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.