CN203639256U - Mobile membrane water treatment technology platform - Google Patents
Mobile membrane water treatment technology platform Download PDFInfo
- Publication number
- CN203639256U CN203639256U CN201320763670.XU CN201320763670U CN203639256U CN 203639256 U CN203639256 U CN 203639256U CN 201320763670 U CN201320763670 U CN 201320763670U CN 203639256 U CN203639256 U CN 203639256U
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- Prior art keywords
- water
- filter
- pump
- reverse osmosis
- pressure pump
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- 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 - Lifetime
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 189
- 239000012528 membrane Substances 0.000 title claims abstract description 35
- 238000005516 engineering process Methods 0.000 title claims abstract description 22
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 50
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 34
- 238000000034 method Methods 0.000 claims description 25
- 239000002455 scale inhibitor Substances 0.000 claims description 14
- 230000001681 protective effect Effects 0.000 claims description 11
- 230000001105 regulatory effect Effects 0.000 claims description 8
- 238000009434 installation Methods 0.000 abstract description 6
- 239000003344 environmental pollutant Substances 0.000 abstract description 2
- 231100000719 pollutant Toxicity 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract 3
- 238000005345 coagulation Methods 0.000 description 4
- 230000015271 coagulation Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 238000011010 flushing procedure Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 239000000084 colloidal system Substances 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- ZFXVRMSLJDYJCH-UHFFFAOYSA-N calcium magnesium Chemical compound [Mg].[Ca] ZFXVRMSLJDYJCH-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000003403 water pollutant Substances 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
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- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The utility model discloses a mobile membrane water treatment technology platform, comprising a raw water tank, a booster pump, a multi-medium filter, an activated carbon filter, a precision filter, a high-pressure pump, a reverse osmosis membrane device and a water production tank, wherein a water inlet of the raw water tank is connected with a raw water source and a raw water electric valve; a water outlet of the raw water tank is connected with the water inlet of the booster pump; the water outlet of the booster pump is connected with the water inlet of the multi-medium filter; the water outlet of the multi-medium filter is connected with the water inlet of the activated carbon filter; the water outlet of the activated carbon filter is connected with the water inlet of the precision filter; the water outlet of the precision filter is connected with the water inlet of the reverse osmosis membrane device through the high-pressure pump; and the water production outlet of the reverse osmosis membrane device is connected with the water inlet of the water production tank. The mobile membrane water treatment technology platform is high in automatic control degree, quick installation can be achieved, the produced water quality is not affected by an external environment basically, and pollutants in the water can be effectively removed.
Description
Technical field
The utility model relates to water technology platform, specifically, relates to a kind of portable embrane method water technology platform.
Background technology
At present, in the wild, the place such as boats and ships, working-yard, suburb, mining area, Scenic Spots, due to distant from waterworks, great majority can not connect municipal tap water pipeline, and because its water consumption is less, be equipped with large-scale water purifying plant and can cause again the waste in resource.Like this, generally the water source in above-mentioned area is adopted to miniature water treatment facility, more typical traditional water technology platform is in former water suction, to carry out coagulation, precipitation, filtration, sterilization etc., but this technique platform has the following disadvantages:
1. each unit for treating water needs on-the-spot installation, and assembling cycle generally, about 7 days, is difficult to reach and send the i.e. effect of use;
2. coagulation, precipitation, filtered water processing unit all need necessarily to take up an area space, and occupation area of equipment is larger;
3. because coagulation, precipitation all need the reaction times of growing, the product water cycle is long;
4. while raining heavily, raw water turbidity raise, affect coagulation effect, and the water of clarifying in settling tank also can become muddiness, affected greatly by extraneous factor;
5. rivers water source heavy contamination nowadays, heavy metal, organism equal size are higher, and this technique platform is to this type of Pollutant Treatment poor effect.
Utility model content
To be solved in the utility model be the few regional traditional water technology platform of remote people producing water property consuming time, take up an area spatiality, be subject to ectocine, installation period, remove the technical problem of the aspect Shortcomings such as contaminative, provide a kind of can Fast Installation, portable embrane method water technology platform that floor space is little, can produce rapidly water, produce water water quality and be not substantially affected by the external environment and can effectively remove water pollutant.
