CN204939036U - A kind of field emergency anti-penetration water purifier - Google Patents
A kind of field emergency anti-penetration water purifier Download PDFInfo
- Publication number
- CN204939036U CN204939036U CN201520674821.3U CN201520674821U CN204939036U CN 204939036 U CN204939036 U CN 204939036U CN 201520674821 U CN201520674821 U CN 201520674821U CN 204939036 U CN204939036 U CN 204939036U
- Authority
- CN
- China
- Prior art keywords
- reverse osmosis
- osmosis membrane
- mount pump
- motor
- shell
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Abstract
The utility model relates to a kind of field emergency anti-penetration water purifier, comprises a RO reverse osmosis membrane, RO reverse osmosis membrane shell, motor-mount pump, motor-mount pump shell, described RO reverse osmosis membrane is located in RO reverse osmosis membrane shell, the sewage draining exit of described RO reverse osmosis membrane and the first row mouth of a river of RO reverse osmosis membrane shell, the pure water outlet of RO reverse osmosis membrane is connected respectively by pipeline with the second row mouth of a river of RO reverse osmosis membrane shell, described motor-mount pump is located in motor-mount pump shell, described motor-mount pump shell is connected to the below of RO reverse osmosis membrane shell, and the water outlet of described motor-mount pump is connected with the water inlet of RO reverse osmosis membrane, the source water inlet that water-in and the motor-mount pump outer casing bottom of described motor-mount pump are provided with is connected, described motor-mount pump is connected with the power electric be provided with outside motor-mount pump shell, structure is simple, be easy to carry, can be practical in the wild, and filtration, purification is respond well.
Description
Technical field
The utility model relates to water treating equipment, is specifically related to a kind of field emergency anti-penetration water purifier.
Background technology
Field man often runs into drinkable fresh water under-reserve, and various reasons, again less than supplementing timely, needs to fetch water from field the problem of drinking.And the water quality in field does not reach the standard of drinking far away, the severe overweights such as earth sandy soil, bacterium, germ, heavy metal, organism, pollutent;
Dopant type main in nature surface water, amounts to 8 kinds of impurity species types.
1. particulate matter (ParticulateMatter), comprise the granulometric impurities such as silt, iron rust, algae, suspended substance, primitive fiber, naked eyes are visible.These particulates are usually suspended among current, the turbid phenomenon that water produces.These particulates are very unstable, can remove by precipitating and filter.Water is when leaving standstill, and heavy particulate (mainly the inorganic substance of sand and clay one class) can avale.On light particulate (mainly a class organic compound of animals and plants and remains thereof) can be bubbled through the water column, with preliminary sedimentation, the separation methods such as filtration can remove.Particulate matter is the main source causing turbidity, colourity, smell.All may exist in the tap water of tap water, secondary supply, rivers and lakes water.
2. colloidalmaterial, colloidalmaterial is larger than ionic species and, diameter particulate 10-4 ~ 10-6mm between less than particulate matter.Colloid is the aggregation of many molecules and ion.The compound of the inorganic mineral colloid in natural water mainly iron, aluminium and silicon.The limbs of the organic colloidal matter in water mainly plant or animal rot the Humus of Sum decomposition.Wherein maximum with the humus content in Lake Water, therefore usually make water be yellow-green colour or brown.Colloidal solid can not the sedimentation and removing voluntarily of mat gravity, is generally in water, to add medicament destroy it and stablize, and makes that colloidal solid increases and sedimentation is removed.All may there is colloidalmaterial in surface water or underground water.
3. ionic species (Ionicmaterial), comprising: positively charged ion, negatively charged ion.Positively charged ion is as calcium ion, magnesium ion, iron ion etc.; Negatively charged ion chlorion, sulfate ion, phosphate ion etc.
4. nonreactive gas dissolved, as the nitrogen etc. in air.
5. the gas dissolved that can react, gas dissolved common in natural water has oxygen (O2), carbonic acid gas (CO2), sometimes also has hydrogen sulfide (H2S), sulfurous gas (SO2), nitrogen (N2) and ammonia (NH3) etc.These gas be dissolved in the water, mostly has corrosive nature to metal, is the important factor causing water system metallic corrosion.CO2 in air has the greatest impact to pure water.CO2 to be present in air and to be easy to soluble in water, and make water quality be acid, namely pH value is lower than 7.Water quality is purer, is more subject to the impact of air, and affecting main manifestations is pH value, conductance (resistance) rate.
