CN104230069B - A kind of direct drinking is processed skid mounted equipment - Google Patents
A kind of direct drinking is processed skid mounted equipment Download PDFInfo
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- CN104230069B CN104230069B CN201410372013.1A CN201410372013A CN104230069B CN 104230069 B CN104230069 B CN 104230069B CN 201410372013 A CN201410372013 A CN 201410372013A CN 104230069 B CN104230069 B CN 104230069B
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Abstract
The present invention relates to a kind of direct drinking and process skid mounted equipment, comprise power plant module, water module and purified treatment module, purified treatment module comprises the coarse filtration unit, micro-filtration unit, preposition activated charcoal unit, ultra filtration unit, nano-filtration unit, ultraviolet sterilization unit, ozonization unit, post active carbon unit and the heating unit that connect successively; Power plant module provides power for water module and purified treatment module. Direct drinking provided by the invention is processed skid mounted equipment, and clean water treatment amount is large, and purifying water effect is good, and sterilization effect is good, and the earth surface water source obtaining can directly become safe domestic water, direct drinking or high-concentration ozone water and warm water after this device is processed.
Description
Technical field
The present invention relates to a kind of direct drinking and process skid mounted equipment.
Background technology
At some in particular cases, for example natural calamity or burst Pollution event, the water source that causes people to depend on for existence is contaminated, then due to rugged environment factor etc., cause obtaining of direct drinking very difficult, this brings great hidden danger to life security of people. Therefore, how these are in particular cases directly prepared into direct drinking and become the emphasis of people's research in contaminated water source.
Summary of the invention
Given this, be necessary to obtain very difficult problem for direct drinking in particular cases, provide a kind of direct drinking to process skid mounted equipment.
Technical scheme of the present invention is:
A kind of direct drinking is processed skid mounted equipment, comprise power plant module, water module and purified treatment module, purified treatment module comprises coarse filtration unit, micro-filtration unit, preposition activated charcoal unit, ultra filtration unit, nano-filtration unit, ultraviolet sterilization unit, ozonization unit, post active carbon unit, heating unit; In described water module and purified treatment module, coarse filtration unit, micro-filtration unit, preposition activated charcoal unit, ultra filtration unit, nano-filtration unit, ultraviolet sterilization unit, ozonization unit, post active carbon unit, heating unit are communicated with successively by pipeline, and power plant module provides power for water module and purified treatment module.
Described water module has back washing anti-blocking plug function, described coarse filtration unit comprises one-level rough filtering component and secondary rough filtering component, described one-level rough filtering component comprises water pump and screen pack, described secondary rough filtering component comprises revolving filter, one-level rough filtering component has back washing anti-blocking plug function, secondary rough filtering component has automatic backwash anti-blockage function, it is large that one-level rough filtering component filters size ratio secondary rough filtering component filtration particle diameter, micro-filtration unit comprises one-level micro-filtration assembly and secondary micro-filtration assembly, and it is large that one-level micro-filtration assembly filters size ratio secondary micro-filtration assembly filtration particle diameter.
The first water storage element that is provided for rinsing micro-filtration unit, ultra filtration unit, nano-filtration unit after described ultra filtration unit, this water storage element is provided with water return pipeline, realizes micro-filtration unit, ultra filtration unit are carried out to pressure back flushing, and nano-filtration unit is just rinsed; Described pressure back flushing is set to move 30 minutes, backwash 3 minutes, and back washing strength is set to 1.2-2 times of this unit operating flux. Behind described nano-filtration unit and ozonization unit, second, third water storage element is set respectively, the water in each water storage element can be directly for or drink.
The container that comprises active carbon and dress active carbon in described preposition activated charcoal unit, it is interval large that active carbon has aperture size, can adsorb larger and less particulate matter simultaneously, and the specific area of active carbon is large, can adsorb a large amount of particulate matters.
Described ultra filtration unit comprises some ultrafiltration membrane filters, and the filtering accuracy of described ultrafiltration membrane filter is 0.01um.
Described nano-filtration unit comprises some nano-filtration membrane filters, and the filtering accuracy of described nano-filtration membrane filter is 0.001um.
Described water module comprises water intaking assembly for extracting water source and for tackling the floating thing of water and the filter assemblies of particle, described filter assemblies surrounds this water intaking assembly, and described water module has backwashing function.
Described filter assemblies comprises the fence of filter screen and this filter screen of encirclement, and the filtration particle diameter of this filter screen is less than the filtration particle diameter of this fence.
