbon filter connected by pipelines in sequence 19. The outlet of the rear activated carbon filter is connected to the water outlet 20 through the high-pressure switch 18, and the outlet of the reverse osmosis membrane filter is connected to a water storage pressure tank 4 through a pipeline at the same time. Wherein, the outlet of the reverse osmosis membrane filter is provided with a waste water discharge pipeline, and the pipeline is provided with a pulse solenoid valve 14; the water storage pressure tank 4 passes through a pipeline and a check valve 22 to return trace pure water to the front end of the reverse osmosis membrane filter 15 It is used to soak the reverse osmosis membrane after the water production is completed.
如图3所示,本发明提出的制水流程去除了恒定流量的废水比例阀,将普通的废水电磁阀改用开启、闭合时间在0.1秒以内的脉冲电磁阀14,用间断式脉冲排污,通过电磁阀快速的开启闭合产生急速的水流瞬时冲洗反渗透膜表面,快速去除膜上积累的污垢沉淀,以极少的冲洗用水量达到有效清洗反渗透膜的目的,大幅减少了废水的产生。与普通纯水机相比,采用本发明系统的急速瞬时脉冲排污,废水与纯水的比率可由废水3:纯水1大幅提高到废水1:纯水3以上(根据水质不同可以做到废水1:纯水6以上),原水利用率从不到25%大幅提高到75%以上。 As shown in Figure 3, the water production process proposed by the present invention removes the waste water proportional valve with a constant flow rate, and replaces the ordinary waste water solenoid valve with a pulse solenoid valve 14 with an opening and closing time within 0.1 second, and uses intermittent pulse blowdown, The rapid opening and closing of the solenoid valve generates a rapid flow of water to instantly flush the surface of the reverse osmosis membrane, quickly remove the accumulated dirt and sediment on the membrane, and achieve the purpose of effectively cleaning the reverse osmosis membrane with a very small amount of flushing water, greatly reducing the generation of wastewater. Compared with ordinary pure water machines, the ratio of waste water to pure water can be greatly increased from waste water 3: pure water 1 to waste water 1: pure water 3 or more (according to different water quality, waste water 1 : pure water 6 or more), the utilization rate of raw water has been greatly increased from less than 25% to more than 75%.
其中,具体的冲洗操作时间如下:除去电磁阀开启、闭合时间,每次冲洗的时间在0.1秒至1秒之间(0.3秒-0.5秒为好)以产生急速强劲的水流,单次冲洗时间太短不能完全去除膜上的污垢沉淀,时间太长则不能产生强劲水流,浪费水而且冲洗效果不佳。每次冲洗间隔时间在15秒至45秒之间。此间隔时间可以作为调节纯水与废水的比例的工具,在水质较好的地区或者客户要求超低废水排放时,可以将间隔时间延长以达到省水的目的。根据连续运转产出纯水达10吨以上的测试,在原水TDS值500以内的地区,可以做到纯水5:废水1的效果而且反渗透膜没有出现出水流量明显减少的现象。在原水TDS值低于300以内的地区,可以做到纯水6:废水1的效果,甚至更高。这样,在中国水质较好的南方地区,可以更高的调高纯水产出,调低废水排放,在大面积使用的情况下节省大量宝贵的水源。 Among them, the specific flushing operation time is as follows: except for the opening and closing time of the solenoid valve, the time for each flushing is between 0.1 second and 1 second (0.3 second-0.5 second is better) to generate rapid and strong water flow, and the single flushing time If it is too short, the dirt deposits on the membrane cannot be completely removed, and if it is too long, it will not produce a strong water flow, wasting water and the flushing effect is not good. The interval between each flushing is between 15 seconds and 45 seconds. This interval time can be used as a tool to adjust the ratio of pure water to waste water. In areas with better water quality or when customers require ultra-low waste water discharge, the interval time can be extended to achieve the purpose of saving water. According to the test that the pure water produced by continuous operation reaches more than 10 tons, in the area where the raw water TDS value is less than 500, the effect of pure water 5: waste water 1 can be achieved, and the reverse osmosis membrane does not show a significant decrease in water flow. In areas where the TDS value of raw water is less than 300, the effect of pure water 6: waste water 1 can be achieved, or even higher. In this way, in the southern region of China where the water quality is better, the output of pure water can be increased more and the discharge of wastewater can be lowered, saving a lot of precious water resources in the case of large-scale use.
