CN102344186B - Integrated portable water purifier - Google Patents

Integrated portable water purifier Download PDF

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CN102344186B
CN102344186B CN 201010244409 CN201010244409A CN102344186B CN 102344186 B CN102344186 B CN 102344186B CN 201010244409 CN201010244409 CN 201010244409 CN 201010244409 A CN201010244409 A CN 201010244409A CN 102344186 B CN102344186 B CN 102344186B
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backwash
water
pipeline
valve
water inlet
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CN102344186A (en
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李伟英
谢良杰
张明
陆俊宇
许京晶
陆辉
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Tongji University
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Tongji University
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Abstract

本发明涉及一体化便携式净水器,净水器壳体(19)内设置进水管路(1)、膜组件(7)、排污管路(8)、产水管路(12)及反洗管路(13),膜组件(7)为柱状结构,内部设有超滤膜,顶部设置排污口,侧面的上部设置产水口,侧面的下部设置反洗口,底部设置进水口,进水管路(1)与进水口连接,排污管路(8)与排污口连接,产水管路(12)与产水口连接,反洗管路(13)与反洗口连接。与现有技术相比,本发明产水量大,水质稳定可靠,符合饮用水水质要求,且设备抗冲击负荷能力强,适用于一定人数的团体集体野外活动的饮用水需求,另外抗污染能力强,膜组件更换方便,集成化程度高,占地面积小,空间利用率合理。

Figure 201010244409

The invention relates to an integrated portable water purifier. A water inlet pipeline (1), a membrane module (7), a sewage pipeline (8), a water production pipeline (12) and a backwashing pipe are arranged in a water purifier housing (19) The road (13), the membrane module (7) is a columnar structure, the interior is provided with an ultrafiltration membrane, the top is provided with a sewage outlet, the upper part of the side is provided with a water production outlet, the lower part of the side is provided with a backwash outlet, the bottom is provided with a water inlet, and the water inlet pipeline ( 1) Connected to the water inlet, the sewage pipeline (8) is connected to the sewage outlet, the water production pipeline (12) is connected to the water production outlet, and the backwash pipeline (13) is connected to the backwash outlet. Compared with the prior art, the present invention has large water production, stable and reliable water quality, meets the requirements of drinking water quality, and the equipment has strong impact load resistance, and is suitable for the drinking water demand of a group of a certain number of collective field activities. In addition, the anti-pollution ability is strong , The membrane module is easy to replace, the degree of integration is high, the floor area is small, and the space utilization rate is reasonable.