Described water module also comprises fixation kit, and this fixation kit is connected with this water intaking assembly and for fixing the position of this water intaking assembly at water.
Described disinfection by ultraviolet light unit comprises that wave-length coverage is the uviol lamp of 254-257nm and the airtight container of dress uviol lamp. uviol lamp is contained in airtight container.
Described ozonization unit comprises ozone generator, gas-liquid mixing pump and stop valve.
Described post active carbon unit comprises the container of active carbon and dress active carbon, and active carbon has the effect that improves mouthfeel, removes peculiar smell, removes colourity, adsorb organic compound and bromate.
The invention has the beneficial effects as follows: this direct drinking water treatment system, clean water treatment amount is large, and purifying water effect is good, and sterilization effect is good, and the earth surface water source obtaining can directly become safe domestic water, direct drinking after this device is processed. high-concentration ozone water and warm water.
Brief description of the drawings
Fig. 1 is the theory of constitution schematic block diagram Part I of equipment of the present invention;
Fig. 2 is the theory of constitution schematic block diagram Part II of equipment of the present invention.
Fig. 3 is the structure chart Part I of apparatus embodiments of the present invention;
Fig. 4 is the structure chart Part II of apparatus embodiments of the present invention.
Detailed description of the invention
Understand technology contents of the present invention for convenience of those skilled in the art, below in conjunction with drawings and Examples, the present invention is described in further detail.
As Figure 1-4, the processing of the direct drinking described in the present embodiment skid mounted equipment comprises power plant module, water module and purified treatment module. Wherein, purified treatment module comprises the coarse filtration unit 1, micro-filtration unit 2, preposition activated charcoal unit 3, ultra filtration unit 4, nano-filtration unit 5, ultraviolet sterilization unit 6, ozonization unit 7, post active carbon unit 8 and the heating unit 9 that connect successively. Heating unit is optional module.
Wherein, power plant module can adopt vehicle, provides electric power for traction direct drinking water treating equipment and to these equipment.
Water module is water intaking filter in the present embodiment, can adopt submersible sewage pump and be arranged on submersible sewage pump screen pack and grid around. Submersible sewage pump can be torn the materials such as the long fibre in sewage, bag, band, grass, cloth, cut off, then discharge smoothly. Grid is used for holding back the thick dirt of sewage, for by particle diameter, the impurity more than 80 orders excludes. In fact water module is similar or identical with the one-level rough filtering component in coarse filtration unit, just filtering accuracy difference.
Coarse filtration unit 1 comprises one-level rough filtering component 12 and secondary rough filtering component 14, one-level rough filtering component comprises water pump and is arranged on water pump screen pack around, secondary rough filtering component comprises automatic backwashing filter, can adopt existing ripe equipment on the market or it is done to suitable improvement. Can certainly adopt special equipment, but this link if adopt there is the equipment of automatic back-flushing function should be in this patent protection domain. Firsts and seconds rough filtering component all has back washing anti-blocking plug function, and it is large that one-level rough filtering component filtration size ratio secondary rough filtering component filters particle diameter, and one-level rough filtering component is for selecting arrangement, and part situation can be omitted need not.
The filtering accuracy of the automatic backwash revolving filter 14 that secondary rough filtering component adopts is traditionally arranged to be 30 ~ 50 μ m. Through water module, the pretreated water of one-level rough filtering component, undertaken after coarse filtration by revolving filter 14, the impurity particle diameter that can realize in water is no more than 50 μ m.
In the present embodiment, micro-filtration unit 2 also adopts the two-stage micro-filtration assembly connecting successively. One-level micro-filtration assembly adopts the cotton filter 20 of PP, secondary micro-filtration assembly to adopt the cotton filter 22 of PP. The cotton filter 20 of PP is communicated with revolving filter 14. The filtering accuracy of the cotton filter of one-level PP is 1 μ m. The filtering accuracy of the cotton filter of secondary PP is 0.1 μ m. The water of crossing through revolving filter 14 coarse filtration, after using micro-filtration assembly to filter, the impurity particle diameter in water is no more than 0.1 μ m.
In other embodiments, micro-filtration unit can comprise the micro-filtration assembly of multiple parallel connections, and each micro-filtration assembly comprises the cotton filter of the one-level PP being communicated with successively, the cotton filter of secondary PP, and the cotton filter of one-level PP of each micro-filtration assembly is all communicated with revolving filter. Becoming multiply to carry out essence filter the moisture after revolving filter coarse filtration, avoided under complex environment, easily there is the problem of stopping up, the stability of intensifier and service life in fine filtering device.
