CN201864606U - Reverse osmosis water purifier without waste water - Google Patents
Reverse osmosis water purifier without waste water Download PDFInfo
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- CN201864606U CN201864606U CN201020572490XU CN201020572490U CN201864606U CN 201864606 U CN201864606 U CN 201864606U CN 201020572490X U CN201020572490X U CN 201020572490XU CN 201020572490 U CN201020572490 U CN 201020572490U CN 201864606 U CN201864606 U CN 201864606U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 359
- 238000001223 reverse osmosis Methods 0.000 title claims abstract description 66
- 239000002351 wastewater Substances 0.000 title abstract description 30
- 238000004146 energy storage Methods 0.000 claims abstract description 40
- 239000012528 membrane Substances 0.000 claims abstract description 39
- 239000002699 waste material Substances 0.000 claims description 14
- 230000004888 barrier function Effects 0.000 claims 1
- 238000004064 recycling Methods 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 description 21
- 238000011010 flushing procedure Methods 0.000 description 16
- 238000000034 method Methods 0.000 description 13
- 238000010586 diagram Methods 0.000 description 6
- 239000012535 impurity Substances 0.000 description 4
- 239000003651 drinking water Substances 0.000 description 3
- 239000008399 tap water Substances 0.000 description 3
- 235000020679 tap water Nutrition 0.000 description 3
- 235000012206 bottled water Nutrition 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000002203 pretreatment Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
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Abstract
本实用新型公开了一种无废水反渗透净水器,包括在进水管路中串联设置的预处理器和深处理器,经预处理器处理过的水流入深处理器,其中深处理器为一密闭容器,通过反渗透膜分隔为纯水区和浓水区,纯水从纯水出口流出,还包括用于收集深处理器运行时产生的浓水的储能罐,储能罐的出水口通过排水管路联接到与净水器进水口直通的水管上,且储能罐的出水口通过回流管路与深处理器的进水管路相连通。本实用新型通过设置对排出的浓水的收集、循环利用装置同时避免专设反渗透膜的冲洗程序,达到节约用水并延长预处理器滤芯工作寿命的目的。
The utility model discloses a reverse osmosis water purifier without waste water, which comprises a preprocessor and a deep processor arranged in series in the water inlet pipeline, and the water treated by the preprocessor flows into the deep processor, wherein the deep processor is A closed container, divided into pure water area and concentrated water area by reverse osmosis membrane, pure water flows out from the pure water outlet, and also includes an energy storage tank for collecting concentrated water generated during the operation of the deep processor, the outlet of the energy storage tank The water outlet is connected to the water pipe directly connected to the water inlet of the water purifier through the drainage pipeline, and the water outlet of the energy storage tank is connected with the water inlet pipeline of the deep processor through the return pipeline. The utility model achieves the purpose of saving water and prolonging the working life of the filter core of the preprocessor by setting the device for collecting and recycling the discharged concentrated water and avoiding the flushing program of the specially designed reverse osmosis membrane.
Description
技术领域technical field
本实用新型涉及一种净水器,特别涉及一种日用无废水反渗透净水器。The utility model relates to a water purifier, in particular to a reverse osmosis water purifier for daily use without waste water.
背景技术Background technique
如图1所示,目前现有技术中日用的反渗透净水器包括预处理系统和深处理系统,预处理系统由数个装有滤芯的预处理器2’组成,预处理器之间通过管路逐个串联,其中首预处理器的进水口通过给水管1’与源水相连;深处理系统由包含反渗透膜的深处理器构成,深处理器为密闭的容器,反渗透膜将深处理器分割为纯水区5’和浓水区6’,纯水区连接有用于取纯水的出水管7’,浓水区设有进水口和出水口;末预处理器的出水口通过管路与深处理器浓水区进水口相连接,管路中串接有为深处理器进水加压的增压泵4’。As shown in Figure 1, the daily reverse osmosis water purifier in the prior art comprises a pretreatment system and a deep treatment system, and the pretreatment system is made up of several preprocessors 2' that filter elements are housed, between the preprocessors The water inlet of the first preprocessor is connected to the source water through the pipeline 1'; the deep treatment system is composed of a deep processor containing a reverse osmosis membrane, which is a closed container, and the reverse osmosis membrane will The deep processor is divided into a pure water area 5' and a concentrated water area 6'. The pure water area is connected with an outlet pipe 7' for taking pure water. The concentrated water area is equipped with a water inlet and a water outlet; It is connected with the water inlet of the concentrated water area of the deep processor through a pipeline, and a booster pump 4' for pressurizing the water inlet of the deep processor is connected in series in the pipeline.