如图3所示,本发明增加了纯水回流装置,在外置式压力桶4或直饮机内置滤芯式压力桶出水处分出一条水管,通过单向阀22将纯水回流到反渗透膜过滤器15前端,在制水完毕后,将纯水输送到反渗透膜过滤器内浸泡反渗透膜。同时在高压开关18前端增加一个单向阀5,以防止在制水完毕后纯水回流时因高压开关失压造成增压泵频繁启动。增加此回流装置的原理是:在反渗透膜急速瞬时脉冲排污时,废水比率显著下降,但反渗透膜排污端累积的浓水较多,TDS值上升较大(特别是原水TDS值高的地区或者提升原水利用到75%以上时更加明显)。在制满水停止产水一段时间后,反渗透膜的静止渗透原理会使纯水端出水TDS值偏高,不利于高质量纯水的产出。通过此纯水回流装置,反渗透膜在制水结束后,经由洁净的纯水冲洗、浸泡,废水端的TDS值显著下降,大幅降低向纯水端渗透的可能,同时也保护了反渗透膜。与其他废水回流到反渗透膜前端达到省水目的的“少废水”纯水机相比,反渗透膜的使用寿命不但没有缩短反而得以延长,纯水高质量的产出也更加有保障。 As shown in Figure 3, the present invention adds a pure water backflow device, and a water pipe is separated from the outlet of the external pressure tank 4 or the built-in filter type pressure tank of the direct drinking machine, and the pure water is returned to the reverse osmosis membrane filter through the one-way valve 22 15 front end, after the water production is completed, the pure water is sent to the reverse osmosis membrane filter to soak the reverse osmosis membrane. At the same time, a check valve 5 is added at the front end of the high pressure switch 18 to prevent the booster pump from frequently starting due to the pressure loss of the high pressure switch when the pure water returns after the water production is completed. The principle of adding this reflux device is: when the reverse osmosis membrane is rapidly and instantaneously pulsed sewage, the waste water ratio drops significantly, but the concentrated water accumulated at the blowdown end of the reverse osmosis membrane is more, and the TDS value rises greatly (especially in areas with high raw water TDS value Or it will be more obvious when the utilization of raw water is increased to more than 75%). After the water production is stopped for a period of time, the static osmosis principle of the reverse osmosis membrane will cause the TDS value of the water at the pure water end to be high, which is not conducive to the output of high-quality pure water. Through this pure water reflux device, the reverse osmosis membrane is rinsed and soaked in clean pure water after the water production is completed, and the TDS value of the waste water end is significantly reduced, which greatly reduces the possibility of seepage to the pure water end, and at the same time protects the reverse osmosis membrane. Compared with other "less waste water" water purifiers that return wastewater to the front of the reverse osmosis membrane to save water, the service life of the reverse osmosis membrane is not shortened but extended, and the output of high-quality pure water is more guaranteed.
图4显示本发明的第二个实施例。该实施例中,可以在纯水出水端增加一个水流传感器7,同时在反渗透膜过滤器15进水前端增加一个四面阀6,用电脑板来控制水路系统,同时进水电磁阀和排污电磁阀都采用不耗电的脉冲电磁阀以及大流量反渗透膜,在自来水水压高于0.2兆帕的城乡地区,可以不用市政电源、不用增压泵,实现纯水机无电条件下微废水排放产出纯水,更加做到节能减排,符合我国建设节约型社会的要求。 Fig. 4 shows a second embodiment of the present invention. In this embodiment, a water flow sensor 7 can be added at the pure water outlet, and at the same time, a four-way valve 6 can be added at the front end of the reverse osmosis membrane filter 15, and a computer board can be used to control the water system. The valves use non-power-consuming pulse solenoid valves and large-flow reverse osmosis membranes. In urban and rural areas where the tap water pressure is higher than 0.2 MPa, municipal power supply and booster pumps can be used to realize micro-waste water under the condition of no electricity for pure water machines. The discharge produces pure water, which is more energy-saving and emission-reducing, which meets the requirements of my country's construction of a conservation-oriented society.
上述实施例仅用于说明本发明的具体实施方式。应当指出的是,对于本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和变化,这些变形和变化都应属于本发明的保护范围。 The above-mentioned embodiments are only used to illustrate specific implementation methods of the present invention. It should be noted that those skilled in the art can make several modifications and changes without departing from the concept of the present invention, and these modifications and changes should all belong to the protection scope of the present invention.