Further, each micro-filtration unit also comprises stop valve, and the cotton filter 20 of one-level PP of each micro-filtration unit is communicated with revolving filter 14 by stop valve. Open when the stop valve of one of them micro-filtration assembly of multiple micro-filtrations unit, when the stop valve of other micro-filtration assemblies is closed, micro-filtration unit is in singly opening state. Open when the wherein stop valve of two micro-filtration assemblies of multiple micro-filtration assemblies, when the stop valve of other micro-filtration assemblies is closed, micro-filtration unit is in two states of opening. By regulating the switch of stop valve of each micro-filtration assembly, can realize singly the opening of fine filtering device, twoly open or open more, facilitate adjust flux to carry out essence filter.
Behind micro-filtration unit, connect preposition activated carbon filter 3, all connect a charcoal filter after each micro-filtration assembly, clean-up effect is better. The filtering accuracy of active carbon filter is 0.1 μ m. This unit adopts coal mass active carbon, and it utilizes the specific area of coal mass active carbon large, can adsorb the characteristic of a large amount of particulate matters, can adsorb larger and less particulate matter simultaneously, realizes and filters object.
Ultra filtration unit 4 can comprise multiple ultrafiltration apparatus 42, also can be only with a ultrafiltration apparatus, and the output of filtered water single channel, nano-filtration unit coordinates the quantity correspondence of ultra filtration unit that nanofiltration device 44 is set. Ultrafiltration apparatus adopts ultrafiltration membrane filter. The filtering accuracy of ultrafiltration apparatus is 0.01 μ m. After the water of micro-filtration unit essence filter collects, carry out ultrafiltration by ultrafiltration apparatus, the impurity particle diameter in the water after ultrafiltration is no more than 0.01 μ m.
In the present embodiment, above-mentioned direct drinking water treating equipment also comprises storage tank 46. Storage tank 46 is for carrying out nanofiltration by cushioning to be delivered to nanofiltration device 44 through the water of ultrafiltration apparatus 42 ultrafiltration, and the impurity particle diameter after nanofiltration in water is no more than 0.001 μ m. Or be delivered to ultrafiltration apparatus 42 as backwash water, and prevent that ultrafiltration apparatus 42 from stopping up, reduce ultrafiltration apparatus 42 two ends pressure reduction.
Be appreciated that storage tank 46 can omit. After carrying out ultrafiltration by ultrafiltration apparatus 42 after the water of micro-filtration unit essence filter collects, directly carry out nanofiltration by nano-filtration unit 5 again, the impurity particle diameter in water is no more than 0.001 μ m. Nano-filtration unit 5 adopts multistage nano-filtration membrane filter.
In the present embodiment, above-mentioned direct drinking water treating equipment also comprises ultraviolet disinfection storage tank 6. Ultraviolet disinfection storage tank 6 two ends are communicated with ozonateur 7 and nano-filtration unit 5. Ultraviolet disinfection storage tank 6 is for cushioning through the water of nano-filtration unit 5 nanofiltrations and ultraviolet disinfection carries out ozonization to be delivered to ozonateur 7. Or be delivered to nanofiltration device 44 as positive wash water.
The water of ultraviolet disinfection storage tank 6 through the water of nano-filtration unit 5 nanofiltrations cushion and ultraviolet disinfection after can be used as domestic water.
Be appreciated that ultraviolet disinfection storage tank 6 can omit. Water through nano-filtration unit 5 nanofiltrations can directly carry out using after ozonization through ozonateur 7. Or ultraviolet disinfection storage tank 6 and ozonateur 7 positions are interchangeable.
Post active carbon unit 8 adopts cocoanut active charcoal adsorption instrument, and this kind of active carbon has the effect that improves mouthfeel, removes peculiar smell, removes colourity, adsorb organic compound and bromate. Cocoanut active charcoal adsorption instrument is communicated with ozonateur 7, and the bromic acid salts substances producing for removing ozonization process, obtains direct drinking.
In the present embodiment, above-mentioned direct drinking water treating equipment also comprises ozone storage tank 70. Ozone storage tank 70 is communicated with ozonateur 7 and charcoal absorption instrument. Ozone storage tank 70 is removed ozone after the water of sterilizing through ozonateur 7 being cushioned to be delivered to the absorption of charcoal absorption instrument, obtains direct drinking; Or can directly export and drink.
Ozone storage tank 70 is for cushioning through the water of ozonateur sterilization using as disinfectant.