In order to solve the problems of the technologies described above, the utility model is achieved by following technical scheme:
A kind of portable embrane method water technology platform, comprises former water tank, topping-up pump, more medium filter, activated charcoal filter, accurate filter, high-pressure pump, reverse osmosis membrane apparatus, product water tank, described former water tank water-in connects Yuan Shui water source by former water motorized valve, described former water tank water outlet connects the water-in of described topping-up pump, the water outlet of described topping-up pump connects the water-in of described more medium filter, the water outlet of described more medium filter connects the water-in of described activated charcoal filter, the water outlet of described activated charcoal filter connects the water-in of described accurate filter, the water outlet of described accurate filter connects the water-in of described reverse osmosis membrane apparatus by described high-pressure pump, the product mouth of a river of described reverse osmosis membrane apparatus connects the water-in of described product water tank,
On pipeline between the water outlet of described accurate filter and the water-in of described high-pressure pump, be provided with into tensimeter, low-voltage protective switch before water specific conductivity table, high-pressure pump pump, on the pipeline between the water outlet of described high-pressure pump and the water-in of described reverse osmosis membrane apparatus, be provided with into tensimeter after water motorized valve, inlet regulating valve, high-pressure pump vacuum breaker, high voltage protective switch, high-pressure pump pump;
On pipeline between the product mouth of a river and the water-in of described product water tank that described reverse osmosis dress film is put, be provided with and produce water conductivity table, produce water flowmeter, the concentrated water spout that described reverse osmosis dress film is put is connected with dense water regulating valve, rinses motorized valve, dense water pressure table, concentrated stream scale.
The water-in of described accurate filter is connected with scale inhibitor feeding device by pipeline, and described scale inhibitor feeding device comprises Scale inhibitors case and volume pump.
On pipeline between the water outlet of described topping-up pump and the water-in of described more medium filter, be provided with topping-up pump vacuum breaker.
Described more medium filter water-in one end, described activated charcoal filter water-in one end, described accurate filter water-in one end are all connected with tensimeter.
Described former water tank and described product water tank are respectively arranged with liquidometer.
The waste water of described former water tank, described more medium filter, described activated charcoal filter, described reverse osmosis membrane apparatus, described product water tank is all disposed to side bilge.
The beneficial effects of the utility model are:
(1) by low-voltage protective switch is installed in high-pressure pump water-in one end; water outlet one end installation high-voltage protection switch; in former water tank, product water tank, liquidometer is installed; the product water process of portable embrane method water technology platform is on the scene without staff; level of automation is high, has guaranteed stability and the security of operation.
(2) in whole portable embrane method water technology platform, adopt tensimeter, rate of flow meter, specific conductivity table to monitor in real time pressure, flow and the specific conductivity of each unit for treating water, facilitate entirety and local control of operations staff to membrane process craft platform, more medium filter, activated charcoal filter, accurate filter are installed before reverse osmosis membrane apparatus and are carried out pre-treatment, perfect on-line monitoring system and pretreatment system, effectively extend reverse osmosis membrane work-ing life, created high economic benefit.
(3) reverse osmosis membrane apparatus is in the time that long-time continuous is moved, the surface of reverse osmosis membrane can constantly be separated out and be attached to calcium magnesium plasma in water, form fouling and stop up fenestra, and scale inhibitor feeding device can automatic feeding Scale inhibitors, delay separating out and face fouling of calcium ions and magnesium ions, can prevent the damage of reverse osmosis membrane, effectively improve reverse osmosis membrane apparatus product water efficiency.
(4) by integrated design, successively topping-up pump, more medium filter, activated charcoal filter, accurate filter, reverse osmosis membrane apparatus are connected by pipeline, be arranged in stainless steel frame, can realize Fast Installation, meet the intensive requirement of portable embrane method water technology platform, convenient transportation, is easy to management.
Accompanying drawing explanation
Accompanying drawing is the structural representation of the portable embrane method water technology platform that provides of the utility model.