Figure 201010244409

Description

Integrated portable water purifier
Technical field
The present invention relates to a kind of purifier, especially relate to integrated portable water purifier.
Background technology
At present, domestic in known patented technology, the water purifier that has suitable family to use, but the volume of this type of water purifier is larger, mainly is to rely on the gravity of water to realize purifying purpose, lacks the required power system of open-air water processed; In addition, common small-sized water purifier is a kind of device with purification filtering that can directly be connected on the water tap, only can purify tap water, but can't realize the water purifier system self-purification, change also and can only judge the pollution level that to judge intuitively filter core by means of the time; Common small-size household water purifier relies on very large to tap water Infrastructure, not only can not carry, and can not be field work personnel, outdoor enthusiast and disaster area (such as earthquake and big flood etc.) people's high efficiency manufacture tap water.
Summary of the invention
Purpose of the present invention is exactly to provide the integrated portable water purifier that a kind of water production rate is large, stain resistance is strong, integrated degree is high for the defective that overcomes above-mentioned prior art existence.
Purpose of the present invention can be achieved through the following technical solutions:
Integrated portable water purifier, comprise case of water purifier, it is characterized in that, in the described case of water purifier suction culvert is set, membrane module, blow-off line, water producing pipe road and backwash pipeline, described membrane module is columnar structure, inside is provided with ultra-filtration membrane, the top of membrane module arranges sewage draining exit, the top of side arranges produces the mouth of a river, and the bottom of side arranges the backwash mouth, and the bottom arranges water-in, described suction culvert is connected with described water-in, described blow-off line is connected with described sewage draining exit, and described water producing pipe road is connected with the described product mouth of a river, and described backwash pipeline is connected with described backwash mouth.
Intake pump, flooding velocity variable valve, flooding velocity meter, inlet gage and water intaking valve are set on the described suction culvert, described intake pump, flooding velocity are taken into account water intaking valve and are connected in turn on the water-in of membrane module through pipeline, described flooding velocity variable valve and intake pump are installed side by side, flooding velocity variable valve one termination enters the intake pump import, between the other end access intake pump outlet and the import of flooding velocity meter, described inlet gage is located between the outlet and water intaking valve of flooding velocity meter.
On the described blow-off line wash water valve is set.
Product discharge is set on the described water producing pipe road takes into account the product water valve, described product water ga(u)ge is located at the product mouth of a river of membrane module and produces between the water valve.
Backwash flow control valve, backwashing pump, backwash pressure table, backwash flow are set on the described backwash pipeline take into account backwash valve, described backwashing pump, backwash flow are taken into account backwash valve and are connected in turn on the backwash mouth of membrane module through pipeline, described backwash pressure table is located between the import of backwash pump outlet and backwash under meter, described backwash flow control valve and backwashing pump are installed side by side, backwash flow control valve one termination enters the import of backwashing pump, between the other end access backwash pump outlet and the import of backwash under meter.
Described intake pump and backwashing pump are vacuum primingpump.
Described flooding velocity variable valve and backwash flow control valve are gate valve.
Described flooding velocity meter, product discharge are taken into account the backwash flow and are counted glass rotameter.
Described inlet gage and backwash pressure table are for rushing oily formula anti-shock pressure meter.
The porosity of described ultra-filtration membrane is 77.8%, contact angle is 42 °, and mean pore size is 0.1715um, and this ultra-filtration membrane is held back the molecular weight ranges of material 5 dalton to 10, ten thousand dalton.
The porosity of described ultra-filtration membrane is 77.5%, contact angle is 38.5 °, and mean pore size is 0.1715um, and this ultra-filtration membrane is held back the molecular weight ranges of material 5 dalton to 7, ten thousand dalton.
