CN204550236U - A micro-waste water purifier - Google Patents
A micro-waste water purifier Download PDFInfo
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- CN204550236U CN204550236U CN201520134821.4U CN201520134821U CN204550236U CN 204550236 U CN204550236 U CN 204550236U CN 201520134821 U CN201520134821 U CN 201520134821U CN 204550236 U CN204550236 U CN 204550236U
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- 239000002351 wastewater Substances 0.000 title claims abstract description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 239
- 239000012528 membrane Substances 0.000 claims abstract description 44
- 238000011045 prefiltration Methods 0.000 claims abstract description 13
- 230000007246 mechanism Effects 0.000 claims abstract description 11
- 238000003860 storage Methods 0.000 claims abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 31
- 239000002131 composite material Substances 0.000 claims description 31
- 238000011010 flushing procedure Methods 0.000 claims description 15
- 229920000742 Cotton Polymers 0.000 claims description 14
- 238000000746 purification Methods 0.000 claims description 10
- 239000011148 porous material Substances 0.000 claims description 9
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- 239000000741 silica gel Substances 0.000 claims description 7
- 229910002027 silica gel Inorganic materials 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 238000005192 partition Methods 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 5
- 238000001223 reverse osmosis Methods 0.000 abstract description 7
- 238000004140 cleaning Methods 0.000 description 17
- 238000004519 manufacturing process Methods 0.000 description 8
- 239000003814 drug Substances 0.000 description 7
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 230000004907 flux Effects 0.000 description 6
- 239000003651 drinking water Substances 0.000 description 5
- 235000020188 drinking water Nutrition 0.000 description 5
- 229940079593 drug Drugs 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
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- 238000000034 method Methods 0.000 description 2
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- 235000021419 vinegar Nutrition 0.000 description 2
- 239000000052 vinegar Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
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- Water Treatment By Sorption (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及净水机技术领域,具体涉及一种微废水净水机。 The utility model relates to the technical field of water purifiers, in particular to a micro-waste water purifier.
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。 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.
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。此外,在浪费水的同时也加大了预处理滤芯的工作负荷,即缩短了预处理滤芯的使用寿命。 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-minded society. In addition, while wasting water, the workload of the pretreatment filter element is also increased, that is, the service life of the pretreatment filter element is shortened.
发明内容 Contents of the invention
本实用新型的目的是针对现有技术中的上述不足,提供一种微废水净水机,该净水机能节约水资源,排出的废水量少,符合国家节能要求,且保证RO膜的使用寿命。 The purpose of this utility model is to provide a micro-waste water purifier for the above-mentioned deficiencies in the prior art. The water purifier can save water resources, discharge less waste water, meet the national energy-saving requirements, and ensure the service life of the RO membrane. .
本实用新型的目的通过以下技术方案实现。 The purpose of this utility model is achieved through the following technical solutions.
一种微废水净水机,包括通过管道依次连接的前置过滤器、进水电磁阀、水泵、滤芯机构和RO膜,所述净水机还包括有限流及循环电磁阀、限流阀、单向阀、高压开关、储水桶和后置过滤器, A micro-waste water purifier, comprising a pre-filter, a water inlet solenoid valve, a water pump, a filter element mechanism and an RO membrane connected sequentially through pipelines, the water purifier also includes a flow-limiting and circulation solenoid valve, a flow-limiting valve, One-way valve, high-pressure switch, water storage tank and post-filter,
所述前置过滤器与原水管线连接,所述RO膜的净水出口连接有净水出水管,所述单向阀和所述高压开关沿水流方向依次设置于所述净水出水管,所述净水出水管的出水端分别与所述储水桶和所述后置过滤器连接; The pre-filter is connected to the raw water pipeline, the water purification outlet of the RO membrane is connected to a water purification outlet pipe, and the one-way valve and the high-pressure switch are sequentially arranged on the water purification outlet pipe along the direction of water flow. The water outlet ends of the water purification outlet pipes are respectively connected with the water storage bucket and the post filter;
所述RO膜的浓水出口连接有浓水出水管,浓水出水管的出水端分别连接有回水管和排水管,所述限流及循环电磁阀设置于所述回水管,所述回水管的出水端与所述水泵的进水端连接,所述限流阀设置于所述排水管,所述排水管的出水口与下水管连接, The concentrated water outlet of the RO membrane is connected to a concentrated water outlet pipe, and the outlet ends of the concentrated water outlet pipe are respectively connected to a return pipe and a drain pipe. The current limiting and circulation solenoid valve is arranged on the return pipe, and the return pipe The water outlet end of the water pump is connected to the water inlet end of the water pump, the flow limiting valve is arranged on the drain pipe, and the water outlet of the drain pipe is connected to the downpipe,
所述净水机还包括有电控装置,所述进水电磁阀、所述高压开关、所述水泵和所述限流及循环电磁阀分别与所述电控装置电连接。 The water purifier also includes an electric control device, the water inlet solenoid valve, the high pressure switch, the water pump and the current limiting and circulation solenoid valve are respectively electrically connected to the electric control device.