深处理器浓水区的出水口连接着用于控制浓水区压力的废水比(即节流装置)8’,废水比8’一方面保持深处理器浓水区的压力,以保证水流穿过反渗透膜有足够的水流动力,另一方面排出一定的浓水以便于增压泵4’补充足量的新水,补充的水不仅可以使浓水区的水的杂质浓度不会太高,且可在反渗透膜的浓水一侧形成较大的切向流速,较大的切向流速既能降低水中的杂质在膜表面沉积的趋势,又能对附着在反渗透膜上的杂质(例如离子、颗粒物、有机物等)进行冲洗,此可在一定程度上延长反渗透膜的使用寿命。The outlet of the concentrated water area of the deep processor is connected to the waste water ratio (throttle device) 8' used to control the pressure of the concentrated water area. The waste water ratio 8' maintains the pressure of the concentrated water area of the deep processor on the one hand to ensure that the water flow The reverse osmosis membrane has sufficient water flow power, and on the other hand, a certain amount of concentrated water is discharged so that the booster pump 4' can replenish a sufficient amount of new water. The replenished water can not only keep the impurity concentration of the water in the concentrated water area from being too high, And it can form a larger tangential flow velocity on the concentrated water side of the reverse osmosis membrane. The larger tangential flow velocity can not only reduce the tendency of impurities in the water to deposit on the membrane surface, but also reduce the impurities attached to the reverse osmosis membrane ( Such as ions, particulate matter, organic matter, etc.), which can prolong the service life of the reverse osmosis membrane to a certain extent.
在增压泵4’的前端进水管路中,设进水电磁阀3’,当制水结束、增压泵停机后,来自给水管1’的源水在水压作用下会经过增压泵流向排水管造成水资源浪费,制水结束后关闭该进水电磁阀,可避免这种不必要的浪费。In the water inlet pipeline at the front end of the booster pump 4', a water inlet solenoid valve 3' is set. When the water production is completed and the booster pump stops, the source water from the water supply pipe 1' will pass through the booster pump under the action of water pressure. Flowing to the drain pipe causes waste of water resources, and closing the water inlet solenoid valve after the water production is completed can avoid this unnecessary waste.
深处理器浓水区的出水口还连接有与废水比并联的旁路水管,旁路水管中的水受冲洗电磁阀9’的控制,用于将专门冲洗反渗透膜的水排出。冲洗电磁阀9’开启时,增压泵4’和进水电磁阀3’均开启,这时流经反渗透膜浓水一侧的切向流速非常大,冲洗过程中的浓水都通过冲洗电磁阀9’的控制排空。The water outlet of the concentrated water area of the deep processor is also connected with a bypass water pipe in parallel with the waste water ratio, and the water in the bypass water pipe is controlled by the flushing solenoid valve 9', which is used to discharge the water specially flushing the reverse osmosis membrane. When the flushing solenoid valve 9' is turned on, both the booster pump 4' and the water inlet solenoid valve 3' are turned on. At this time, the tangential flow velocity on the concentrated water side of the reverse osmosis membrane is very large, and the concentrated water in the flushing process passes through the flushing process. Controlled evacuation by solenoid valve 9'.
上述现有技术中的反渗透净水器结构的缺点在于,经废水比排出的浓水已经过预处理系统过滤,虽其杂质含量与纯水相比相差较大,但其水质仍高于或相当于普通自来水(主要是矿物质浓度比自来水高),此处则只能以废水的形式排掉而造成巨大的浪费。通常情况下每制成1立方米纯水就要排掉3立方米的浓水;另外此结构还需要独立的反渗透膜冲洗程序,冲洗过程所使用的水通过冲洗电磁阀控制也会作为废水排掉,在浪费水源的同时也加大了预处理器的工作负荷,影响预处理器中滤芯的工作寿命。The disadvantage of the reverse osmosis water purifier structure in the above-mentioned prior art is that the concentrated water discharged through the waste water ratio has been filtered by the pretreatment system. Although its impurity content is quite different from that of pure water, its water quality is still higher than or It is equivalent to ordinary tap water (mainly because the concentration of minerals is higher than that of tap water), and here it can only be discharged in the form of waste water, causing huge waste. Normally, 3 cubic meters of concentrated water will be drained for every cubic meter of pure water produced; in addition, this structure also requires an independent reverse osmosis membrane flushing program, and the water used in the flushing process will also be used as waste water through the flushing solenoid valve control Draining, while wasting water, also increased the workload of the preprocessor, affecting the working life of the filter element in the preprocessor.