The porosity of described ultra-filtration membrane is 77.%, contact angle is 32.4 °, and mean pore size is 0.1715um, and this ultra-filtration membrane is held back the molecular weight ranges of material 5 dalton to 6, ten thousand dalton.
The flexible pipe that described suction culvert, blow-off line, water producing pipe road and backwash pipeline use pipeline to make as UPVC.
Described integrated portable water purifier is provided with cross flow filter system, dead-end filtration system, suitable flushing system and backwashing system, and both the former water of applicable different quality can prevent effectively again that film from polluting.
Compared with prior art, the present invention has the following advantages:
(1) (15~50L/h), water conditioning is reliable, meets the drinking-water quality requirement, and the equipment anti-shock portative power is strong, is applicable to the outdoorsman tap water demand of collective of group of certain number greatly for water production rate;
(2) contamination resistance is strong, and system arranges self-cleaning system, can through effectively realize the self-cleaning of system along punching and backwash operation, largely strengthen the resistance to crocking of water purifier core component membrane module;
(3) core component (membrane module) is changed conveniently;
(4) be provided with membrane module external and internal pressure table, can judge by pressure difference the pollution level of membrane module, be convenient to timely replacing;
(5) integrated degree is high, and floor space is little, and space availability ratio is reasonable.
Description of drawings
Fig. 1 is structural representation of the present invention.
1 is that water-in, 2 is that intake pump, 3 is that flooding velocity variable valve, 4 is that flooding velocity meter, 5 is that inlet gage, 6 is that water intaking valve, 7 is that membrane module, 8 is that sewage draining exit, 9 is that wash water valve, 10 is that product water ga(u)ge, 11 is that product water valve, 12 is that the product mouth of a river, 13 is that backwash water-in, 14 is that backwash flow control valve, 15 is that backwashing pump, 16 is that backwash pressure table, 17 is that backwash under meter, 18 is that backwash valve, 19 is case of water purifier among the figure.
Embodiment
The present invention is described in detail below in conjunction with the drawings and specific embodiments.
Embodiment
Integrated portable water purifier, its structure as shown in Figure 1, case of water purifier 19 interior suction culvert 1, membrane module 7, blow-off line 8, water producing pipe road 12 and the backwash pipelines 13 of arranging, membrane module 7 is columnar structure, inside is provided with ultra-filtration membrane, the porosity of this ultra-filtration membrane is 77.8%, contact angle is 42 °, holds back the molecular weight ranges of material 5 dalton to 10, ten thousand dalton; Preferable porosity is 77.5%, contact angle is 38.5 °, holds back the molecular weight ranges of material at 5 dalton to 7, ten thousand daltonian ultra-filtration membranes; More preferably porosity is 77.%, contact angle is 32.4 °, holds back the molecular weight ranges of material at 5 dalton to 6, ten thousand daltonian ultra-filtration membranes, and the mean pore size of above-mentioned ultra-filtration membrane is 0.1715um.The top of membrane module 7 arranges sewage draining exit, the top of side arranges produces the mouth of a river, the bottom of side arranges the backwash mouth, the bottom arranges water-in, suction culvert 1 is connected with water-in, and blow-off line 8 is connected with sewage draining exit, and water producing pipe road 12 is connected with the product mouth of a river, backwash pipeline 13 with the backwash mouth be connected, suction culvert 1, blow-off line 8, water producing pipe road 12 and backwash pipeline 13 use pipeline to be the flexible pipe that UPVC makes.
Intake pump 2, flooding velocity variable valve 3, flooding velocity meter 4, inlet gage 5 and water intaking valve 6 are set on the suction culvert 1, wherein, intake pump 2, flooding velocity meter 4 and water intaking valve 6 are connected in turn on the water-in through pipeline, flooding velocity variable valve 3 is installed side by side with intake pump 2, one termination enters intake pump 2 imports, between 2 outlets of the other end access intake pump and 4 imports of flooding velocity meter, inlet gage 5 is located between the outlet and water intaking valve 6 of flooding velocity meter 4.
Wash water valve 9 is set on the blow-off line 8, arranges on the water producing pipe road 12 and produce water ga(u)ge 10 and produce water valve 11, produce water ga(u)ge 10 and be located between the product mouth of a river and the product water valve 11.