其中,所述限流及循环电磁阀包括电磁阀体和与电磁阀体配合安装的阀座,电磁阀体和阀座之间设置有挡水板和密封垫,电磁阀体中部依次设置有弹簧、阀芯和硅胶粒,硅胶粒与挡水板抵接,密封垫与阀座嵌接,阀座内设有循环腔室,循环腔室与阀座的内壁之间设置有隔板,隔板的高度小于循环腔室的高度,阀座的两侧分别设置有进水管和出水管,进水管与阀座的内部连通,循环腔室开设有循环孔,出水管与循环孔连通,出水管还开设有限流孔,限流孔与阀座的内部连通。 Wherein, the current-limiting and circulating solenoid valve includes a solenoid valve body and a valve seat cooperating with the solenoid valve body, a water retaining plate and a gasket are arranged between the solenoid valve body and the valve seat, and springs are arranged in the middle of the solenoid valve body in sequence. , the valve core and the silica gel grains, the silica gel grains are in contact with the water retaining plate, the gasket is embedded with the valve seat, there is a circulation chamber in the valve seat, and a partition is arranged between the circulation chamber and the inner wall of the valve seat, and the partition board The height of the valve seat is less than the height of the circulation chamber. The two sides of the valve seat are respectively provided with an inlet pipe and an outlet pipe. The inlet pipe communicates with the inside of the valve seat. The circulation chamber is provided with a circulation hole. A flow-limiting hole is provided, and the flow-limiting hole communicates with the inside of the valve seat.
其中,所述挡水板开设有漏水孔,所述密封垫对应漏水孔的位置开设有通孔,通孔、漏水孔均与所述阀座的内腔连通。 Wherein, the water retaining plate is provided with a leakage hole, and the sealing pad is provided with a through hole at a position corresponding to the leakage hole, and the through hole and the leakage hole are both connected with the inner cavity of the valve seat.
其中,所述水泵作为循环泵使用时的单位时间的通量为2.0L/min。 Wherein, when the water pump is used as a circulating pump, the flux per unit time is 2.0 L/min.
所述浓水出水管的出水端还连接有冲洗管,冲洗管设置有冲洗电磁阀。 The outlet end of the concentrated water outlet pipe is also connected with a flushing pipe, and the flushing pipe is provided with a flushing solenoid valve.
其中,所述净水机还包括有用于清洗RO膜的清洗液,清洗液为食品级的柠檬酸或白醋。 Wherein, the water purifier also includes a cleaning solution for cleaning the RO membrane, and the cleaning solution is food-grade citric acid or white vinegar.
其中,所述滤芯机构包括依次串联连接的一级滤芯和二级滤芯,所述一级滤芯为活性炭滤芯,所述二级滤芯为pp棉滤芯。 Wherein, the filter element mechanism includes a primary filter element and a secondary filter element which are sequentially connected in series, the primary filter element is an activated carbon filter element, and the secondary filter element is a pp cotton filter element.
其中,所述滤芯机构包括并联连接的二级复合滤芯和三级复合滤芯,所述二级复合滤芯、所述三级复合滤芯的出水端分别与所述RO膜的进水端连接,所述前置过滤器为孔径20μm的折纸滤芯。 Wherein, the filter element mechanism includes a secondary composite filter element and a tertiary composite filter element connected in parallel, the water outlet ends of the secondary composite filter element and the tertiary composite filter element are respectively connected to the water inlet end of the RO membrane, and the The pre-filter is an origami filter element with a pore size of 20 μm.
