CN201182973Y - Full-automatic hyperfiltration water treatment apparatus - Google Patents
Full-automatic hyperfiltration water treatment apparatus Download PDFInfo
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- CN201182973Y CN201182973Y CNU2008200890554U CN200820089055U CN201182973Y CN 201182973 Y CN201182973 Y CN 201182973Y CN U2008200890554 U CNU2008200890554 U CN U2008200890554U CN 200820089055 U CN200820089055 U CN 200820089055U CN 201182973 Y CN201182973 Y CN 201182973Y
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Abstract
The utility model relates to a completely-automatic ultra-filtration water treatment plant, which mainly solves the problem that the automaticity of the prior water treatment plant is low. The completely-automatic ultra-filtration water treatment plant is characterized in that a water supplying pump (1) is connected in parallel with a hollow fiber ultra-filter diaphragm (8) through a water inlet pipeline (2) and an upper and a lower portal tracts (6, 7), a valve, a temperature sensor (3), a water inlet pneumatic valve (4) and a pressure sensor (5) are connected in series on the water inlet pipeline (2) in sequence, a portal tract (10) and the upper and the lower portal tracts (6, 7) are connected in parallel at the upper end of the hollow fiber ultra-filter diaphragm (8), and a water outlet pneumatic valve (9), a backwashing pneumatic valve (11), a backwashing pump (12), a backwashing pollution discharge pneumatic valve (13), a backwashing pressure sensor (14) and a flowmeter (15) are respectively connected in parallel at the inlet and outlet of the portal tract (10), and the inlet and outlet of the portal tract (10) are respectively connected with an automatic controlling device (16), and an air supplying device (17) is communicated with the outlet end of the upper and the lower portal tracts (6, 7). The completely-automatic ultra-filtration water treatment plant is characterized in that the completely-automatic controlling for the ultra-filtration water treatment plant is realized.
Description
Technical field:
The utility model relates to a kind of water treatment facilities, especially full-automatic ultrafiltration water treatment facilities.
Background technology:
Along with the developing water treating apparatus of society obtains extensively should.As the production of electroplating wastewater, textile waste, drinking water, the processing of oily waste water.But major part is still used traditional filter on oil-contaminated water of oil field is handled at present.Its shortcoming is that equipment volume is big, automaticity is low, backwashing manner is too single and the low problem of utilization rate water, handles the back shipwreck with up to standard.Its equipment is difficult to promote.
The utility model content:
Existing water treatment facilities equipment volume is big, automaticity is low, backwashing manner is too single and the low problem of utilization rate water in order to solve, the utility model provides a kind of full-automatic ultrafiltration water treatment facilities, and this full-automatic ultrafiltration water treatment facilities has realizes that Automatic Control, structure are compact more, cleaning performance reaches the stable characteristics of producing water water quality well.
The technical solution of the utility model is: this full-automatic ultrafiltration water treatment facilities comprises supply-water pump, supply-water pump is connected with header up and down by back with water inlet line, header links to each other with 1 vertical fixing hollow fiber ultrafiltration membrane device at least up and down, be connected with manually-operated gate on the back with water inlet line successively, the inflow temperature sensor, the intake pressure sensor, the water inlet pneumatic operated valve, Pressure gauge, butterfly valve, the header port of export is connected with butterfly valve respectively up and down, the water outlet pneumatic operated valve, hollow fiber ultrafiltration membrane device upper end also is connected with header, be communicated with Pressure gauge on the header, be connected with backwash pneumatic operated valve and backwashing pump successively on the header water inlet end pipeline, be connected with the water purification pneumatic operated valve successively on the header port of export pipeline, the discharge pressure sensor, flow is taken into account the leaving water temperature sensor, and wherein water purification blowoff valve and water purification pneumatic operated valve are both from header and connect.Inflow temperature sensor, supply-water pump, intake pressure sensor, backwashing pump, discharge pressure sensor, flowmeter, outlet temperature sensor are connected with automaton respectively by electric wire, water inlet pneumatic operated valve, water outlet pneumatic operated valve, water purification pneumatic operated valve, water purification blowoff valve and backwash pneumatic operated valve link to each other with magnetic valve in the automatic control cabinet by the tracheae line and then link to each other with PLC, feeder one end is connected with header up and down by pipeline and electromagnetic valve, and the other end is linked in the automatic control cabinet.