In figure: 1: pipeline, 2-1: former water tank liquidometer, 2-2: produce water tank liquidometer, 3: former water tank, 4: topping-up pump, 5-1: topping-up pump vacuum breaker, 5-2: high-pressure pump vacuum breaker, 6-1: more medium filter tensimeter, 6-2: activated charcoal filter tensimeter, 6-3: accurate filter tensimeter, 6-4: tensimeter before high-pressure pump pump, 6-5: tensimeter after high-pressure pump pump, 6-6: dense water pressure table, 7: more medium filter, 8: activated charcoal filter, 9: volume pump, 10: Scale inhibitors case, 11: accurate filter, 12-1: water inlet specific conductivity table, 12-2: produce water conductivity table, 13-1: low-voltage protective switch, 13-2: high voltage protective switch, 14: high-pressure pump, 15-1: former water motorized valve, 15-2: water inlet motorized valve, 15-3: rinse motorized valve, 16-1: inlet regulating valve, 16-2: dense water regulating valve, 17: reverse osmosis membrane apparatus, 18-1: concentrated stream scale, 18-2: produce water flowmeter, 19: produce water tank, 20: side bilge.
Embodiment
As shown in drawings, the present embodiment has disclosed a kind of portable embrane method water technology platform, comprises the former water tank 3, topping-up pump 4, more medium filter 7, activated charcoal filter 8, accurate filter 11, high-pressure pump 14, reverse osmosis membrane apparatus 17, the product water tank 19 that connect in turn by pipeline 1.
Former water tank 3 water-ins connect Yuan Shui water source, and on this connecting tube, are provided with former water motorized valve 15-1.The water outlet of former water tank 3 connects the water-in of topping-up pump 4, the water outlet of topping-up pump 4 connects the water-in of more medium filter 7, the water outlet of more medium filter 7 connects the water-in of activated charcoal filter 8, the water outlet of activated charcoal filter 8 connects the water-in of accurate filter 11, the water outlet of accurate filter 11 connects the water-in of reverse osmosis membrane apparatus 17 by high-pressure pump 14, the product mouth of a river of reverse osmosis membrane apparatus 17 connects the water-in that produces water tank 19.The water-in of accurate filter 11 is connected with scale inhibitor feeding device by pipeline 1, and scale inhibitor feeding device comprises Scale inhibitors case 10 and volume pump 9.
On pipeline 1 between the water-in of the water outlet of topping-up pump 4 and more medium filter 7, be provided with topping-up pump vacuum breaker 5-1.
Water-in one end of high-pressure pump 14 is connected with in turn into tensimeter 6-4, low-voltage protective switch 13-1 before water specific conductivity table 12-1, high-pressure pump pump, and water outlet one end of high-pressure pump 14 is connected with in turn into tensimeter 6-5 after water motorized valve 15-2, inlet regulating valve 16-1, high-pressure pump vacuum breaker 5-2, high voltage protective switch 13-2, high-pressure pump pump.
Reverse osmosis membrane apparatus 17 is provided with and produces the mouth of a river and concentrated water spout, produce one end, the mouth of a river and be connected with product water conductivity table 12-2 in turn, produce water flowmeter 18-2, concentrated water spout one end is connected with dense water regulating valve 16-2 in turn, rinses motorized valve 15-3, dense water pressure table 6-6, concentrated stream scale 18-1.
Former water tank 3, product water tank 19 are respectively arranged with former water tank liquidometer 2-1, produce water tank liquidometer 2-2.
The waste water of former water tank 3, more medium filter 7, activated charcoal filter 8, reverse osmosis membrane apparatus 17, product water tank 19 is all disposed to side bilge 20.
Brief description working process of the present utility model:
Produce water process: former water enters into former water tank 3 by pipeline 1, in the time that former water tank liquidometer 2-1 detects that former water water level arrives the highest liquid level, water inlet motorized valve 15-1 closes, and stops into water.Former water in former water tank 3, first via topping-up pump 4 pressurizations, successively enters in more medium filter 7, activated charcoal filter 8, accurate filter 11.By bed filtration effect, remove suspended substance in former water, mineral colloid, organic colloid, solvability organic polymer impurity etc.Water after cascade filtration is by the pressurization of high-pressure pump 14, the motorized valve 15-2 of simultaneously intaking opens, volume pump 9 starts, the Scale inhibitors that Scale inhibitors medicine-chest is 10 li and filtered water are mixed by reverse osmosis membrane apparatus 17, produce water and produce one end, mouth of a river inflow product water tank 19 water-ins from reverse osmosis membrane apparatus 17, dense water enters side bilge 20 from reverse osmosis membrane apparatus 17 concentrated water spout one end.