其中,所述二级复合滤芯、所述三级复合滤芯均为活性炭和PP棉的复合滤芯,该复合滤芯的外层为孔径1-5μm的PP棉,PP棉内填充有烧结活性炭。 Wherein, the secondary composite filter element and the tertiary composite filter element are composite filter elements of activated carbon and PP cotton, the outer layer of the composite filter element is PP cotton with a pore size of 1-5 μm, and the PP cotton is filled with sintered activated carbon.
其中,所述后置过滤器为活性炭滤芯过滤器。 Wherein, the post-filter is an activated carbon filter element filter.
本实用新型的有益效果: The beneficial effects of the utility model :
本实用新型的微废水净水机,由电控装置控制,当水泵、限流及循环电磁阀打开时水机为循环状态,水泵此时作为循环泵使用,循环水流量为2升/分钟,其目的是利用大通量水流来冲洗RO膜,循环2分钟后,由电控装置控制,限流及循环电磁阀关闭水机为制水状态,水泵此时作为增压泵使用,利用限流及循环电磁阀的限流功能达到控制制水工作压力。实现在不提高TDS值的同时制得的纯水和排出的废水的比例为3:1,排出的废水量少,且纯水的TDS值低,大大节约水资源,符合国家节能要求,纯水质量高,且保证RO膜的使用寿命及纯水水质。 The micro-waste water purifier of the utility model is controlled by an electric control device. When the water pump, current limiting and circulation solenoid valve are opened, the water machine is in a circulating state, and the water pump is used as a circulating pump at this time, and the circulating water flow rate is 2 liters/minute. Its purpose is to flush the RO membrane with a large flow of water. After 2 minutes of circulation, the electric control device controls the current limiting and circulating solenoid valve to close the water machine and enter the water production state. The water pump is used as a booster pump at this time. And the current limiting function of the circulating solenoid valve can control the working pressure of water production. Realize that the ratio of pure water to discharged wastewater is 3:1 without increasing the TDS value, the amount of discharged wastewater is small, and the TDS value of pure water is low, which greatly saves water resources and meets the national energy-saving requirements. Pure water The quality is high, and the service life of the RO membrane and the quality of pure water are guaranteed.
本实用新型的净水机仅通过水泵和限流及循环电磁阀配合,只需利用一个水泵即可实现增压和循环两种功能,大大降低了材料和生产成本,且净水机的结构更简单,更便于组装及维修。 The water purifier of the utility model only cooperates with the water pump and the current limiting and circulation solenoid valve, and only needs to use one water pump to realize the two functions of pressurization and circulation, which greatly reduces the cost of materials and production, and the structure of the water purifier is more efficient. Simple, easier to assemble and maintain.
附图说明 Description of drawings
利用附图对实用新型作进一步说明,但附图中的实施例不构成对本实用新型的任何限制,对于本领域的普通技术人员,在不付出创造性劳动的前提下,还可以根据以下附图获得其它的附图。 Utilize accompanying drawing to further illustrate the utility model, but the embodiment in the accompanying drawing does not constitute any restriction to the present utility model, for those of ordinary skill in the art, under the premise of not paying creative work, also can obtain according to following accompanying drawing Additional drawings.
图1是本实用新型的实施例1的原理结构示意图。 Fig. 1 is a schematic diagram of the principle structure of Embodiment 1 of the present utility model.
图2是本实用新型的实施例2的原理结构示意图。 Fig. 2 is a schematic diagram of the principle structure of Embodiment 2 of the present utility model.
图3是本实用新型的限流及循环电磁阀的剖面结构示意图。 Fig. 3 is a schematic cross-sectional structure diagram of the current limiting and circulating solenoid valve of the present invention.
图4是本实用新型的限流及循环电磁阀的阀座的结构示意图。 Fig. 4 is a structural schematic diagram of the valve seat of the current limiting and circulating solenoid valve of the present invention.