The utlity model has following beneficial effect: this full-automatic ultrafiltration water treatment facilities is owing to take such scheme, at first mutually and connect by header up and down and vertical fixing hollow fiber ultrafiltration membrane device, make compact conformation, be connected with automaton respectively by electric wire because of inflow temperature sensor, supply-water pump, intake pressure sensor, backwashing pump, discharge pressure sensor, flowmeter, leaving water temperature sensor again, realize Automatic Control, and improved cleaning performance, guaranteed to produce the stability of water water quality.This full-automatic ultrafiltration water treatment facilities has the stable characteristics that realize that Automatic Control, structure are compact more, cleaning performance reaches product water water quality well thus.
Description of drawings:
Accompanying drawing 1 is the utility model structural representation.
1-supply-water pump among the figure, 2-back with water inlet line, 3-intake pressure sensor, the 4-pneumatic operated valve of intaking, 5-Pressure gauge, the last header of 6-, header under the 7-, 8-hollow fiber ultrafiltration membrane device, 9-water outlet pneumatic operated valve, the 10-header, 11-backwash pneumatic operated valve, 12-backwashing pump, 13-water purification pneumatic operated valve, 14-discharge pressure sensor, the 15-flowmeter, 16-automaton, 17-feeder, the 18-Pressure gauge, 19-inflow temperature sensor, 20-leaving water temperature sensor, 21-water purification blowoff valve, 22-import butterfly valve, the 23-exit butterfly valve.
The specific embodiment:
The utility model is described in further detail below in conjunction with accompanying drawing:
As shown in drawings, this full-automatic ultrafiltration water treatment facilities comprises supply-water pump 1, supply-water pump 1 reaches down by back with water inlet line 2 and last header 6, and header 7 is connected, last header 6 and down header 7 at least with 1 vertical fixing hollow fiber ultrafiltration membrane device 8 mutually and connect, be connected with manually-operated gate on the back with water inlet line 2 successively, inflow temperature sensor 19, intake pressure sensor 3, water inlet pneumatic operated valve 4, Pressure gauge 5, import butterfly valve 22, last header 6 reaches down, and header 7 ports of export are connected with exit butterfly valve 23 respectively, water outlet pneumatic operated valve 9, hollow fiber ultrafiltration membrane device 8 upper ends also are connected with header 10, be communicated with Pressure gauge 18 on the header 10, be connected with backwash pneumatic operated valve 11 and backwashing pump 12 successively on the header 10 water inlet end pipelines, be connected with water purification pneumatic operated valve 13 successively on header 10 port of export pipelines, discharge pressure sensor 14, flowmeter 15 and leaving water temperature sensor 20, wherein water purification blowoff valve 21 is both from header 10 with water purification pneumatic operated valve 13 and connects.Inflow temperature sensor 19, supply-water pump 1, intake pressure sensor 3, backwashing pump 12, discharge pressure sensor 14, flowmeter 15, outlet temperature sensor 20 are connected with automaton 16 respectively by electric wire, water inlet pneumatic operated valve 4, water outlet pneumatic operated valve 9, water purification pneumatic operated valve 13, water purification blowoff valve 21 and backwash pneumatic operated valve 11 link to each other with magnetic valve in the automatic control cabinet 16 by the tracheae line and then link to each other with PLC, feeder 17 1 ends are connected with last header 6 and following header 7 by pipeline and electromagnetic valve, and the other end is linked in the automatic control cabinet.