Backwash flow control valve 14, backwashing pump 15, backwash pressure table 16, backwash under meter 17 and backwash valve 18 are set on the backwash pipeline 13, wherein, backwashing pump 15, backwash under meter 17 and backwash valve 18 are connected in turn on the backwash mouth of membrane module 7 through pipeline, backwash pressure table 16 is located between the import of the outlet of backwashing pump 15 and backwash under meter 17 backwash flow control valve 14 and installs side by side with backwashing pump 15, one termination enters the import of backwashing pump 15, between the outlet and 17 imports of backwash under meter of the other end access backwashing pump 15.
Water purifier is provided with cross flow filter system, dead-end filtration system, suitable flushing system and backwashing system, and this invention is the former water of applicable different quality both, can prevent effectively that again film from polluting, and has following operating method:
(1) end-filtration operation
Open flooding velocity variable valve 3, water intaking valve 6 and produce water valve 11, close wash water valve 9 and backwash valve 18.Former water enters membrane module 7 from water-in 1 through intake pump 2, flooding velocity meter 4, inlet gage 5 and water intaking valve 6, produces water and flows out multiparity water ga(u)ge 10, produces the water valve 11 multiparity mouths of a river, 12 water outlets from membrane module 7.Can realize the water production rate of Controlling System and advance film pressure by regulating flooding velocity variable valve 3.
(2) cross flow filter operation
Open flooding velocity variable valve 3, water intaking valve 6, wash water valve 9 and produce water valve 11, close backwash valve 18.Former water enters membrane module 7 from water-in 1 through intake pump 2, flooding velocity meter 4, inlet gage 5 and water intaking valve 6, produce water and enter product water tank 13 from membrane module 7 outflow multiparity water ga(u)ges 10, product water valve 11 and the product mouth of a river 12, dense water flows out through wash water valve 9 and sewage draining exit 8 outflows from membrane module 7.Can realize control product water ratio and advance film pressure by regulating flooding velocity variable valve 3.When raw water quality is relatively relatively poor, can adopt this kind operation scheme water processed, rely on dense water in the shearing souring on film surface, guaranteed product water water quality, effectively reduce film and pollute.
(3) along the punching operation
Open flooding velocity variable valve 3, water intaking valve 6 and wash water valve 9, close and produce water valve 11 and backwash valve 18.Current enter through intake pump 2, flooding velocity meter 4, inlet gage 5 and water intaking valve 6 from water-in 1 and enter membrane module 7, wash away the pollution substance of film surface adsorption and precipitation, then sewage flows out through wash water valve 9 from membrane module 7 and discharges, and can realize controlling washing water quantity and advance film pressure by regulating flooding velocity variable valve 3.
(4) backwash operation
Open backwash valve 18, backwash flow control valve 14 and wash water valve 9, close water intaking valve 6 and produce water valve 11.Backwash enters membrane module 7 from backwash water-in 13, backwashing pump 15, backwash pressure table 16, backwash under meter 17 and backwash valve 18, adsorbs to be rinsed with the pollution substance that is deposited on the film surface to drain through wash water valve 9 and sewage draining exit 8 down.The backwash water yield and backwash pressure can be by regulating 14 controls of backwash flow control valve.
The selection of water pump is most important to whole system, is the prerequisite of assurance equipment steady running.Intake pump 2 and backwashing pump 15 among the present invention are vacuum primingpump, can guarantee system stable operation.
Each valve among the present invention all adopts gate valve, comprises flooding velocity variable valve 3, water intaking valve 6, wash water valve 9, produces water valve 11, backwash flow control valve 14 and backwash valve 18.Because gate valve is easy to slowly, continuously and stably adjust flux and pressure, be conducive to the stable of operations and carry out, the core membrane module of equipment is had good provide protection.
Flooding velocity meter 4 among the present invention, product water ga(u)ge 10 and backwash under meter 17 are all selected glass rotameter, inlet gage 5 selects to rush oily formula tensimeter with backwash pressure table 16, this kind tensimeter is the Anti-seismic tensimeter, and working pressure is stable, is conducive to open-air mal-condition and uses.