附图标记包括: Reference signs include:
10——前置过滤器 20——进水电磁阀 30——水泵 10——Pre-filter 20——Inlet solenoid valve 30——Water pump
41——一级滤芯 42——二级滤芯 43——二级复合滤芯 41——Primary filter element 42——Secondary filter element 43——Secondary composite filter element
44——三级复合滤芯 50——RO膜 44——three-stage composite filter element 50——RO membrane
60——限流及循环电磁阀 70——限流阀 80——单向阀 60——Limiting and circulation solenoid valve 70——Limiting valve 80——One-way valve
90——高压开关 100——储水桶 110——后置过滤器 90——High pressure switch 100——Water storage tank 110——Post filter
120——纯水龙头 11——原水管线 12——净水出水管 120——pure water faucet 11——raw water pipeline 12——clean water outlet pipe
13——浓水出水管 14——回水管 15——排水管 13——Concentrated water outlet pipe 14——Return pipe 15——Drain pipe
16——冲洗管 161——冲洗电磁阀 130——电控装置 16——flushing pipe 161——flushing solenoid valve 130——electric control device
301——电磁阀体 302——阀座 301——Solenoid valve body 302——Valve seat
303——挡水板 304——密封垫 305——弹簧 303——Water flap 304——Sealing gasket 305——Spring
306——阀芯 307——硅胶粒 308——循环腔室 306——spool 307——silica gel 308——circulation chamber
309——隔板 310——进水管 311——出水管 309——Partition 310——Water inlet pipe 311——Water outlet pipe
312——循环孔 313——限流孔。 312——circulation hole 313——restriction hole.
具体实施方式 Detailed ways
结合以下实施例对本实用新型作进一步描述,见图1至图4。 The utility model is further described in conjunction with the following embodiments, see Fig. 1 to Fig. 4 .
实施例1Example 1
如图1所示,本实施例的一种微废水净水机,包括通过管道依次连接的前置过滤器10、进水电磁阀20、水泵30、滤芯机构和RO膜50,所述净水机还包括有限流及循环电磁阀60、限流阀70、单向阀80、高压开关90、储水桶100和后置过滤器110, As shown in Figure 1, a kind of micro-waste water purifier of the present embodiment comprises the pre-filter 10, water inlet solenoid valve 20, water pump 30, filter element mechanism and RO membrane 50 connected successively by pipelines, the water purifier The machine also includes a flow limiting and circulation solenoid valve 60, a flow limiting valve 70, a one-way valve 80, a high pressure switch 90, a water storage tank 100 and a post filter 110,
所述前置过滤器10与原水管线11连接,所述RO膜50的净水出口连接有净水出水管12,所述单向阀80和所述高压开关90沿水流方向依次设置于所述净水出水管12,所述净水出水管12的出水端分别与所述储水桶100和所述后置过滤器110连接; The pre-filter 10 is connected to the raw water pipeline 11, the water purification outlet of the RO membrane 50 is connected to the water purification outlet pipe 12, and the one-way valve 80 and the high-pressure switch 90 are sequentially arranged on the water flow direction. A clean water outlet pipe 12, the outlet ends of the clean water outlet pipe 12 are respectively connected to the water storage bucket 100 and the post filter 110;
所述RO膜50的浓水出口连接有浓水出水管13,浓水出水管13的出水端分别连接有回水管14和排水管15,所述限流及循环电磁阀60设置于所述回水管14,所述回水管14的出水端与所述水泵30的进水端连接,所述限流阀70设置于所述排水管15,所述排水管15的出水口与下水管连接。 The concentrated water outlet of the RO membrane 50 is connected with a concentrated water outlet pipe 13, and the outlet ends of the concentrated water outlet pipe 13 are respectively connected with a return pipe 14 and a drain pipe 15, and the flow limiting and circulation solenoid valve 60 is arranged in the return The water pipe 14, the water outlet end of the return pipe 14 is connected to the water inlet end of the water pump 30, the flow limiting valve 70 is arranged on the drain pipe 15, and the water outlet of the drain pipe 15 is connected to a downpipe.
本实用新型的微废水净水机,由电控装置130控制,当水泵30、限流及循环电磁阀60打开时水机为循环状态,水泵30此时作为循环泵使用,循环水流量为2升/分钟,其目的是利用大通量水流来冲洗RO膜,循环2分钟后,由电控装置130控制,限流及循环电磁阀60关闭水机为制水状态,水泵30此时作为增压泵使用,利用限流及循环电磁阀60的限流功能达到控制制水工作压力。实现在不提高TDS值的同时满足制得的纯水和排出的废水的比例为3:1,排出的废水量少,且纯水的TDS值低,大大节约水资源,符合国家节能要求,纯水质量高,且保证RO膜50的使用寿命。 The micro-waste water purifier of the present utility model is controlled by the electric control device 130. When the water pump 30, the current limiting and circulation solenoid valve 60 are opened, the water machine is in a circulating state, and the water pump 30 is used as a circulating pump at this time, and the circulating water flow rate is 2 The purpose is to flush the RO membrane with a large flow of water. After 2 minutes of circulation, it is controlled by the electric control device 130. The current limiting and circulation solenoid valve 60 closes the water machine and is in the water production state. The water pump 30 is now used as an increasing The pressure pump is used, and the current limiting function of the current limiting and circulating solenoid valve 60 is used to control the working pressure of water production. Realize that the ratio of the produced pure water to the discharged wastewater is 3:1 without increasing the TDS value, the amount of discharged wastewater is small, and the TDS value of pure water is low, which greatly saves water resources and meets the national energy-saving requirements. The water quality is high, and the service life of the RO membrane 50 is guaranteed.