During actual the use, after the automatic operation on operating personnel's hand point touch-screen, supply-water pump 1 starts, former water enters hollow fiber ultrafiltration membrane device 8 respectively by back with water inlet line 2 and water inlet pneumatic operated valve 4, with hollow fiber ultrafiltration membrane device 8 inside and outside pressure reduction is driving force, do filter medium in stoste is flowed through the process on film surface with hollow fiber ultrafiltration membrane device 8, water and small-molecule substance become scavenging solution through hollow fiber ultrafiltration membrane device 8 film silks surface and enter the water purification pipeline, particle diameter then is trapped within the inboard of film in the stoste greater than the material of hollow fiber ultrafiltration membrane device 8 film surface apertures, become concentrate, in such process, realized purification stoste, separate.
Because of the operation backwash process of this full-automatic ultrafiltration water treatment facilities is written among the interior PLC of automaton 16, so after the operation of the backwash on operating personnel's hand point touch-screen, make its switch of controlling backwash pneumatic operated valve 11, water purification pneumatic operated valve 13, water inlet pneumatic operated valve 4, water outlet pneumatic operated valve 9, water purification blowoff valve 21, milipore filter backwashing pump 12 and feeder 17 automatically carry out backwash.The water conservancy flushing process of milipore filter is divided into that the water inlet of following work step flings, air water flings, recoil, aerating recoil, but the washing time Field adjustment of each work step.The water inlet pneumatic operated valve 4 and the water outlet pneumatic operated valve 9 with dense water pipeline import and export of back with water inlet line can be switched mutually in the backwash process, thereby changing the milipore filter surface liquid flows to, and by backwash aerating simultaneously film silk surface has been increased to shear the easier pollutant that washes away film silk surface of flow velocity, prolong the service life of milipore filter.The design of water purification blowoff valve 21 is to discharge for the water that the milipore filter initial stage is produced in the work step, avoids the influence of milipore filter backwash, to guarantee finally to produce the stable of water water quality.The milipore filter of this full-automatic ultrafiltration water treatment facilities can adopt that dead-end filtration, cross-flow filtration, crossing filtering, online medicine are washed according to the water quality treatment difference, the method for operation such as little wadding before the film, greatly brings into play the advantage of film.
Field Force's operation and management that wherein application of touch-screen is more convenient, the Field Force can understand the running status of complete equipment (comprising supply-water pump 1 constantly by the dynamic menu on the touch-screen, intake pressure sensor 3, discharge pressure sensor 14, flowmeter 15, inflow temperature sensor 19, leaving water temperature sensor 20, water inlet pneumatic operated valve 4, water outlet pneumatic operated valve 9, backwashing pump 12, water purification pneumatic operated valve 13, the switch of water purification blowoff valve 21, fluid temperature, produce net water flux, the variation of ultrafiltration membrane pressure), program is dispatched from the factory and is configured in the equipment, and the Field Force is according to changing the also running time of adjustable apparatus, the backwash time.
In sum, this full-automatic ultrafiltration water treatment facilities is at first because of switch, fluid temperature, pressure variation, product net water flux by supply-water pump 1, intake pressure sensor 3, discharge pressure sensor 14, flowmeter 15, inflow temperature sensor 19, leaving water temperature sensor 20, water inlet pneumatic operated valve 4, water outlet pneumatic operated valve 9, backwashing pump 12, water purification pneumatic operated valve 13, water purification blowoff valve 21 in the PLC in the automaton 16, touch-screen, the Frequency Converter Control equipment, thus realization Automatic Control and demonstration.Again by vertical fixedly hollow fiber ultrafiltration membrane device, make compact conformation, floor space is dwindled.And wherein go up header 6 and descend the design of header 7 upper inlet butterfly valves 22, exit butterfly valve 23 can realize the online chemical regeneration of this device.At last by the backwash pneumatic operated valve 11 on the PLC internal program control appliance, water outlet pneumatic operated valve 9, water inlet pneumatic operated valve 4, milipore filter backwashing pump 12 and feeder 17 realize water inlet fling wash, air water flings and washes, backwash, aerating backwash, solved the single problem of existing water treatment facilities backwashing manner, strengthened cleaning performance, improve the utilization rate of water simultaneously, guaranteed the stable of final product water water quality.