Claims (7)

1.一体化便携式净水器,包括净水器壳体(19),其特征在于,所述的净水器壳体(19)内设置进水管路(1)、膜组件(7)、排污管路(8)、产水管路(12)及反洗管路(13),所述的膜组件(7)为柱状结构,内部设有超滤膜,膜组件(7)的顶部设置排污口,侧面的上部设置产水口,侧面的下部设置反洗口,底部设置进水口,所述的进水管路(1)与所述的进水口连接,所述的排污管路(8)与所述的排污口连接,所述的产水管路(12)与所述的产水口连接,所述的反洗管路(13)与所述的反洗口连接;1. An integrated portable water purifier, including a water purifier housing (19), characterized in that, the water purifier housing (19) is provided with a water inlet pipeline (1), a membrane module (7), a sewage discharge Pipeline (8), water production pipeline (12) and backwash pipeline (13), the membrane module (7) is a columnar structure with an ultrafiltration membrane inside, and a sewage outlet is set on the top of the membrane module (7) , the upper part of the side is provided with a water production port, the lower part of the side is provided with a backwash port, and the bottom is provided with a water inlet, the water inlet pipeline (1) is connected to the water inlet, the sewage discharge pipeline (8) is connected to the The sewage outlet is connected, the water production pipeline (12) is connected to the water production outlet, and the backwash pipeline (13) is connected to the backwash outlet; 所述的进水管路(1)上设置进水泵(2)、进水流量调节阀(3)、进水流量计(4)、进水压力表(5)及进水阀(6),所述的进水泵(2)为自吸泵,所述的进水流量计(4)为玻璃转子流量计,所述的进水压力表(5)为冲油式抗震压力表,进水泵(2)、进水流量计(4)及进水阀(6)经管道依次连接在膜组件(7)的进水口上,所述的进水流量调节阀(3)为闸阀,与进水泵(2)并列安装,进水流量调节阀(3)一端接入进水泵(2)进口,另一端接入进水泵(2)出口与进水流量计(4)进口之间,所述的进水压力表(5)设在进水流量计(4)的出口与进水阀(6)之间;The water inlet pipeline (1) is provided with an inlet pump (2), an inlet flow regulating valve (3), an inlet flowmeter (4), an inlet pressure gauge (5) and an inlet valve (6). The water inlet pump (2) is a self-priming pump, the water inlet flowmeter (4) is a glass rotameter, the water inlet pressure gauge (5) is an oil flushing anti-seismic pressure gauge, and the water inlet pump (2) ), the water inlet flow meter (4) and the water inlet valve (6) are connected to the water inlet of the membrane module (7) through pipelines in turn, and the water inlet flow regulating valve (3) is a gate valve, which is connected with the water inlet pump (2 ) are installed side by side, one end of the water inlet flow regulating valve (3) is connected to the inlet of the water inlet pump (2), and the other end is connected between the outlet of the water inlet pump (2) and the inlet of the water inlet flowmeter (4). The meter (5) is set between the outlet of the water inlet flow meter (4) and the water inlet valve (6); 所述的反洗管路(13)上设置反洗流量调节阀(14)、反洗泵(15)、反洗压力表(16)、反洗流量计(17)及反洗阀(18),所述的流量调节阀(14)为闸阀,所述的反洗泵(15)为自吸泵,所述的反洗压力表(16)为冲油式抗震压力表,所述的反洗流量计(17)为玻璃转子流量计,反洗泵(15)、反洗流量计(17)及反洗阀(18)经管道依次连接在膜组件(7)的反洗口上,所述的反洗压力表(16)设在反洗泵(15)的出口与反洗流量计(17)的进口之间,所述的反洗流量调节阀(14)为闸阀,与反洗泵(15)并列安装,反洗流量调节阀(14)一端接入反洗泵(15)的进口,另一端接入反洗泵(15)的出口与反洗流量计(17)进口之间。The backwash pipeline (13) is provided with a backwash flow regulating valve (14), a backwash pump (15), a backwash pressure gauge (16), a backwash flow meter (17) and a backwash valve (18) , the flow regulating valve (14) is a gate valve, the backwash pump (15) is a self-priming pump, the backwash pressure gauge (16) is an oil flushing anti-seismic pressure gauge, and the backwash The flow meter (17) is a glass rotameter, and the backwash pump (15), backwash flow meter (17) and backwash valve (18) are sequentially connected to the backwash port of the membrane module (7) through pipelines. The backwash pressure gauge (16) is set between the outlet of the backwash pump (15) and the inlet of the backwash flowmeter (17), and the backwash flow regulating valve (14) is a gate valve, which is connected with the backwash pump (15) ) are installed side by side, one end of the backwash flow regulating valve (14) is connected to the inlet of the backwash pump (15), and the other end is connected between the outlet of the backwash pump (15) and the inlet of the backwash flowmeter (17). 