Flushing process: before each system closing and startup, all system is carried out to low-pressure washing process one time, rinse well remaining in the dense water of sending out in permeable membrane device 17.Detailed process is that former water in former water tank 3 is first via topping-up pump 4 pressurizations, successively enter in more medium filter 7, activated charcoal filter 8, accurate filter 11, intake simultaneously motorized valve 15-2, rinse motorized valve 15-3 and open, water after cascade filtration flows in reverse osmosis membrane apparatus 17, low-pressure washing is carried out in reverse osmosis membrane surface wherein, and wash-down water is drained in side bilge 20 from concentrated water spout one end through rinsing motorized valve 15-3.
Testing process: by reading the detected pressure value of tensimeter 6-5, dense water pressure table 6-6 after tensimeter 6-4 before more medium filter tensimeter 6-1, activated charcoal filter tensimeter 6-2, accurate filter tensimeter 6-3, high-pressure pump pump, high-pressure pump pump, once pressure reduction exceedes normal value, immediately movable type water treatment process platform is carried out to corresponding maintenance measure.Water inlet specific conductivity table 12-1 and product water conductivity table 12-2 can carry out on-line monitoring to water quality, can guarantee to produce water security and stability.Concentrated stream scale 18-1 and product water flowmeter 18-2 can the real-time Transmission water yield, conveniently statistics.
Automatically operational process: after the interior liquid level of product water liquidometer 2-2 detection product water tank 19 is not full water state, topping-up pump 4 starts, and the motorized valve 15-2 of simultaneously intaking, flushing motorized valve 15-3 open, rinse after 1-3 minute, open high-pressure pump 14, after several seconds, close and rinse motorized valve 15-3.After flushing motorized valve 15-3 closes, high voltage protective switch 13-2 and low-voltage protective switch 13-1 are detected.If high-voltage switch gear pressure superpressure, stops at once high-pressure pump 14 and allow system alarm, if low-tension switch pressure superpressure (too low) continue 1min, system alarm is also closed whole system.Detect after the interior full water of product water tank 19 when producing water tank liquidometer 2-2, stop successively high-pressure pump 14, topping-up pump 4 and water inlet motorized valve 15-1, volume pump 9.
Although preferred embodiment of the present utility model is described with preferred embodiment by reference to the accompanying drawings above; but the utility model is not limited to above-mentioned embodiment; above-mentioned embodiment is only schematic; be not restrictive; those of ordinary skill in the art is under enlightenment of the present utility model; do not departing from the scope situation that the utility model aim and claim protect; can also make the concrete conversion of a lot of forms, within these all belong to protection domain of the present utility model.
Claims (5)
1. a portable embrane method water technology platform, is characterized in that, comprises former water tank, topping-up pump, more medium filter, activated charcoal filter, accurate filter, high-pressure pump, reverse osmosis membrane apparatus, product water tank, described former water tank water-in connects Yuan Shui water source by former water motorized valve, described former water tank water outlet connects the water-in of described topping-up pump, the water outlet of described topping-up pump connects the water-in of described more medium filter, the water outlet of described more medium filter connects the water-in of described activated charcoal filter, the water outlet of described activated charcoal filter connects the water-in of described accurate filter, the water outlet of described accurate filter connects the water-in of described reverse osmosis membrane apparatus by described high-pressure pump, the product mouth of a river of described reverse osmosis membrane apparatus connects the water-in of described product water tank,
On pipeline between the water outlet of described accurate filter and the water-in of described high-pressure pump, be provided with into tensimeter, low-voltage protective switch before water specific conductivity table, high-pressure pump pump, on the pipeline between the water outlet of described high-pressure pump and the water-in of described reverse osmosis membrane apparatus, be provided with into tensimeter after water motorized valve, inlet regulating valve, high-pressure pump vacuum breaker, high voltage protective switch, high-pressure pump pump;
On pipeline between the product mouth of a river and the water-in of described product water tank that described reverse osmosis dress film is put, be provided with and produce water conductivity table, produce water flowmeter, the concentrated water spout that described reverse osmosis dress film is put is connected with dense water regulating valve, rinses motorized valve, dense water pressure table, concentrated stream scale.