Be appreciated that ozone storage tank 70 can omit. The water of sterilizing through ozonateur directly, after charcoal absorption instrument adsorbs, is removed the bromic acid salts substances of the inside, obtains direct drinking.
In other embodiments, can also be communicated with heater 9 after charcoal absorption instrument, for heating direct drinking, directly be drunk warm water. Heater can adopt has rapid heating function, and normal-temperature water reaches more than 90 degrees Celsius to heating unit delivery port temperature after by heating unit, directly for drinking.
Be appreciated that through the sewage of the cotton filtration of one-level PP, ultra filtration unit ultrafiltration or nano-filtration unit nanofiltration, all reached discharge standard, can be directly emptying.
When concrete enforcement, the filtration pressure control of the cotton filter of one-level PP is 0.6 ~ 1.6MPa, and temperature is 5 ~ 35 DEG C. The filtration pressure of the cotton filter of secondary PP is 1 ~ 1.6MPa, and temperature is 5 ~ 35 DEG C. The filtration pressure of active carbon filter is 0.6 ~ 1.6MPa, and temperature is 5 ~ 35 DEG C. The ultrafiltration pressure of ultrafiltration apparatus is 0.05-0.3MPa, and temperature is 5 ~ 35 DEG C. The nanofiltration pressure of nanofiltration device is 0.5-0.8MPa, and temperature is 5 ~ 35 DEG C.
Above-mentioned direct drinking water treating equipment, simple in structure, by water intaking filter, automatic backwash revolving filter, micro-filtration unit, ultrafiltration and the nano-filtration unit, disinfection unit and the charcoal absorption instrument that are communicated with successively, by eliminations such as the earth in sewage, general impurity, bacterium, viruses, the direct drinking of producing completely meets and drinks requirement. In addition, adopt multiple essence filters unit to be communicated with side by side, avoided under complex environment, easily there is the problem of stopping up in fine filtering device, has strengthened stability and the service life of device.
Above-described embodiment is only wherein specific implementation of the present invention, and it describes comparatively concrete and detailed, but can not therefore be interpreted as the restriction to the scope of the claims of the present invention. It should be pointed out that for the person of ordinary skill of the art, without departing from the inventive concept of the premise, can also make some distortion and improvement, these apparent replacement forms all belong to protection scope of the present invention.
Claims (8)
1. direct drinking is processed a skid mounted equipment, it is characterized in that, comprises power plant module, water module and purified treatment module, described inPurified treatment module comprises that coarse filtration unit, micro-filtration unit, preposition activated charcoal unit, ultra filtration unit, nano-filtration unit, ultraviolet ray killBacterium unit, ozonization unit, post active carbon unit; Coarse filtration unit in described water module and purified treatment module, micro-Filter unit, preposition activated charcoal unit, ultra filtration unit, nano-filtration unit, ultraviolet sterilization unit, ozonization unit, rearmounted livingProperty charcoal unit is communicated with successively by pipeline, and power plant module provides operation power for water module and purified treatment module;
Described water module comprises water intaking assembly for extracting water source and for tackling the floating thing of water and the filter assemblies of particle, instituteState filter assemblies and surround this water intaking assembly; Also comprise fixation kit, this fixation kit is connected with this water intaking assembly and is somebody's turn to do for fixingThe position of water intaking assembly in water;
Described filter assemblies comprises the fence of filter screen and this filter screen of encirclement, and the filtration particle diameter of this filter screen is less than the filtration particle diameter of this fence.
2. water treatment skid mounted equipment according to claim 1, is characterized in that, described coarse filtration unit comprises one-level rough filtering componentWith secondary rough filtering component, described one-level rough filtering component comprises water pump and is located at water pump screen pack around, described secondary rough filtering componentComprise automatic backwashing filter; Described micro-filtration unit comprises one-level micro-filtration assembly and secondary micro-filtration assembly, one-level micro-filtration assembly mistakeIt is large that filter size ratio secondary micro-filtration assembly filters particle diameter.
3. water treatment skid mounted equipment according to claim 1, is characterized in that, is provided for rinsing micro-after described ultra filtration unitThe first water storage element of filter unit, ultra filtration unit, nano-filtration unit, this water storage element is provided with water return pipeline, realizes micro-filtration listUnit, ultra filtration unit are carried out pressure back flushing, and nano-filtration unit is just rinsed; Described pressure back flushing is set to move 30 pointsClock, backwash 3 minutes, back washing strength is set to 1.2-2 times of this unit operating flux.