2.根据权利要求1所述的一体化便携式净水器,其特征在于,所述的排污管路(8)上设置排污阀(9)。2. The integrated portable water purifier according to claim 1, characterized in that, the sewage discharge pipeline (8) is provided with a sewage discharge valve (9). 3.根据权利要求1所述的一体化便携式净水器,其特征在于,所述的产水管路(12)上设置产水流量计(10)及产水阀(11),所述的产水流量计(10)为玻璃转子流量计,设在膜组件(7)的产水口与产水阀(11)之间。3. The integrated portable water purifier according to claim 1, characterized in that, the water production pipeline (12) is provided with a water production flow meter (10) and a water production valve (11), and the production water The water flow meter (10) is a glass rotameter, which is arranged between the water production port of the membrane module (7) and the water production valve (11). 4.根据权利要求1所述的一体化便携式净水器,其特征在于,所述的超滤膜的孔隙率为77.8%、接触角为42°,平均孔径为0.1715um,该超滤膜截留物质的分子量范围在5道尔顿至10万道尔顿。4. The integrated portable water purifier according to claim 1, characterized in that, the porosity of the ultrafiltration membrane is 77.8%, the contact angle is 42°, and the average pore diameter is 0.1715um. The molecular weight of the species ranges from 5 Daltons to 100,000 Daltons. 5.根据权利要求1所述的一体化便携式净水器,其特征在于,所述的超滤膜的孔隙率为77.5%、接触角为38.5°,平均孔径为0.1715um,该超滤膜截留物质的分子量范围在5道尔顿至7万道尔顿。5. The integrated portable water purifier according to claim 1, characterized in that, the porosity of the ultrafiltration membrane is 77.5%, the contact angle is 38.5°, and the average pore diameter is 0.1715um. The molecular weight of the species ranges from 5 Daltons to 70,000 Daltons. 6.根据权利要求1所述的一体化便携式净水器,其特征在于,所述的超滤膜的孔隙率为77.%、接触角为32.4°,平均孔径为0.1715um,该超滤膜截留物质的分子量范围在5道尔顿至6万道尔顿。6. The integrated portable water purifier according to claim 1, wherein the porosity of the ultrafiltration membrane is 77.%, the contact angle is 32.4°, and the average pore diameter is 0.1715um. The molecular weight of the intercepted species ranges from 5 Daltons to 60,000 Daltons. 7.根据权利要求1所述的一体化便携式净水器,其特征在于,所述的进水管路(1)、排污管路(8)、产水管路(12)及反洗管路(13)使用管道为UPVC制造的软管。7. The integrated portable water purifier according to claim 1, characterized in that the water inlet pipeline (1), the sewage pipeline (8), the water production pipeline (12) and the backwash pipeline (13 ) use pipes made of UPVC hose.
CN 201010244409 2010-08-03 2010-08-03 Integrated portable water purifier Expired - Fee Related CN102344186B (en)

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CN113603168A (en) * 2021-08-12 2021-11-05 深圳市汉尔顿环保科技有限公司 Manual-automatic water purifier frequency conversion control system and water purifier with same

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Publication number Priority date Publication date Assignee Title
CN2899920Y (en) * 2006-05-22 2007-05-16 杨永平 Super filter water purifier
CN200942333Y (en) * 2006-08-16 2007-09-05 张健锋 Automatic ultrafiltration machine
CN201454425U (en) * 2009-07-17 2010-05-12 浙江玉泉环境工程有限公司 Ultrafiltration membrane water-air mixing cleaning device

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JP2008183510A (en) * 2007-01-30 2008-08-14 Toray Ind Inc Purified water production method and apparatus

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Publication number Priority date Publication date Assignee Title
CN2899920Y (en) * 2006-05-22 2007-05-16 杨永平 Super filter water purifier
CN200942333Y (en) * 2006-08-16 2007-09-05 张健锋 Automatic ultrafiltration machine
CN201454425U (en) * 2009-07-17 2010-05-12 浙江玉泉环境工程有限公司 Ultrafiltration membrane water-air mixing cleaning device

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Title
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