2. the portable embrane method water technology of one according to claim 1 platform, is characterized in that, the water-in of described accurate filter is connected with scale inhibitor feeding device by pipeline, and described scale inhibitor feeding device comprises Scale inhibitors case and volume pump.
3. the portable embrane method water technology of one according to claim 1 platform, is characterized in that, on the pipeline between the water outlet of described topping-up pump and the water-in of described more medium filter, is provided with topping-up pump vacuum breaker.
4. the portable embrane method water technology of one according to claim 1 platform, is characterized in that, described more medium filter water-in one end, described activated charcoal filter water-in one end, described accurate filter water-in one end are all connected with tensimeter.
5. the portable embrane method water technology of one according to claim 1 platform, is characterized in that, described former water tank and described product water tank are respectively arranged with liquidometer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320763670.XU CN203639256U (en) | 2013-11-26 | 2013-11-26 | Mobile membrane water treatment technology platform |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320763670.XU CN203639256U (en) | 2013-11-26 | 2013-11-26 | Mobile membrane water treatment technology platform |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203639256U true CN203639256U (en) | 2014-06-11 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320763670.XU Expired - Lifetime CN203639256U (en) | 2013-11-26 | 2013-11-26 | Mobile membrane water treatment technology platform |
Country Status (1)
| Country | Link |
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| CN (1) | CN203639256U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104098199A (en) * | 2014-07-23 | 2014-10-15 | 江苏永尚能源科技有限公司 | Self-suction type household water purifier |
| CN105858934A (en) * | 2016-05-30 | 2016-08-17 | 张兆生 | Household sewage micro-purification device |
| CN106630225A (en) * | 2016-12-07 | 2017-05-10 | 珠海格力智能装备有限公司 | Drinking water production equipment and control method thereof |
| CN107746097A (en) * | 2017-09-29 | 2018-03-02 | 江苏科技大学 | A kind of reverse osmosis membrane and capacitance method desalinization combined system |
| CN108483701A (en) * | 2018-05-25 | 2018-09-04 | 宣化钢铁集团有限责任公司 | A kind of cooling water machine of conticaster magnetic stirrer |
| CN111018158A (en) * | 2019-12-25 | 2020-04-17 | 安徽元通水处理设备有限公司 | Fluorine removing equipment by membrane method |
| CN113830911A (en) * | 2021-10-11 | 2021-12-24 | 成都川力智能流体设备股份有限公司 | Direct drinking water treatment process with adjustable water quality |
-
2013
- 2013-11-26 CN CN201320763670.XU patent/CN203639256U/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104098199A (en) * | 2014-07-23 | 2014-10-15 | 江苏永尚能源科技有限公司 | Self-suction type household water purifier |
| CN105858934A (en) * | 2016-05-30 | 2016-08-17 | 张兆生 | Household sewage micro-purification device |
| CN105858934B (en) * | 2016-05-30 | 2018-11-09 | 山东好妯娌电器科技股份有限公司 | The micro- purifier of domestic sewage |
| CN106630225A (en) * | 2016-12-07 | 2017-05-10 | 珠海格力智能装备有限公司 | Drinking water production equipment and control method thereof |
| CN107746097A (en) * | 2017-09-29 | 2018-03-02 | 江苏科技大学 | A kind of reverse osmosis membrane and capacitance method desalinization combined system |
| CN108483701A (en) * | 2018-05-25 | 2018-09-04 | 宣化钢铁集团有限责任公司 | A kind of cooling water machine of conticaster magnetic stirrer |
| CN111018158A (en) * | 2019-12-25 | 2020-04-17 | 安徽元通水处理设备有限公司 | Fluorine removing equipment by membrane method |
| CN113830911A (en) * | 2021-10-11 | 2021-12-24 | 成都川力智能流体设备股份有限公司 | Direct drinking water treatment process with adjustable water quality |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140611 |