Claims (7)
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| CN201410078645.7A CN103803736B (en) | 2014-01-15 | 2014-03-05 | Strong-pulse micro-wastewater emission and purification system |
| PCT/CN2014/074159 WO2015131422A1 (en) | 2014-03-05 | 2014-03-27 | Intense pulsation micro wastewater discharge water purification system |
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| CN201410078645.7A CN103803736B (en) | 2014-01-15 | 2014-03-05 | Strong-pulse micro-wastewater emission and purification system |
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| CN203781935U (en) * | 2014-01-15 | 2014-08-20 | 深圳澳特弗科技有限公司 | Strong-pulse micro-wastewater discharge water purification system |
| CN104607050A (en) * | 2014-12-30 | 2015-05-13 | 广东艾沃科技有限公司 | Pulse flushing method of reverse osmosis membrane in water purifier |
| CN105152378A (en) * | 2015-09-14 | 2015-12-16 | 珠海格力电器股份有限公司 | Water purifier with pure water reflux device |
| CN106587264A (en) * | 2015-10-14 | 2017-04-26 | 乌日尼乐 | Pure water machine |
| CN105293638A (en) * | 2015-12-05 | 2016-02-03 | 中山市雅乐思净水科技有限公司 | A device and method for intelligently adjusting the ratio of purified water and concentrated water in a water purifier |
| CN107915282B (en) * | 2016-10-11 | 2019-12-10 | 青岛经济技术开发区海尔热水器有限公司 | A reverse osmosis water purifier |
| CN206616073U (en) * | 2017-01-23 | 2017-11-07 | 上海六滴环保科技有限公司 | A kind of Novel water purifier with pure water vacuolar membrane function when shutting down static |
| CN106830400A (en) * | 2017-01-23 | 2017-06-13 | 上海六滴环保科技有限公司 | A kind of water purifier with pure water vacuolar membrane function when shutting down static |
| CN106861441B (en) * | 2017-03-29 | 2020-02-21 | 海南立昇净水科技实业有限公司 | Method and device for cleaning water purification membrane module |
| CN107010744A (en) * | 2017-05-02 | 2017-08-04 | 浙江艾波特环保科技股份有限公司 | A kind of micro- waste water water purifier |
| CN106986492A (en) * | 2017-05-02 | 2017-07-28 | 浙江艾波特环保科技股份有限公司 | One kind prevents the elevated water purifier of TDS values |
| CN111302514B (en) * | 2018-12-11 | 2024-12-10 | 佛山市顺德区美的饮水机制造有限公司 | Waterway board and water purifier |
| CN110615505A (en) * | 2019-10-08 | 2019-12-27 | 浙江诺水科技发展有限公司 | Integrated water purifier |
| CN114515464B (en) * | 2020-11-17 | 2024-05-07 | 台湾积体电路制造股份有限公司 | Filtration system and method of cleaning a filtration device |
| CN114275849A (en) * | 2021-12-29 | 2022-04-05 | 佛山市美的清湖净水设备有限公司 | Water purifier with double TDS probes |
| CN114394647A (en) * | 2021-12-29 | 2022-04-26 | 佛山市美的清湖净水设备有限公司 | Water purifier |
| CN115646201A (en) * | 2022-09-29 | 2023-01-31 | 珠海格力智能装备有限公司 | A flushing device, water purifier and flushing method |
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| JPH11319827A (en) * | 1998-03-19 | 1999-11-24 | Daisen Membrane Systems Kk | Reverse osmosis membrane type water purifying device |
| CN2875574Y (en) * | 2006-02-17 | 2007-03-07 | 佳尼特(上海)纯水设备有限公司 | Intermittent drain water saving type reverse osmosis water purification device |
| CN100445212C (en) * | 2006-06-23 | 2008-12-24 | 深圳市英尼克电器有限公司 | A method for controlling the recycling of concentrated water in reverse osmosis water purification treatment |
| CN201923895U (en) * | 2010-12-13 | 2011-08-10 | 余泽嗣 | Water-saving RO (Reverse Osmosis) water purifier system |
| CN202148205U (en) * | 2011-05-09 | 2012-02-22 | 江苏正本净化节水科技实业有限公司 | Reverse-osmosis water purifier |
| CN203173901U (en) * | 2013-02-04 | 2013-09-04 | 深圳安吉尔饮水产业集团有限公司 | Water purifier and impulse type waste water discharge device thereof |
| CN103183419A (en) * | 2013-03-18 | 2013-07-03 | 艾欧史密斯(上海)水处理产品有限公司 | Reverse osmosis purification system |
| CN203781935U (en) * | 2014-01-15 | 2014-08-20 | 深圳澳特弗科技有限公司 | Strong-pulse micro-wastewater discharge water purification system |
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