CN201477450U - Anti-permeation constant flow control system - Google Patents
Anti-permeation constant flow control system Download PDFInfo
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- CN201477450U CN201477450U CN2009201916823U CN200920191682U CN201477450U CN 201477450 U CN201477450 U CN 201477450U CN 2009201916823 U CN2009201916823 U CN 2009201916823U CN 200920191682 U CN200920191682 U CN 200920191682U CN 201477450 U CN201477450 U CN 201477450U
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- water
- permeation
- control system
- pressure pump
- flow
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses an anti-permeation constant flow control system, comprising a pressure control system and an anti-permeation device; wherein the pressure control system comprises a pressure feedback device and a high pressure pump, the anti-permeation device comprises a water inlet pipe, a water production pipe and a concentrated water pipe, the water inlet pipe is connected with the high pressure pump and the pressure feedback device in turn, the high pressure pump is provided with a variable frequency controller, and the water production pipe is provided with a water production flow meter. When anti-permeation water production flow is higher or lower than a preset value, the water production flow meter feeds signal to the high pressure pump which changes the frequency of a power supply via the variable frequency controller, to control the speed of a motor and adjust water intake flow, thereby realizing constant flow of water production. The anti-permeation constant flow control system can confirm the quality of output water and resolve the problem as instable flow of anti-permeation water output, and has low equipment investment and operation cost.
Description
Technical field
The utility model relates to counter-infiltration constant flux control system.
Background technology
Counter-infiltration is a new membrane separation technique that grows up the sixties in last century, and reverse osmosis membrane relies on the solvent that makes under the pressure-driven in the solution to be separated with solute.Under certain pressure, H2O molecule in the former water can pass through the RO film, and impurity such as the inorganic salts in the former water, heavy metal ion, organism, colloid, bacterium, virus can't pass through the RO film, thereby pure water that can see through and the condensed water strictness that can't see through are made a distinction.Reverse osmosis equipment is present a kind of common process water production equipment, is widely used in fields such as scientific research, medicine, food, beverage, desalinization.Reverse osmosis unit is in operational process, because of labile factors such as the water temperature of outer net water inlet, intake pressure, raw water quality cause the instability of producing discharge, if contained salinity or organism are higher in the former water, then osmotic pressure also increases, under the constant situation of intake pressure, net pressure will reduce, and water production rate reduces; Moreover along with the increase of water temperature, the increase that water flux is also linear, just increase/minimizing 2.5%~3.0% of water flux is produced in 1 ℃ of the every rising of water inlet water temperature/reductions, and the variation of the water temperature of intaking can influence water production rate equally.So it is very necessary that discharge is produced in control, because too high product discharge, the too high recovery have not only strengthened concentration polarization, can cause the salt rate to rise again, thereby cause the salt rejection rate influence that descends to produce water water quality.If the water production rate deficiency then can't guarantee the stability that supplies water.
The utility model content
Technical problem to be solved in the utility model provides a kind of in assurance water flow, equipment investment cost and the cheap counter-infiltration constant flux control system of operating cost.
For solving the problems of the technologies described above, the utility model adopts following technical scheme: counter-infiltration constant flux control system, comprise control pressurer system and reverse osmosis unit, described control pressurer system comprises pressure feedback device, high-pressure pump, described reverse osmosis unit is provided with inlet channel, water producing pipe road and dense waterpipe, described inlet channel connects high-pressure pump, pressure feedback device successively, and described high-pressure pump is provided with frequency-variable controller, and described water producing pipe road is provided with the product water ga(u)ge.
Described pressure feedback device is a pressure unit.
Described inlet channel is provided with tensimeter.
Described dense waterpipe is provided with the emission flow meter.
The utility model is owing to adopted technique scheme, when reverse osmosis produced discharge is higher or lower than the setting flow, produce the water ga(u)ge signal feedback and give high-pressure pump, high-pressure pump changes supply frequency by frequency-variable controller, motor is realized speed control, adjust flow of inlet water, thereby realize producing the constant of discharge.The utility model has solved counter-infiltration water flow problem of unstable when guaranteeing effluent quality, and equipment investment cost and operating cost are cheap.
Description of drawings
Fig. 1 is the structural representation of the utility model counter-infiltration constant flux control embodiment of system.
Embodiment
Below in conjunction with accompanying drawing embodiment of the present utility model is further described.
Figure 1 shows that the utility model counter-infiltration constant flux control system, comprise control pressurer system and reverse osmosis unit 1, described control pressurer system comprises pressure feedback device, high-pressure pump 2, described reverse osmosis unit 1 is provided with inlet channel 3, water producing pipe road 4 and dense waterpipe 5, described inlet channel 3 connects high-pressure pump 2, pressure feedback device successively, and described high-pressure pump 2 is provided with frequency-variable controller.Frequency conversion is by changing supply frequency motor to be realized speed control, and frequency conversion can be regulated and move arbitrarily between 0~50HZ.Described pressure feedback device is a pressure unit 6.Described inlet channel 3 is provided with tensimeter 7.Described water producing pipe road 4 is provided with and produces water ga(u)ge 8.Described dense waterpipe 5 is provided with emission flow meter 9.