如图3和图4所示,本实施例的限流及循环电磁阀包括电磁阀体301和与电磁阀体301配合安装的阀座302,电磁阀体301和阀座302之间设置有挡水板303和密封垫304,电磁阀体301中部依次设置有弹簧305、阀芯306和硅胶粒307,硅胶粒307与挡水板303抵接,密封垫304与阀座302嵌接,阀座302内设有循环腔室308,循环腔室308与阀座302的内壁之间设置有隔板309,隔板309的高度小于循环腔室308的高度,阀座302的两侧分别设置有进水管310和出水管311,进水管310与阀座302的内部连通,循环腔室308开设有循环孔312,出水管311与循环孔312连通,出水管311还开设有限流孔313,限流孔313与阀座302的内部连通。 As shown in Figures 3 and 4, the current limiting and circulating solenoid valve of this embodiment includes a solenoid valve body 301 and a valve seat 302 cooperating with the solenoid valve body 301, and a stopper is arranged between the solenoid valve body 301 and the valve seat 302. The water plate 303 and the sealing gasket 304, the middle part of the solenoid valve body 301 are provided with a spring 305, a valve core 306 and silica gel particles 307 in sequence, the silica gel particles 307 abut against the water retaining plate 303, the sealing gasket 304 is embedded with the valve seat 302, and the valve seat 302 is provided with a circulation chamber 308, and a partition 309 is arranged between the circulation chamber 308 and the inner wall of the valve seat 302. The water pipe 310 and the water outlet pipe 311, the water inlet pipe 310 communicates with the inside of the valve seat 302, the circulation chamber 308 is provided with a circulation hole 312, the water outlet pipe 311 communicates with the circulation hole 312, and the water outlet pipe 311 also has a limited flow hole 313, the flow limit hole 313 communicates with the inside of the valve seat 302 .
当净水机为循环状态时,水从进水管310进入阀座302后,硅胶粒307被弹起,挡水板303和密封垫304在水压作用下被抬升,水进入循环腔室308内,然后经过循环孔312留到出水管311并循环到水泵的进水端,此时水泵作为循环泵使用;当净水机为制水状态时,硅胶粒307与挡水板303抵接,水从进水管310进入阀座302后,溢过隔板309后即通过限流孔313进入出水管311,此时水泵作为增压泵使用。本实用新型利用限流及循环电磁阀实现限流和循环两种状态的控制,利用限流及循环电磁阀的限流功能达到控制制水工作压力。净水机在边制水的同时可实现同时排放,使用便利性大大增强。 When the water purifier is in a circulating state, after water enters the valve seat 302 from the water inlet pipe 310, the silica gel particles 307 are bounced up, the water retaining plate 303 and the gasket 304 are lifted under the action of water pressure, and the water enters the circulation chamber 308 , and then left to the outlet pipe 311 through the circulation hole 312 and circulated to the water inlet end of the water pump. At this time, the water pump is used as a circulation pump; After entering the valve seat 302 from the water inlet pipe 310, it overflows the dividing plate 309 and then enters the water outlet pipe 311 through the flow limiting hole 313. At this time, the water pump is used as a booster pump. The utility model utilizes the current limiting and circulating electromagnetic valve to realize the control of the two states of current limiting and circulating, and utilizes the current limiting function of the current limiting and circulating electromagnetic valve to control the working pressure of water production. The water purifier can realize simultaneous discharge while producing water, which greatly enhances the convenience of use.
其中,所述挡水板303开设有漏水孔,所述密封垫304对应漏水孔的位置开设有通孔,通孔、漏水孔均与所述阀座302的内腔连通,确保渗入挡水板303顶部的水能及时通过漏水孔和通孔落入阀座302内部,避免液体渗漏到电磁阀体301外。 Wherein, the water retaining plate 303 is provided with a leaking hole, and the sealing gasket 304 is provided with a through hole corresponding to the leaking hole, and the through hole and the leaking hole are all communicated with the inner cavity of the valve seat 302 to ensure that the water retaining plate is infiltrated. The water on the top of the 303 can fall into the inside of the valve seat 302 through the leakage hole and the through hole in time, so as to prevent the liquid from leaking out of the electromagnetic valve body 301.