实用新型内容Utility model content
本实用新型是为了克服上述现有技术中缺陷,通过设置对排出的浓水的收集、循环利用装置同时避免专设反渗透膜的冲洗程序,达到节约用水并延长预处理器滤芯工作寿命的目的。The utility model aims at overcoming the defects in the above-mentioned prior art, by setting up a collection and recycling device for the discharged concentrated water and avoiding the flushing program of the specially designed reverse osmosis membrane, so as to save water and prolong the working life of the preprocessor filter element .
本实用新型的无废水反渗透净水器,包括在进水管路中串联设置的预处理器和深处理器,经预处理器处理过的水流入深处理器,其中深处理器为一密闭容器,通过反渗透膜分隔为纯水区和浓水区,纯水从纯水出口流出,还包括用于收集深处理器运行时产生的浓水的储能罐,储能罐的出水口通过排水管路联接到与净水器进水口直通的水管上,且储能罐的出水口通过回流管路与深处理器的进水管路相连通。通过增加储能罐以及排水管路、回流管路可实现浓水的收集和循环利用,可节约用水并有效延长预处理器滤芯的工作寿命。The non-wastewater reverse osmosis water purifier of the utility model includes a preprocessor and a deep processor arranged in series in the water inlet pipeline, and the water treated by the preprocessor flows into the deep processor, wherein the deep processor is a closed container , divided into pure water area and concentrated water area by reverse osmosis membrane, pure water flows out from the pure water outlet, and also includes an energy storage tank for collecting concentrated water generated during the operation of the deep processor, and the water outlet of the energy storage tank is drained The pipeline is connected to the water pipe directly connected to the water inlet of the water purifier, and the water outlet of the energy storage tank is connected to the water inlet pipeline of the deep processor through the return pipeline. The collection and recycling of concentrated water can be realized by adding energy storage tanks, drainage pipelines and return pipelines, which can save water and effectively prolong the working life of preprocessor filter elements.
其中,储能罐中设有水腔和气腔,气腔与水腔之间设有隔膜,气腔中储存的气体被流入水腔中的浓水压缩而储存能量,优选地,所述储能罐分别设有相互独立的进水口和出水口。通过储能罐中的压力作用可使收集的浓水顺利进入排水管路或回流管路。Wherein, the energy storage tank is provided with a water chamber and an air chamber, and a diaphragm is provided between the air chamber and the water chamber. The gas stored in the air chamber is compressed by the concentrated water flowing into the water chamber to store energy. Preferably, the energy storage The tanks are respectively provided with mutually independent water inlets and water outlets. Through the pressure in the energy storage tank, the collected concentrated water can smoothly enter the drainage pipeline or the return pipeline.
所述储能罐的出水口通过排水管路联接到与净水器进水口直通的水管上,其包括两种情况:其一,储能罐的出水口通过排水管路联接到与净水器进水口直通的净水器进水管上,这时,净水器与水源管之间只有一根水管联接,该水管既是净水器的进水管也是净水器的浓水排水管,适用于水源管位置与净水器位置相对较近场合;其二,储能罐的出水口通过排水管路联接到与净水器进水口直通的水源管上,这时,净水器与水源管之间有两根水管联接,一根是净水器的进水管,另一根是净水器的浓水排水管,适用于水源管位置与净水器位置相对较远场合。The water outlet of the energy storage tank is connected to the water pipe directly connected to the water inlet of the water purifier through a drainage pipeline, which includes two situations: one, the water outlet of the energy storage tank is connected to the water pipe connected to the water purifier through a drainage pipeline. The water inlet is directly connected to the water inlet pipe of the water purifier. At this time, there is only one water pipe connected between the water purifier and the water source pipe. This water pipe is both the water inlet pipe of the water purifier and the concentrated water drain pipe of the water purifier. The position of the water pipe is relatively close to the position of the water purifier; secondly, the water outlet of the energy storage tank is connected to the water source pipe directly connected to the water inlet of the water purifier through the drainage pipeline. At this time, the water purifier and the water source pipe There are two water pipes connected, one is the water inlet pipe of the water purifier, and the other is the concentrated water drain pipe of the water purifier, which is suitable for the occasion where the water source pipe is relatively far from the water purifier.