6. microorganism, mainly refers to the bacteria content in water.The Conventional bacteria of China's tap water allows content < 100cfu/ml; The Conventional bacteria of pure water allows content < 1cfu/ml.
7. thermal source, thermal source also known as bacterial endotoxin, be mainly used in medicinal water particularly water for injection time need consider thermal source content control.When having the application of the biological aspects such as cell cultures in laboratory, to thermal source content control overflow.
8. organic substance, the organic substance in water mainly refers to the pollutent of humic acid, sanitary sewage and trade effluent.Humic substance is the product of the vital movement process of hydrobiont one class.These Organic pollutants water body, and make water quality deterioration.Organism in water has individual common feature, will carry out bio-oxidation decomposition exactly, needs to consume the dissolved oxygen in water, and causes anoxic in water.Can putrid fermentation be there is simultaneously, make bacterial growth, worsen water quality, destroy water body; The organic contamination of process water, also can reduce the quality of product.Organism is the one of the main reasons causing water pollution.In surface water, organic content is usually above the content in underground water.
Current in order to purify got water, can quote, usually adopt activated carbon filtration and large-scale filtering purifying equipment, and in the environment worked in the wild, activated carbon filtration generally just adsorbs the impurity of some larger particles, cannot except the comparatively small impurities molecule in anhydrating; Although large-scale filtering purifying equipment filtration, purification effect is fine, defect cannot be carried in the wild.
Utility model content
In order to overcome the shortcoming of above-mentioned prior art, it is fine that the purpose of this utility model is to provide a kind of filtration, purification effect, and the field emergency anti-penetration water purifier that can carry.
In order to achieve the above object, the technical scheme that the utility model is taked is: a kind of field emergency anti-penetration water purifier, comprises a RO reverse osmosis membrane, RO reverse osmosis membrane shell, motor-mount pump, motor-mount pump shell;
Described RO reverse osmosis membrane is located in RO reverse osmosis membrane shell, the sewage draining exit of described RO reverse osmosis membrane and the first row mouth of a river of RO reverse osmosis membrane shell, the pure water outlet of RO reverse osmosis membrane is connected respectively by pipeline with the second row mouth of a river of RO reverse osmosis membrane shell, described motor-mount pump is located in motor-mount pump shell, described motor-mount pump shell is connected to the below of RO reverse osmosis membrane shell, and the water outlet of described motor-mount pump is connected with the water inlet of RO reverse osmosis membrane, the source water inlet that water-in and the motor-mount pump outer casing bottom of described motor-mount pump are provided with is connected, described motor-mount pump is connected with the power electric be provided with outside motor-mount pump shell.
Filtering net is provided with in described source water inlet.
Described RO reverse osmosis membrane shell and described motor-mount pump shell are threaded connection.
Described RO reverse osmosis membrane shell is connected by buckle with described motor-mount pump shell.
Described motor-mount pump shell is provided with battery compartment, is provided with battery in this battery compartment, and described battery is electrically connected with motor-mount pump.
Described motor-mount pump is V DC electropump.
The utility model adopts above technical scheme, have the following advantages, structure is simple, be easy to carry, can be practical in the wild, and filtration, purification is respond well, the ratio of desalinization of the RO reverse osmosis membrane reverse osmosis simultaneously adopted is high, the ratio of desalinization of single film can reach 99%, the general Absorbable organic halogens of single-stage reverse osmosis system ratio of desalinization is more than 90%, the general Absorbable organic halogens of double-stage reverse osmosis system ratio of desalinization is more than 98%, because reverse osmosis effectively can remove the microorganisms such as bacterium, organism, and the inorganics such as metallic element, effluent quality is greatly better than other method, reverse osmosis pure water running cost and cost of labor cheap, reduce environmental pollution, slow down the product water change of water quality caused due to source water quality fluctuation, thus water quality stable in being conducive to producing, this has positive effect to the stable of pure water quality product.