所述浓水出水管13的出水端还连接有冲洗管16,冲洗管16设置有冲洗电磁阀161,冲洗电磁阀161与所述电控装置130电连接。当需要冲洗RO膜50时,冲洗后的废水可通过冲洗管16排出,延长RO膜50的使用寿命。 The outlet end of the concentrated water outlet pipe 13 is also connected with a flushing pipe 16 , and the flushing pipe 16 is provided with a flushing solenoid valve 161 , which is electrically connected with the electric control device 130 . When the RO membrane 50 needs to be flushed, the waste water after flushing can be discharged through the flushing pipe 16 to prolong the service life of the RO membrane 50 .
以传统的净水机100加仑机型进行测试,在原水压力2.2kg,原水TDS为1960,原水温度为18℃的条件下,制得的纯水和排出的废水的不同比例下,TDS值的变化情况如下表所示: Tested with a traditional 100-gallon water purifier, the raw water pressure is 2.2kg, the raw water TDS is 1960, and the raw water temperature is 18°C. Under the different ratios of the pure water produced and the discharged waste water, the TDS value The changes are shown in the table below:
以本实用新型的微废水净水机100加仑机型进行测试,在原水压力2.3kg,原水TDS为1960,原水温度为18℃的条件下,制得的纯水和排出的废水的不同比例下,TDS值的变化情况如下表所示: Tested with the 100-gallon model of the micro-waste water purifier of the present utility model, under the conditions of raw water pressure 2.3kg, raw water TDS of 1960, and raw water temperature of 18°C, the prepared pure water and the discharged waste water are in different proportions , the change of TDS value is shown in the table below:
由上述两个数据表可以看出,当纯水和废水比例为1:3时,传统净水机与本实用新型的净水机的TDS值相接近,而当纯水和废水比例为1:1甚至是3:1和6:1时,本净水机的纯水TDS值比传统净水机的TDS值少20。本微废水净水机制得的纯水与废水的比例为3:1,在不损失TDS值的情况下,大大节约水资源,减少废水排放量,符合国家节能要求,纯水质量高,且保证RO膜50的使用寿命。 As can be seen from the above two data tables, when the ratio of pure water and waste water is 1:3, the TDS value of the traditional water purifier is close to that of the water purifier of the present utility model, and when the ratio of pure water and waste water is 1:3 1 or even 3:1 and 6:1, the pure water TDS value of this water purifier is 20 less than that of traditional water purifiers. The ratio of pure water to waste water produced by this micro-waste water purifier is 3:1. Without losing the TDS value, it greatly saves water resources and reduces waste water discharge. It meets the national energy-saving requirements. The service life of the RO membrane 50.
另外,本微废水净水机还具有以下优点: In addition, this micro-waste water purifier also has the following advantages:
A、由电控装置130控制,当水泵、限流及循环电磁阀打开时水机为循环状态,水泵此时作为循环泵使用,循环水流量为2升/分钟,其目的是利用大通量水流来冲洗RO膜,循环2分钟后,由电控装置130控制,限流及循环电磁阀关闭水机为制水状态,水泵此时作为增压泵使用,利用限流及循环电磁阀的限流功能达到控制制水工作压力。 A. Controlled by the electric control device 130, when the water pump, current limiting and circulation solenoid valves are opened, the water machine is in a circulating state. The water pump is used as a circulating pump at this time, and the circulating water flow rate is 2 liters per minute. The purpose is to use large flux The water flows to flush the RO membrane. After 2 minutes of circulation, the electric control device 130 controls the flow limiting and circulation solenoid valve to close the water machine and enters the water production state. The water pump is used as a booster pump at this time. Flow function to control the working pressure of water.