优选地,可在排水管路上设第一电控阀。该第一电控阀用于控制制水过程和排水过程之间的切换,其中制水过程包括储能罐内压力从低压状态逐渐升到高压状态这一预制水过程和储能罐内压力处于高压状态的正式制水过程,预制水过程实际上就是对反渗透膜的冲洗过程。Preferably, a first electric control valve can be arranged on the drainage pipeline. The first electric control valve is used to control the switching between the water production process and the drainage process, wherein the water production process includes the process of prefabricating water in which the pressure in the energy storage tank gradually rises from a low pressure state to a high pressure state, and the pressure in the energy storage tank is at The official water production process under high pressure, the prefabricated water process is actually the flushing process of the reverse osmosis membrane.
所述电控阀是指可采用电力控制启闭的阀门,例如电磁阀、电动阀等。The electric control valve refers to a valve that can be opened and closed by electric control, such as a solenoid valve, an electric valve, and the like.
优选地,当源水管中的水压较低、不足以克服反渗透膜的阻力时,在深处理器的进水管路上可设置第一增压泵;在回流管路上设置节流装置,节流装置出口端与第一增压泵的进口管路相连通。优选采用废水比这种节流装置。Preferably, when the water pressure in the source water pipe is low enough to overcome the resistance of the reverse osmosis membrane, a first booster pump can be set on the water inlet pipeline of the deep processor; a throttling device is set on the return pipeline to throttle The outlet port of the device communicates with the inlet pipeline of the first booster pump. It is preferred to use waste water than this throttling device.
优选地,当源水管中的水压较低、不足以克服反渗透膜的阻力时,在深处理器的进水管路上设置第一增压泵;在回流管路上设置第二增压泵,第二增压泵的出口管路与第一增压泵的出口管路相连通。使用第二增压泵可进一步提升流经反渗透膜浓水一侧的切向水流量,并可使流量更加稳定。Preferably, when the water pressure in the source water pipe is low enough to overcome the resistance of the reverse osmosis membrane, a first booster pump is set on the water inlet pipeline of the deep processor; a second booster pump is set on the return pipeline, and the second booster pump is The outlet pipeline of the second booster pump communicates with the outlet pipeline of the first booster pump. The use of the second booster pump can further increase the tangential flow of water flowing through the concentrated water side of the reverse osmosis membrane, and can make the flow more stable.
优选地,当源水管中的水压较高、能够克服反渗透膜的阻力时,在回流管路上设置第二增压泵(此方案由于源水管水压较高而无需在进水管路中使用第一增压泵)。Preferably, when the water pressure in the source water pipe is high enough to overcome the resistance of the reverse osmosis membrane, a second booster pump is arranged on the return line (this solution does not need to be used in the water inlet line due to the high water pressure of the source water pipe) first booster pump).
优选地,当源水管中的水压较高、能够克服反渗透膜的阻力时,在回流管路上设置第二增压泵;在所述进水管路上、进水管路与源水管的接口处设置压力检测装置。所述压力检测装置可以是压力开关,也可以是压力传感器。所述压力开关是一种通过水压控制的电气开关。压力检测装置的作用是:当其检测到管路中压力较低时,净水器的控制系统将开启排水管路上的第一电控阀,使储能罐中的浓缩水经排水管路排向源水管。Preferably, when the water pressure in the source water pipe is high enough to overcome the resistance of the reverse osmosis membrane, a second booster pump is provided on the return pipeline; Pressure detection device. The pressure detecting device may be a pressure switch or a pressure sensor. The pressure switch is an electrical switch controlled by water pressure. The function of the pressure detection device is: when it detects that the pressure in the pipeline is low, the control system of the water purifier will open the first electric control valve on the drainage pipeline, so that the concentrated water in the energy storage tank will be discharged through the drainage pipeline. To the source water pipe.