Accompanying drawing explanation
Fig. 1: structural representation of the present utility model.
In figure: 1.RO reverse osmosis membrane shell; 2. motor-mount pump shell; 3.RO reverse osmosis membrane; 4. motor-mount pump; 5. water inlet; 6. filtering net; 7. source water inlet; 8. battery compartment; 9. battery; 10. sewage draining exit; 11. first row water holes; The 12. second row mouths of a river; 13. pure water outlets.
Embodiment
Below in conjunction with drawings and Examples, the utility model is described in detail.
Embodiment 1
As shown in Figure 1, a kind of field emergency anti-penetration water purifier, is characterized in that, comprises a RO reverse osmosis membrane 3, RO reverse osmosis membrane shell 1, motor-mount pump 4, motor-mount pump shell 2;
Described RO reverse osmosis membrane 3 is located in RO reverse osmosis membrane shell 1, the sewage draining exit 10 of described RO reverse osmosis membrane 3 and the first row mouth of a river 11 of RO reverse osmosis membrane shell 1, the pure water outlet 13 of RO reverse osmosis membrane 3 is connected respectively by pipeline with the second row mouth of a river 12 of RO reverse osmosis membrane shell 1, described motor-mount pump 4 is located in motor-mount pump shell 2, described motor-mount pump shell 2 is connected to the below of RO reverse osmosis membrane shell 1, and the water outlet of described motor-mount pump 4 is connected with the water inlet 5 of RO reverse osmosis membrane 3, the water-in of described motor-mount pump 4 is connected with the source water inlet 7 be provided with bottom motor-mount pump shell 2, described motor-mount pump 4 is connected with the power electric be provided with outside motor-mount pump shell 2.
When field work personnel with pure water finish off time, back with water inlet line is accessed to source water inlet 7, the other end of this pipeline is placed with the place of water, open motor-mount pump 4, motor-mount pump 4 is pumped into water in RO reverse osmosis membrane 3, there is no treated water after RO reverse osmosis membrane 3, the sewage produced is discharged by sewage draining exit 10, the pure water produced is discharged by pure water outlet 13, drink for people, can find out that the anti-penetration water purifier structure in the present embodiment is simple, be easy to carry, and work is simple, and filtration, purification is respond well;
The RO reverse osmosis membrane adopted in the present embodiment is the art personnel known RO reverse osmosis filter core, it is a kind of artificial semi-permeable membranes with certain characteristic of simulating biological semi-permeable film and making, general macromolecular material is made, as cellulose acetate membrane, aromatic polyhydrazide film, aromatic polyamide film; The diameter of surface micropore is generally between 0.5 ~ 10nm, and the size of perviousness is relevant with the chemical structure of film itself.Some macromolecular materials are good to the repellency of salt, and the penetration speed of water bad.Some high polymer material chemical structures have more hydrophilic radical, and thus the penetration speed of water is relatively very fast.Therefore a kind of reverse osmosis membrane of satisfaction should have suitable infiltration capacity or ratio of desalinization.