B、因为有大通量循环系统,净水机其自身具备了药物清洗RO膜50的功能,在传统机型使用时水中的钙、镁离子及胶体一旦堵塞RO膜50时,产水量严重不足,只能更换RO膜50。而本进水机可对RO膜50进行药物清洗,以此来延长RO膜50的使用寿命。经药物清洗后的RO膜50其产水量完全达到新RO膜50的水平,与传统机型相比其使用寿命延长3倍以上。 B. Because of the large flux circulation system, the water purifier itself has the function of cleaning the RO membrane 50 with drugs. When the calcium, magnesium ions and colloids in the water block the RO membrane 50 when the traditional model is used, the water production will be seriously insufficient. , only the RO membrane 50 can be replaced. And this water inlet machine can carry out medicine cleaning to RO membrane 50, prolong the service life of RO membrane 50 with this. The water yield of the RO membrane 50 after cleaning with drugs has reached the level of the new RO membrane 50, and its service life has been extended by more than 3 times compared with the traditional model.
其中,所述净水机还包括有与市电连接的电控装置130,所述进水电磁阀20、所述高压开关90、所述水泵30和所述限流及循环电磁阀60分别与所述电控装置130电连接。 Wherein, the water purifier also includes an electric control device 130 connected to the mains, the water inlet solenoid valve 20, the high pressure switch 90, the water pump 30 and the current limiting and circulation solenoid valve 60 are respectively connected to The electric control device 130 is electrically connected.
其中,所述水泵30的单位时间的通量为2.0L/min,即净水机的循环水通过RO膜50表面单位时间的通量为2.0L/min,利用水泵30的大通量使本实用新型的净水机自带有清洗RO膜50的功能。 Wherein, the flux per unit time of the water pump 30 is 2.0L/min, that is, the flux of the circulating water of the water purifier passing through the surface of the RO membrane 50 per unit time is 2.0L/min, and the large flux of the water pump 30 is used to make this The water purifier of the utility model has the function of cleaning the RO membrane 50.
其中,所述净水机还包括有用于清洗RO膜50的清洗液,清洗液为食品级的柠檬酸或白醋,便于取材,清洗成本低。具体实现如下:当水机产水流量下降或作为保养性药物清洗时,首先断水断电,将任意一只膜前预处理滤瓶取下,倒掉与清洗液相同比例的循环水,注满药液后再将滤瓶重新安装好,送电后让水泵30和限流及循环电磁阀60工作,滤瓶中的清洗药液在水泵30作用下循环药物冲洗RO膜50,根据RO膜50堵膜程度来确定药物清洗时间,清洗时间达到后,打开冲洗电磁阀161,将所有滤瓶中的清洗液彻底从冲洗管16中置换出来,从而完成药物清洗RO膜50的工作。膜前预处理滤瓶是指RO膜前连接的滤芯机构的滤瓶。 Wherein, the water purifier also includes a cleaning solution for cleaning the RO membrane 50, and the cleaning solution is food-grade citric acid or white vinegar, which is easy to obtain materials and has low cleaning cost. The specific implementation is as follows: When the flow rate of the water produced by the water machine drops or is used as a maintenance drug for cleaning, first cut off the water and power, remove any pre-membrane pretreatment filter bottle, pour out the circulating water in the same proportion as the cleaning solution, and fill it up. After the liquid medicine, the filter bottle is reinstalled, and the water pump 30 and the current-limiting and circulation solenoid valve 60 work after the power is supplied. The drug cleaning time is determined by the degree of membrane blocking. After the cleaning time is reached, the flushing solenoid valve 161 is opened to completely replace the cleaning solution in all filter bottles from the flushing pipe 16, thereby completing the work of cleaning the RO membrane 50 with the drug. The pre-membrane pretreatment filter bottle refers to the filter bottle of the filter element mechanism connected in front of the RO membrane.
其中,所述滤芯机构包括依次串联连接的一级滤芯41和二级滤芯42,所述一级滤芯41为活性炭滤芯,所述二级滤芯42为pp棉滤芯。滤芯结构简单,有利于更换和维护,降低使用和维修成本。 Wherein, the filter element mechanism includes a primary filter element 41 and a secondary filter element 42 connected in series in sequence, the primary filter element 41 is an activated carbon filter element, and the secondary filter element 42 is a pp cotton filter element. The filter element has a simple structure, which is convenient for replacement and maintenance, and reduces the cost of use and maintenance.
其中,所述后置过滤器110均活性炭滤芯过滤器,有利于改善纯水的口感,纯水饮用效果好。 Wherein, the post-filter 110 is an activated carbon filter element filter, which is beneficial to improve the taste of pure water, and the drinking effect of pure water is good.