Claims (1)
1, a kind of full-automatic ultrafiltration water treatment facilities, comprise supply-water pump (1), it is characterized in that: supply-water pump (1) is by back with water inlet line (2) and header (6 up and down, 7) be connected, header (6 up and down, 7) link to each other with 1 vertical fixing hollow fiber ultrafiltration membrane device (8) at least, back with water inlet line is connected with manually-operated gate on (2) successively, inflow temperature sensor (19), intake pressure sensor (3), water inlet pneumatic operated valve (4), Pressure gauge (5), import butterfly valve (22), header (6 up and down, 7) port of export is connected with exit butterfly valve (23) respectively, water outlet pneumatic operated valve (9), hollow fiber ultrafiltration membrane device (8) upper end also is connected with header (10), be communicated with Pressure gauge (18) on the header (10), be connected with backwash pneumatic operated valve (11) and backwashing pump (12) on header (10) the water inlet end pipeline successively, be connected with water purification pneumatic operated valve (13) successively on header (10) port of export pipeline, discharge pressure sensor (14), flowmeter (15) and leaving water temperature sensor (20), wherein water purification blowoff valve (21) is both from header (10) with water purification pneumatic operated valve (13) and connects, inflow temperature sensor (19), supply-water pump (1), intake pressure sensor (3), backwashing pump (12), discharge pressure sensor (14), flowmeter (15), outlet temperature sensor (20) is connected with automaton (16) respectively by electric wire, water inlet pneumatic operated valve (4), water outlet pneumatic operated valve (9), water purification pneumatic operated valve (13), water purification blowoff valve (21) and backwash pneumatic operated valve (11) link to each other by the magnetic valve in tracheae line and the automatic control cabinet (16) and then link to each other with PLC, feeder (17) one ends are by pipeline and electromagnetic valve and header (6 up and down, 7) be connected, the other end is linked in the automatic control cabinet (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200890554U CN201182973Y (en) | 2008-01-14 | 2008-01-14 | Full-automatic hyperfiltration water treatment apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200890554U CN201182973Y (en) | 2008-01-14 | 2008-01-14 | Full-automatic hyperfiltration water treatment apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201182973Y true CN201182973Y (en) | 2009-01-21 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200890554U Expired - Fee Related CN201182973Y (en) | 2008-01-14 | 2008-01-14 | Full-automatic hyperfiltration water treatment apparatus |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102631807A (en) * | 2012-04-09 | 2012-08-15 | 南通海利源船舶设备工程有限公司 | Deicing filter method and equipment for seawater in ice region |
| CN104785116A (en) * | 2014-01-17 | 2015-07-22 | 浦华环保有限公司 | Ultrafilter membrane vertical pipeline valve assembly |
| CN109231299A (en) * | 2018-10-12 | 2019-01-18 | 南京奥特净化工程有限公司 | A kind of water treatment facilities intelligence gas source storage distribution application apparatus and its control method |
| CN115317986A (en) * | 2022-10-10 | 2022-11-11 | 佛山市绿田环保机械设备有限公司 | Automatic back flush sewage treatment device and control system thereof |
-
2008
- 2008-01-14 CN CNU2008200890554U patent/CN201182973Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102631807A (en) * | 2012-04-09 | 2012-08-15 | 南通海利源船舶设备工程有限公司 | Deicing filter method and equipment for seawater in ice region |
| CN102631807B (en) * | 2012-04-09 | 2016-12-14 | 南通海利源船舶设备工程有限公司 | Ice formation sea water disappears ice filter method |
| CN104785116A (en) * | 2014-01-17 | 2015-07-22 | 浦华环保有限公司 | Ultrafilter membrane vertical pipeline valve assembly |
| CN109231299A (en) * | 2018-10-12 | 2019-01-18 | 南京奥特净化工程有限公司 | A kind of water treatment facilities intelligence gas source storage distribution application apparatus and its control method |
| CN115317986A (en) * | 2022-10-10 | 2022-11-11 | 佛山市绿田环保机械设备有限公司 | Automatic back flush sewage treatment device and control system thereof |
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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: 20090121 Termination date: 20160114 |