优选地,排水管路上可设置第一单向阀。该第一单向阀可使从储能罐的出水口中流出浓水沿排水管路单向流动。Preferably, a first one-way valve can be set on the drain pipeline. The first one-way valve can make the concentrated water flowing out from the water outlet of the energy storage tank flow in one direction along the drainage pipeline.
优选地,进水管路上可设置第二单向阀。该第二单向阀可使源水沿进水管路单向流动。Preferably, a second one-way valve can be arranged on the water inlet pipeline. The second one-way valve can make the source water flow in one direction along the water inlet pipeline.
优选地,在深处理器的纯水出水管路上或者在深处理器的进水管路上设置在净水器不制水时能够防止深处理器内浓水区压力持续大于纯水区压力的第二电控阀,以便防止反渗透膜出现“死过滤”而影响反渗透膜的使用寿命。Preferably, on the pure water outlet pipeline of the deep processor or on the water inlet pipeline of the deep processor, when the water purifier does not produce water, the second water tank that can prevent the pressure of the concentrated water area in the deep processor from continuing to be greater than the pressure of the pure water area is set. Electronically controlled valves to prevent "dead filtration" of the reverse osmosis membrane and affect the service life of the reverse osmosis membrane.
当净水器需要制水时,使排水管路上的第一电控阀处于关闭状态,水源水经预处理器进行预处理后流入深处理器,从深处理器的纯水出口流出的水就是纯水,从深处理器的浓水出口流出的浓水流入储能罐的水腔,从储能罐的水腔流出的浓水经回流管流回深处理器的进水管路,制水过程就这样进行;当净水器需要冲洗反渗透膜时或制水过程结束时,开启排水管路上的第一电控阀,使储能罐中的浓缩水流向水源管路,在水源管路上其它用水器具(例如水龙头)开启时,该浓缩水流向用水器具,于是浓缩水得到利用,避免直接排放造成浪费。When the water purifier needs to produce water, the first electric control valve on the drainage pipeline is closed. The source water is pretreated by the preprocessor and then flows into the deep processor. The water flowing out of the pure water outlet of the deep processor is Pure water, the concentrated water flowing out from the concentrated water outlet of the deep processor flows into the water cavity of the energy storage tank, and the concentrated water flowing out of the water cavity of the energy storage tank flows back to the water inlet pipeline of the deep processor through the return pipe, the water production process Just like this; when the water purifier needs to flush the reverse osmosis membrane or when the water production process is over, open the first electric control valve on the drainage pipeline, so that the concentrated water in the energy storage tank flows to the water source pipeline, and the other on the water source pipeline When the water appliance (such as a faucet) is turned on, the concentrated water flows to the water appliance, so that the concentrated water can be utilized, avoiding waste caused by direct discharge.
对于设有第一增压泵的实施例,反渗透膜的冲洗还可以通过开启第一增压泵和第一电控阀来实现。For the embodiment provided with the first booster pump, the flushing of the reverse osmosis membrane can also be realized by turning on the first booster pump and the first electric control valve.
与现有技术相比,本实用新型具有如下有益效果:Compared with the prior art, the utility model has the following beneficial effects:
1、本实用新型的净水器不产生排放的废水,既节约了水资源,又避免了废水排放管的安装;1. The water purifier of the present utility model does not produce discharged waste water, which not only saves water resources, but also avoids the installation of waste water discharge pipes;
2、本实用新型的净水器无需现有技术中的单独的冲洗反渗透膜程序,而只需在每次制水开始时通过使流经反渗透膜表面水流较大的切向流速实现反渗透膜的冲洗;2. The water purifier of the present utility model does not need a separate flushing reverse osmosis membrane program in the prior art, but only needs to realize the reverse osmosis membrane by making the water flow through the reverse osmosis membrane surface larger tangential flow velocity at the beginning of each water production. flushing of permeable membranes;
3、可有效延长预处理滤芯的使用寿命。3. It can effectively prolong the service life of the pretreatment filter element.
附图说明Description of drawings
图1是现有技术中的反渗透膜净水器结构连接示意图;Fig. 1 is the structural connection schematic diagram of reverse osmosis membrane water purifier in the prior art;
图2是本实用新型无废水反渗透净水器实施例1结构连接示意图;Fig. 2 is the structural connection diagram of Example 1 of the utility model without waste water reverse osmosis water purifier;
图3是本实用新型无废水反渗透净水器实施例2结构连接示意图;Fig. 3 is the structural connection diagram of
图4是本实用新型无废水反渗透净水器实施例3结构连接示意图;Fig. 4 is the structural connection schematic diagram of
图5是本实用新型无废水反渗透净水器实施例4结构连接示意图;Fig. 5 is a structural connection schematic diagram of
图6是本实用新型无废水反渗透净水器实施例5结构连接示意图。Fig. 6 is a structural connection schematic diagram of
结合附图在其上标记以下附图标记:In conjunction with the accompanying drawings, the following reference numerals are marked thereon:
1’-给水管,2’-预处理器,3’-进水电磁阀,4’-增压泵,5’-纯水区,6’-浓水区,7’-净水出水管,8’-废水比,9’-冲洗电磁阀。1'-water supply pipe, 2'-preprocessor, 3'-inlet solenoid valve, 4'-booster pump, 5'-pure water area, 6'-concentrated water area, 7'-clean water outlet pipe, 8'-wastewater ratio, 9'-flushing solenoid valve.
1-给水管,2-预处理器,3-水龙头,4-第一增压泵,5-纯水区,6-浓水区,7-净水出水管,8-废水比,9-储能罐,10-储水腔,11-气腔,12-第一电控阀,13-第一单向阀,14-第二增压泵,15-压力开关,16-第二电控阀,17-第二单向阀。1-water supply pipe, 2-preprocessor, 3-faucet, 4-first booster pump, 5-pure water area, 6-concentrated water area, 7-clean water outlet pipe, 8-wastewater ratio, 9-storage Energy tank, 10-water storage chamber, 11-air chamber, 12-first electric control valve, 13-first one-way valve, 14-second booster pump, 15-pressure switch, 16-second electric control valve , 17-the second one-way valve.
具体实施方式Detailed ways
下面结合附图,对本实用新型的几个具体实施方式进行详细描述,但应当理解本实用新型的保护范围并不受具体实施方式的限制。Several specific embodiments of the present utility model will be described in detail below in conjunction with the accompanying drawings, but it should be understood that the protection scope of the present utility model is not limited by the specific embodiments.
实施例1Example 1
如图2所示,实施例1的无废水反渗透净水器的各部件可以按照下述方式连接:As shown in Figure 2, the parts of the reverse osmosis water purifier without waste water of
在源水管(内有自来水)上连接一根给水管1,给水管1依次串联连接预处理器2、低压开关、第一增压泵4和深处理器,形成进水水路,低压开关可防止水泵无水空转损坏水泵。其中预处理器2由彼此串联连接的三个预处理滤芯组成。深处理器内设反渗透膜组件,反渗透膜将深处理器分割为纯水区5和浓水区6,纯水区5与纯水出水管连通,用于获得纯水。浓水区6的进口与第一增压泵4的出口相连,浓水区6的出口与储能罐9的水腔相连通,储能罐9用于收集、储存从深处理器中排出的浓水,储能罐设有水腔10和气腔11,气腔与水腔之间设有隔膜以便防止气体溶解到水中随水流排出而减少气腔中的气体储量。另外,水腔10通过连接管路依次与第一电控阀12、第一单向阀13串联,最终连接到给水管1上,形成排水管路,第一单向阀13可防止源水反向直接流入储能罐9,上述气腔中储存的气压可为储能罐9的水腔10中的浓水流向给水管1提供能量,在水腔10的出水口与第一电控阀12之间的管路上引出一根回流管至第一增压泵4进口管路上,在该回流管上设废水比8(节流装置的一种)。A
实施例1的工作过程如下:The working process of
第一电控阀12可以为常开电控阀,在源水管中有水时,低压开关在水压作用下处于闭合状态,如果此时启动制水系统制水,则接通第一增压泵4的电源电路和第一电控阀12的电路,于是,第一增压泵4通电启动,第一电控阀12关闭;来自源水管中的水经三个预处理滤芯(即预处理器)预处理再经第一增压泵的增压后,进入反渗透滤芯(即深处理器)进行深度处理;从反渗透滤芯出水口(即纯水区5出口)流出的水即为纯水;从反渗透滤芯浓水排放口(即浓水区6出口)排出的水流入储能罐9的水腔10,再经废水比8减压后流回第一增压泵4的进水口,从而得到再次循环利用。The first