实施例2Example 2
如图2所示,本实施例的滤芯机构包括并联连接的二级复合滤芯43和三级复合滤芯44,所述二级复合滤芯43、所述三级复合滤芯44的出水端分别与所述RO膜50的进水端连接,所述前置过滤器10为孔径20μm的折纸滤芯。进一步地,所述二级复合滤芯43、所述三级复合滤芯44均为活性炭和PP棉的复合滤芯,该复合滤芯的外层为孔径1-5μm的PP棉,PP棉内填充有烧结活性炭。 As shown in Figure 2, the filter element mechanism of the present embodiment comprises the secondary composite filter element 43 and the tertiary composite filter element 44 connected in parallel, and the water outlets of the secondary composite filter element 43 and the tertiary composite filter element 44 are respectively connected to the The water inlet end of the RO membrane 50 is connected, and the pre-filter 10 is an origami filter element with a pore size of 20 μm. Further, the two-stage composite filter element 43 and the three-stage composite filter element 44 are composite filter elements of activated carbon and PP cotton, the outer layer of the composite filter element is PP cotton with a pore size of 1-5 μm, and the PP cotton is filled with sintered activated carbon .
第一级的折纸滤芯(前置过滤器10)的作用在于过滤原水中较大颗粒物质,使整套过滤系统起到先粗滤后细滤作用,并且折纸滤芯较PP棉滤芯其表面积增加数倍故而延长了使用寿命。所述二级滤芯、三级滤芯为复合滤芯,所述复合滤芯的结构为外层为孔径1-5微米的PP棉滤料,其作用为过滤原水中较小颗粒物质,内层为烧结活性炭,其主要作用为吸附原水中的余氯,并且烧结活性炭比较颗粒碳其吸附能力更强可达2倍以上。将二级复合滤芯43、三级复合滤芯44采用并联连接更能有效发挥其功效,通过改变连接方式及改变滤芯结构可最大提高RO膜50前预处理的功效及使用寿命。 The function of the first-stage origami filter element (pre-filter 10) is to filter larger particles in the raw water, so that the entire filtration system can perform coarse filtration first and then fine filtration, and the surface area of the origami filter element is several times larger than that of the PP cotton filter element Therefore, the service life is prolonged. The secondary filter element and the tertiary filter element are composite filter elements, and the structure of the composite filter element is that the outer layer is a PP cotton filter material with a pore size of 1-5 microns, and its function is to filter smaller particulate matter in raw water, and the inner layer is sintered activated carbon , its main function is to adsorb residual chlorine in raw water, and the adsorption capacity of sintered activated carbon is more than 2 times stronger than that of granular carbon. Connecting the secondary composite filter element 43 and the tertiary composite filter element 44 in parallel can exert their effects more effectively. By changing the connection mode and the structure of the filter element, the efficiency and service life of the pretreatment before the RO membrane 50 can be improved to the greatest extent.
本实施例的其余部分与实施例1相同,这里不再赘述。 The rest of this embodiment is the same as Embodiment 1, and will not be repeated here.
最后应当说明的是,以上实施例仅用以说明本实用新型的技术方案,而非对本实用新型保护范围的限制,尽管参照较佳实施例对本实用新型作了详细地说明,本领域的普通技术人员应当理解,可以对本实用新型的技术方案进行修改或者等同替换,而不脱离本实用新型技术方案的实质和范围。 Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present utility model, rather than limiting the protection scope of the present utility model. Although the utility model has been described in detail with reference to the preferred embodiments, those skilled in the art Personnel should understand that the technical solution of the utility model can be modified or equivalently replaced without departing from the essence and scope of the technical solution of the utility model.
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| CN104649454A (en) * | 2015-03-10 | 2015-05-27 | 广东汇聚环保科技有限公司 | A micro-waste water purifier |
| CN114671493A (en) * | 2020-12-24 | 2022-06-28 | 广东栗子科技有限公司 | A small flow desktop water purification system, water purification control method and water purification equipment |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104649454A (en) * | 2015-03-10 | 2015-05-27 | 广东汇聚环保科技有限公司 | A micro-waste water purifier |
| CN104649454B (en) * | 2015-03-10 | 2016-04-06 | 广东汇聚环保科技有限公司 | Little waste water purifier |
| CN114671493A (en) * | 2020-12-24 | 2022-06-28 | 广东栗子科技有限公司 | A small flow desktop water purification system, water purification control method and water purification equipment |
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