RO reverse osmosis membrane can be placed in pressurized vessel, and when high flow rate, the mode flowing through membrane element by the cleaning water of circulation (RO product water or not containing the clean water of free chlorine) is cleaned.The wash procedure of RO reverse osmosis membrane depends on particular case completely, changes the cleaning water for circulating if desired.The conventional wash procedure of RO reverse osmosis membrane is as follows: under 0.4MPa or power condition at low pressure, carry out low-pressure washing, namely in pressurized vessel, pumps into cleaning water from (or suitable water source) purge tank and then emits, and runs several minutes.Wash-down water must be clean, removal hardness, the RO product water not containing transition metal and chlorine residue or deionized water.Specific cleaning solution is prepared in purge tank.Preparation water must be remove hardness, the RO product water not containing transition metal and chlorine residue or deionized water.Temperature and pH should be transferred to required value.Starting scavenging pump pumps in membrane module by scavenging solution, wash cycles about a hour or the time required.At initial period, before scavenging solution is back to RO purge tank, initial phegma is emitted, in order to avoid the water be detained in system causes dilution to cleaning solution.In initial 5 minutes, at leisure by flow rate regulation to 1/3 of design maximum flow velocity.This can reduce the potential dirt caused by a large amount of deposition of dirt and block up.At second in 5 minutes, increase flow velocity to 2/3 of design maximum flow velocity, then, then increase the Peak Flow Rate value of flow velocity to design.If needed, when the change of pH is greater than 1, will again adjust back to former numerical value.As required, wash cycles and immersion program can alternately be adopted.Soak time suggestion selection 1 to 8 hour.Suitable temperature and pH value to be kept modestly.After matting terminates, low-pressure washing is carried out by cleaning water (removing hardness, non-metal ion as the RO product water of iron and chlorine or deionized water), the lingering section of chemical agent is removed from washing unit/parts, discharge and rinse purge tank, and then filling purge tank completely to be used as to rinse by cleaning water.All wash-down water flushing pressure containers are pumped into discharge from purge tank.If needed, second time cleaning can be carried out.Once after RO system rinses completely by the cleaning water in water storing tank, carry out final low-pressure washing with regard to available pre-treating feed water.Feed pressure should lower than 0.4MPa, and final flushing continues to carry out until wash-down water is clean, and not containing any foam and clean-out system resistates.Usually this needs 15 ~ 60 minutes.Operator can sample with clean flask, shake up, the residual condition of washing composition and foam in monitoring discharge outlet place wash-down water.
Embodiment 2
On the basis of embodiment 1, need water to be pumped in RO reverse osmosis membrane 3 at motor-mount pump 4, because needing the water pumped into be surface water, there is a large amount of impurity, as to these impurity not advanced processing, this impurity enters in motor-mount pump 4 or RO reverse osmosis membrane 3, damage is brought to motor-mount pump 4 or RO reverse osmosis membrane 3, the present embodiment adopts in source water inlet 7 and is provided with filtering net 6, before water enters into motor-mount pump 4, first by filtering net 6, filtration decon is carried out to it, then enter into motor-mount pump 4 and RO reverse osmosis membrane 3.
Embodiment 3
On the basis of embodiment 1, in order to motor-mount pump shell 2 and RO reverse osmosis membrane 1 shell can be dismantled smoothly, the convenient cleaning to RO reverse osmosis membrane 3, motor-mount pump shell 2 is connected by screw thread or buckle with RO reverse osmosis membrane 1 shell.
Implement 4
On the basis of embodiment 1, conveniently carry, and make the weight ratio of this anti-penetration water purifier lower, described motor-mount pump shell 2 is provided with battery compartment 8, be provided with battery 9 in this battery compartment 8, described battery 9 is electrically connected with motor-mount pump 4, and described motor-mount pump 4 is 12V DC electropump.If when needing this water purifier there is no an electricity in the process worked, open battery compartment 8 and change battery 9, in the process of work, controlled the working order of motor-mount pump 4 by the switch be connected between battery 9 and motor-mount pump 4.
More than exemplifying is only illustrate of the present utility model, does not form the restriction to protection domain of the present utility model, everyly all belongs within protection domain of the present utility model with the same or analogous design of the utility model.
Claims (6)
1. a field emergency anti-penetration water purifier, is characterized in that, comprises a RO reverse osmosis membrane (3), RO reverse osmosis membrane shell (1), motor-mount pump (4), motor-mount pump shell (2);
Described RO reverse osmosis membrane (3) is located in RO reverse osmosis membrane shell (1), the sewage draining exit (10) of described RO reverse osmosis membrane (3) and the first row mouth of a river (11) of RO reverse osmosis membrane shell (1), pure water outlet (13) of RO reverse osmosis membrane (3) is connected respectively by pipeline with the second row mouth of a river (12) of RO reverse osmosis membrane shell (1), described motor-mount pump (4) is located in motor-mount pump shell (2), described motor-mount pump shell (2) is connected to the below of RO reverse osmosis membrane shell (1), and the water outlet of described motor-mount pump (4) is connected with the water inlet (5) of RO reverse osmosis membrane (3), the source water inlet (7) that water-in and motor-mount pump shell (2) bottom of described motor-mount pump (4) are provided with is connected, described motor-mount pump (4) is connected with the power electric be provided with outside motor-mount pump shell (2).