制水完毕时,第一增压泵4和第一电控阀12断电,即增压泵停止运行同时第一电控阀12开启,此时,储能罐水腔10中的浓水经第一电控阀12和第一单向阀13流入给水管1进而流入源水管(一般情况下,此时储能罐内压力高于源水压力),使用者在源水管的上游或下游开启水龙头时,浓水将随之排出供非饮用水使用。When the water production is completed, the
到下一个制水周期开始时,由于储能罐水腔10中的水很少或没有,第一增压泵启动和第一电控阀关闭后,从浓水区6出口排出的浓水的流量会很大,但此时浓水区的水压较小,将使得流经反渗透膜浓水一侧的切向流动的水流量很大出现高强度冲洗的效果(此时过滤量较小),以便有效冲刷膜表面可能沉积的堵塞物。随着冲洗过程的进行,储能罐水腔10中的水压会逐渐上升,流经反渗透膜浓水一侧的切向水流量会逐渐下降,流速逐渐减小,储能罐水腔10中的水或浓水区6出口排出的水通过废水比减压后回流到第一增压泵进水口的流量会逐渐加大,浓水区的压力逐渐上升,当该流量上升到正常值后反渗透滤芯开始正常滤水。At the beginning of the next water production cycle, since there is little or no water in the
当然,第一电控阀12也可以为常闭电控阀,如果使用常闭电控阀,在制水-冲洗-再制水的过程中其开启的控制需要进行相应的调整,在此不再详述。Of course, the first
储能罐9的最大储水量可小于4L,考虑到可以经常将储能罐中的浓水排出,浓水的浓度不会太高,因此容积可小一些以降低制造成本,优选小于2L。The maximum water storage capacity of the energy storage tank 9 can be less than 4L. Considering that the concentrated water in the energy storage tank can be discharged frequently, the concentration of the concentrated water will not be too high, so the volume can be smaller to reduce the manufacturing cost, preferably less than 2L.
相对于现有技术,实施例1的储能罐的使用实现了浓水的循环利用,没有产生排放的废水,既节约了水资源,又避免了废水排放管的安装;由于浓水的循环使用,系统可不需要单独的冲洗反渗透膜程序,而只需在下一次制水开始时通过使流经反渗透膜表面水流较大的切向流速实现反渗透膜的冲洗;现有技术中的净水器在制水时只有四分之一的水得到利用,而有四分之三的水作为废水排放到系统外,但这四分之三的排放水仍需要进行预处理滤芯的处理,因此预处理滤芯的利用率较低,严重影响了其使用寿命。而实施例1的回流管路的设计可有效分担上述四分之三的进水流量,因此可有效延长预处理滤芯的使用寿命。Compared with the prior art, the use of the energy storage tank in Example 1 realizes the recycling of concentrated water without producing discharged waste water, which not only saves water resources, but also avoids the installation of waste water discharge pipes; due to the recycling of concentrated water , the system does not need a separate program for flushing the reverse osmosis membrane, but only needs to realize the flushing of the reverse osmosis membrane at the beginning of the next water production by making the water flowing through the surface of the reverse osmosis membrane at a relatively large tangential flow rate; Only 1/4 of the water is used when the device produces water, and 3/4 of the water is discharged out of the system as waste water, but this 3/4 of the discharged water still needs to be treated by the pre-treatment filter element, so the pre-treatment The utilization rate of the processing filter element is low, which seriously affects its service life. However, the design of the return pipeline in
实施例2Example 2
如图3所示,实施例2的无废水反渗透净水器的各部件的连接关系与实施例1类似,不同的是将废水比8替换为第二增压泵14,且连接位置有所不同,即第二增压泵14的进口连接在储能罐水腔10的出水口上,其出口连接在第一增压泵4出口管路上。相比于实施例1,使用第二增压泵14可进一步提升流经反渗透膜浓水一侧的切向水流量,且流量更加稳定。As shown in Figure 3, the connection relationship of each part of the non-wastewater reverse osmosis water purifier of