4. direct drinking according to claim 1 is processed skid mounted equipment, it is characterized in that, described preposition activated charcoal comprises in unitActive carbon and for the container of splendid attire active carbon, this active carbon adopts coal mass active carbon;
Described post active carbon unit comprises active carbon and the container for splendid attire active carbon, and this active carbon adopts active fruit shell carbon.
5. direct drinking according to claim 1 is processed skid mounted equipment, it is characterized in that, described ultra filtration unit comprises some ultrafiltrationFilm filter, the filtering accuracy of described ultrafiltration membrane filter is 0.01um.
6. direct drinking according to claim 1 is processed skid mounted equipment, it is characterized in that, described nano-filtration unit comprises some nanofiltrationsFilm filter, the filtering accuracy of described nano-filtration membrane filter is 0.001um.
7. water treatment skid mounted equipment according to claim 1, is characterized in that, behind described nano-filtration unit and ozonization unitSecond, third water storage element is set respectively, the water in each water storage element can be directly for or drink.
8. water treatment skid mounted equipment according to claim 1, is characterized in that, described disinfection by ultraviolet light unit comprises wavelength modelEnclosing is the uviol lamp of 254-257nm; Described uviol lamp is installed in airtight container;
Described ozonization unit comprises interconnective ozone generator, gas-liquid mixing pump, on described gas-liquid mixing pump, establishes stop valve.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201410372013.1A CN104230069B (en) | 2014-07-31 | 2014-07-31 | A kind of direct drinking is processed skid mounted equipment |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201410372013.1A CN104230069B (en) | 2014-07-31 | 2014-07-31 | A kind of direct drinking is processed skid mounted equipment |
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| CN104230069A CN104230069A (en) | 2014-12-24 |
| CN104230069B true CN104230069B (en) | 2016-05-18 |
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Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106186388B (en) * | 2015-04-29 | 2019-09-20 | 杭州超纳净水设备有限公司 | A kind of membrane type household water filter |
| CN106467336A (en) * | 2015-08-17 | 2017-03-01 | 深圳市明鑫高分子技术有限公司 | Water purification installation and method for purifying water |
| CN105152428A (en) * | 2015-08-26 | 2015-12-16 | 惠州市泰林科技有限公司 | Skid-mounted emergency water service treatment system |
| CN105236642A (en) * | 2015-11-13 | 2016-01-13 | 天津市振津石油天然气工程有限公司 | Fluorine-containing drinking water treatment method and skid-mounted device |
| CN107792975A (en) * | 2016-09-05 | 2018-03-13 | 康师傅饮品控股有限公司 | Remove the method and device of ferrimanganic in drinking water |
| CN107055895A (en) | 2017-06-16 | 2017-08-18 | 云南大学 | The vertical plug-flow photocatalysis treatment of waste water skid mounted equipment of diffusion in a kind of upper cloth stream |
| CN109534564B (en) * | 2018-12-04 | 2019-10-08 | 朴成淑 | A kind of natural selenium-rich water filtration method |
| CN110092517A (en) * | 2019-06-12 | 2019-08-06 | 苏州普滤得净化股份有限公司 | A kind of sanitation-grade drinking water purification system |
| CA3145046A1 (en) * | 2019-06-28 | 2020-12-30 | Grafoid Inc. | Graphene based filters and systems comprising same |
| CN112479466A (en) * | 2020-12-17 | 2021-03-12 | 苏州国净净化科技有限公司 | Direct water dispenser and control method thereof |
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| CN101948190A (en) * | 2010-09-06 | 2011-01-19 | 杭州浙华水务有限公司 | Field emergency water treatment equipment |
| CN202988906U (en) * | 2012-12-31 | 2013-06-12 | 北京净道科技有限公司 | Vehicle-mounted movable and direct emergency drinking water equipment |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN203959975U (en) * | 2014-07-31 | 2014-11-26 | 惠州市泰林科技有限公司 | A kind of direct-drinking water is processed skid mounted equipment |
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6416668B1 (en) * | 1999-09-01 | 2002-07-09 | Riad A. Al-Samadi | Water treatment process for membranes |
| CN101948190A (en) * | 2010-09-06 | 2011-01-19 | 杭州浙华水务有限公司 | Field emergency water treatment equipment |
| CN202988906U (en) * | 2012-12-31 | 2013-06-12 | 北京净道科技有限公司 | Vehicle-mounted movable and direct emergency drinking water equipment |
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