During use, former water produces certain driving force through high-pressure pump 2, sends into reverse osmosis unit 1 by inlet channel 3, and tensimeter 7 is set on the inlet channel 3, shows feed water by reverse osmosis pressure; Reverse osmosis produced water multiparity waterpipe 4 is collected, and establishes on the water producing pipe road 4 and produces water ga(u)ge 8, shows reverse osmosis produced discharge, produce water ga(u)ge 8 flow signals and feed back to pressure unit 6, thereby the frequency-variable controller on the high-pressure pump 2 is made indication to high-pressure pump; Reverse osmosis concentrated water is established concentrated stream amount meter 9 through dense waterpipe 5 dischargings on the dense waterpipe 5, show the concentrated stream amount.
In the counter-infiltration operational process, produce water ga(u)ge and set certain flow value, the corresponding 4-20mA current analog of this flow value amount output valve, be lower than the setting flow when producing discharge, the analog quantity output valve fluctuation of electric current, signal feedback is to the frequency-variable controller on the high-pressure pump, and frequency-variable controller carries out accuracy controlling to all relative variablees such as rotating speed, moment of torsion and power, reach the current analog signal output valve of setting the flow correspondence, thereby reach the purpose of constant product discharge.The product discharge of producing the water ga(u)ge demonstration when influent quality fluctuation or temperature variation also can fluctuate.The utility model counter-infiltration constant flux control system is by PLC control of conversion controller, pressure unit and product water ga(u)ge, and automation degree of equipment and running efficiency of system all improve, and satisfy the suitability for industrialized production requirement, guarantees the continuation and the stability that supply water.
Claims (4)
1. counter-infiltration constant flux control system, it is characterized in that: comprise control pressurer system and reverse osmosis unit (1), described control pressurer system comprises pressure feedback device, high-pressure pump (2), described reverse osmosis unit (1) is provided with inlet channel (3), water producing pipe road (4) and dense waterpipe (5), described inlet channel (3) connects high-pressure pump (2), pressure feedback device successively, described high-pressure pump (2) is provided with frequency-variable controller, and described water producing pipe road (4) is provided with and produces water ga(u)ge (8).
2. according to the described counter-infiltration constant flux control of claim 1 system, it is characterized in that: described pressure feedback device is pressure unit (6).
3. according to the described counter-infiltration constant flux control of claim 1 system, it is characterized in that: described inlet channel (3) is provided with tensimeter (7).
4. according to the described counter-infiltration constant flux control of claim 1 system, it is characterized in that: described dense waterpipe (5) is provided with emission flow meter (9).
Priority Applications (1)
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CN2009201916823U CN201477450U (en) | 2009-08-12 | 2009-08-12 | Anti-permeation constant flow control system |
Applications Claiming Priority (1)
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CN2009201916823U CN201477450U (en) | 2009-08-12 | 2009-08-12 | Anti-permeation constant flow control system |
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CN201477450U true CN201477450U (en) | 2010-05-19 |
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CN2009201916823U Expired - Fee Related CN201477450U (en) | 2009-08-12 | 2009-08-12 | Anti-permeation constant flow control system |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103626263A (en) * | 2013-11-27 | 2014-03-12 | 长沙中联重科环卫机械有限公司 | Method, device and system for treatment control of percolate and sewage treatment device |
CN108069535A (en) * | 2017-12-20 | 2018-05-25 | 沁园集团股份有限公司 | A kind of water purifier system of voltage adaptive controlling |
CN109336304A (en) * | 2018-11-30 | 2019-02-15 | 佛山市云米电器科技有限公司 | A kind of circulating household water purifier and domestic water purifying machine of stable water delivery |
CN109336275A (en) * | 2018-11-30 | 2019-02-15 | 佛山市云米电器科技有限公司 | A kind of reverse osmosis household water purifier and domestic water purifying machine of stable water delivery |
-
2009
- 2009-08-12 CN CN2009201916823U patent/CN201477450U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103626263A (en) * | 2013-11-27 | 2014-03-12 | 长沙中联重科环卫机械有限公司 | Method, device and system for treatment control of percolate and sewage treatment device |
CN103626263B (en) * | 2013-11-27 | 2015-12-09 | 长沙中联重科环卫机械有限公司 | The process control method of percolate, device, system and sewage disposal device |
CN108069535A (en) * | 2017-12-20 | 2018-05-25 | 沁园集团股份有限公司 | A kind of water purifier system of voltage adaptive controlling |
CN109336304A (en) * | 2018-11-30 | 2019-02-15 | 佛山市云米电器科技有限公司 | A kind of circulating household water purifier and domestic water purifying machine of stable water delivery |
CN109336275A (en) * | 2018-11-30 | 2019-02-15 | 佛山市云米电器科技有限公司 | A kind of reverse osmosis household water purifier and domestic water purifying machine of stable water delivery |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100519 Termination date: 20130812 |