需要特别说明的是,上述实施例1、2均在进水管路上使用了第一增压泵4,这是针对源水压力(即自来水压力)较低,不足以克服反渗透膜的阻力的情况下设计的。而当源水压力较大时,则无需使用该第一增压泵4,具体实施例请参见下述实施例3、4。It should be noted that the
实施例3Example 3
如图4所示,与实施例2不同的是,在给水管处、预处理器前端串联一个压力开关15和第二电控阀16,取消实施例2中进水管路上设置的低压开关和第一增压泵4。As shown in Figure 4, the difference from
在本实施例3中,当需要制水时,在高水压作用下,压力开关15处于关闭(或开启)状态,控制系统根据压力开关信号和需要制水信号分别开启第二增压泵14、开启第二电控阀16和关闭第一电控阀12,源水依次穿过第二电控阀16和预处理器进入深处理器的反渗透滤芯,纯水从纯水区出口流出,浓水进入储能罐,再经回流管路上的第二增压泵增压后回流至反渗透滤芯的进水口,系统进入制水状态;当系统检测到制水量符合要求时(例如可以在纯水区出口处设置高压开关,当该高压开关起跳后可认为制水量已符合要求),控制系统关闭第二电控阀16、关闭第二增压泵14和开启第一电控阀12,即设备停机;当需要使用源水使得管路中的水龙头开启时,压力开关15处的水压下降使得其断开(或闭合),控制系统根据该信号开启第二电控阀16,此时储能罐中的浓水在压力作用下流向源水管供非饮用水使用,直至关闭水龙头使压力开关15处的压力回升该压力开关重新闭合(或断开),此时控制系统根据该信号关闭第二电控阀16,使用者在下次使用水龙头时将重复出现上述流程(系统可设置累计第二电控阀16开启时间的功能,当累计的开启时间达到设定值时,说明储能罐中的浓水已基本排尽,然后控制系统中将储存的累计时间清零)。In
实施例4Example 4
如图5所示,与实施例3不同的是,将实施例3中的第二电控阀16移设于深处理器纯水区出口处;另外,在预处理器和深处理器之间的进水管路上设置能够防止水流逆向流过预处理器的第二单向阀17。As shown in Figure 5, different from
当需要制水时,压力开关15在高水压下处于关闭(或开启)状态,控制系统根据压力开关信号和需要制水信号开启第二增压泵14和第二电控阀16,同时关闭第一电控阀12,设备进入纯净水的制水状态;当制水量符合要求后,控制系统关闭第二电控阀16和第二增压泵14,同时开启第一电控阀12,此时储能罐中的浓水流向源水管上的水龙头(在该水龙头开启时)可供非饮用水使用。本实施例4的浓水排放只需打开水龙头放水,无需额外的控制元件。When water production is required, the
实施例5Example 5
如图6所示,还可以将回流管路接在预处理器前端的进水管路,即将废水比的出口接在预处理器的进口管路上;第一增压泵还可接在预处理器内串联的滤芯之间的管路中。当然在不脱离本实用新型原理的基础上还可以有其它的连接方式。As shown in Figure 6, the return line can also be connected to the water inlet line at the front end of the preprocessor, that is, the outlet of the waste water ratio is connected to the inlet line of the preprocessor; the first booster pump can also be connected to the preprocessor In the pipeline between the filter elements in series. Of course, other connection methods can also be arranged on the basis of not departing from the principle of the utility model.
以上公开的仅为本实用新型的几个具体实施例,但是,本实用新型并非局限于此,任何本领域的技术人员能思之的变化都应涵盖在本实用新型的权利要求范围中。The above disclosures are only a few specific embodiments of the utility model, but the utility model is not limited thereto, and any changes conceivable by those skilled in the art should be included in the scope of claims of the utility model.
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CN103908894A (en) * | 2013-01-08 | 2014-07-09 | 美的集团股份有限公司 | Water purifier and water production control method thereof |
CN103908894B (en) * | 2013-01-08 | 2016-08-24 | 美的集团股份有限公司 | Water purifier and water production control method thereof |
CN106565026A (en) * | 2015-10-10 | 2017-04-19 | 杜也兵 | Switching water production method for double-pump water purifier with discharged concentrated water recovery device |
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CN105502577A (en) * | 2015-12-01 | 2016-04-20 | 中国电子系统工程第二建设有限公司 | Reverse osmosis device |
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