2. a kind of field emergency anti-penetration water purifier according to claim 1, is characterized in that, is provided with filtering net (6) in described source water inlet (7).
3. a kind of field emergency anti-penetration water purifier according to claim 1, is characterized in that, described RO reverse osmosis membrane shell (1) and described motor-mount pump shell (2) are threaded connection.
4. a kind of field emergency anti-penetration water purifier according to claim 1, is characterized in that, described RO reverse osmosis membrane shell (1) is connected by buckle with described motor-mount pump shell (2).
5. a kind of field emergency anti-penetration water purifier according to claim 1, it is characterized in that, described motor-mount pump shell (2) is provided with battery compartment (8), is provided with battery (9) in this battery compartment (8), and described battery (9) is electrically connected with motor-mount pump (4).
6. a kind of field emergency anti-penetration water purifier according to claim 1 or 5, it is characterized in that, described motor-mount pump (4) is 12V DC electropump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520674821.3U CN204939036U (en) | 2015-09-02 | 2015-09-02 | A kind of field emergency anti-penetration water purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520674821.3U CN204939036U (en) | 2015-09-02 | 2015-09-02 | A kind of field emergency anti-penetration water purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204939036U true CN204939036U (en) | 2016-01-06 |
Family
ID=55006479
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520674821.3U Expired - Fee Related CN204939036U (en) | 2015-09-02 | 2015-09-02 | A kind of field emergency anti-penetration water purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204939036U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109665650A (en) * | 2019-03-04 | 2019-04-23 | 河北首力科技有限公司 | The dual-purpose water purifier of portable lithium electricity |
-
2015
- 2015-09-02 CN CN201520674821.3U patent/CN204939036U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109665650A (en) * | 2019-03-04 | 2019-04-23 | 河北首力科技有限公司 | The dual-purpose water purifier of portable lithium electricity |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2606599C2 (en) | Method and system for water treatment used for industrial purposes | |
| CN101481182B (en) | Reverse osmosis water production apparatus, water production method, and method for cleaning and maintaining reverse osmosis water production apparatus | |
| CN202358976U (en) | Glass wastewater treatment equipment | |
| CN203820606U (en) | Purification system for deep treatment of tap water | |
| CN201330179Y (en) | Reverse osmosis water production equipment | |
| CN105906086B (en) | A kind of the drinking water advanced treatment system and technique of short route | |
| CN110156275A (en) | A kind of environmentally friendly recirculated water by-pass flow biological treatment system and method | |
| CN202643477U (en) | Drinking water treatment device | |
| CN204588956U (en) | A kind of low turbidity micro-polluted surface water advanced treatment apparatus | |
| CN104118947B (en) | A kind of method of antibiotic waste water advanced treatment and reuse | |
| CN205850604U (en) | The full-automatic device for making of urea for vehicle solution | |
| CN204939036U (en) | A kind of field emergency anti-penetration water purifier | |
| CN102380252B (en) | Backwashing water discharge reduction method of tow filter | |
| CN204999657U (en) | Open -air emergent manual reverse osmosis water purifier | |
| CN110330140A (en) | Saline and alkaline region water pollution improvement and system for regenerating and recycling and method | |
| CN203582663U (en) | Reclaimed water reuse system applied to domestic sewage treatment | |
| CN203021404U (en) | Biochemical wastewater treatment device | |
| CN115159739A (en) | Reverse osmosis seawater desalination system | |
| CN1344690A (en) | Water treating method and treater for producing pure health water | |
| CN205740556U (en) | A kind of brackish water desalination system utilizing dense water to carry out backwash | |
| CN204079651U (en) | Removal of Fluorine From Underground Water and regeneration system rapidly | |
| CN205874128U (en) | Dyeing and finishing waste water treatment and retrieval and utilization device | |
| CN203095802U (en) | Island direct drinking water process integrated equipment | |
| CN101549931B (en) | Process for treating drinking water | |
| CN113336374B (en) | Mariculture wastewater treatment device and process |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160106 Termination date: 20160902 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |