CN203513381U - Serial-parallel reverse osmosis system - Google Patents
Serial-parallel reverse osmosis system Download PDFInfo
- Publication number
- CN203513381U CN203513381U CN201320587148.0U CN201320587148U CN203513381U CN 203513381 U CN203513381 U CN 203513381U CN 201320587148 U CN201320587148 U CN 201320587148U CN 203513381 U CN203513381 U CN 203513381U
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- Prior art keywords
- reverse osmosis
- osmosis system
- valve
- water tank
- water
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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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- 238000001223 reverse osmosis Methods 0.000 title claims abstract description 90
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 80
- 239000003814 drug Substances 0.000 claims description 5
- 230000008676 import Effects 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 8
- 230000008569 process Effects 0.000 abstract description 8
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 230000006866 deterioration Effects 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 abstract description 3
- 230000004907 flux Effects 0.000 description 6
- 230000009183 running Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 241000700605 Viruses Species 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002158 endotoxin Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000002510 pyrogen Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910021642 ultra pure water Inorganic materials 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to a water treatment system, and particularly relates to a serial-parallel reverse osmosis system, which mainly solves the technical problems in the prior art that equipment is bound to be idle when water quality is good, resulting in waste if a technological process and equipment are determined according to the standard of low-quality water, and the produced water is unqualified to lead to potential safety hazards and the like in production due to deterioration of water quality if the technological process and the equipment are determined according to the standard of high-quality water. The serial-parallel reverse osmosis system comprises a pretreatment water tank, wherein the pretreatment water tank is connected with a lift pump A; the lift pump A is connected with a reverse osmosis system A; the reverse osmosis system A is communicated with a water tank A; the water tank A is connected with a lift pump B; the lift pump B is connected with a reverse osmosis system B; the reverse osmosis system B is communicated with a water tank B; the inlets of the reverse osmosis system A and the reverse osmosis system B are connected with each other through a pipeline.
Description
Technical field
The utility model relates to a kind of water treatment system, especially relates to a kind of series-parallel connection reverse osmosis system.
Background technology
Reverse osmosis membrane is a kind of by pressure-actuated Novel separation film, and under pressure promotes, the water molecules in solution sees through film, and other molecule, ion, bacterium, virus etc. are trapped, thereby reaches the object of Pure-water Making.The aperture of reverse osmosis membrane is less than 1nm (nanometer), can effectively remove divalent ion, to the clearance of monovalent ion, also can reach 95～99%; To the clearance of low-molecular-weight organic matter, can reach 100%; Reverse osmosis system can be removed more than 99% mineral substance, bacterium, virus, pyrogen and bacterial endotoxin etc. in former water.
Due to the advanced person of reverse osmosis isolation technology, efficient and energy conservation characteristic, at each industrial circle, be all widely used, existing large-scale reverse osmosis equipment is for sea water desaltination, and brackish water purifies and Industrial Wastewater Treatment.Utilize reverse osmosis desalination, can prepare pure water or ultrapure water for semi-conductor, unicircuit manufacture water, power plant boiler water, pure water for pharmaceutical industries, pure water, beverage industry water and other industry (makeup, printing and dyeing, plating etc.) water for chemical industry.
Just because of reverse osmosis technology widespread use, aspect reverse osmosis operation, exist some uncertain factors to affect the stability of reverse osmosis operation.The impact that example reverse osmosis operation conditions is subject to that influent quality fluctuation saliferous and temperature variation, the total water production rate of system change, reverse osmosis operating pressure changes etc. factor greatly.
In Treatment of Industrial Water application, technical process determines and during lectotype selection, if determine the technical process lectotype selection of going forward side by side by poor water quality, certainly will cause when water quality is better, and the idleness of equipment causes investment to waste; If determine technical process type selecting equipment according to good raw water quality, in the time of again can be because of water quality deterioration, produce that quality is defective brings potential safety hazard to production.
Utility model content
The utility model is to provide a kind of series-parallel connection reverse osmosis system, it is mainly to solve that the existing technical process of prior art is determined and during lectotype selection, if determine the technical process lectotype selection of going forward side by side by poor water quality, certainly will cause when water quality is better, the idleness of equipment causes investment waste; If determine technical process type selecting equipment according to good raw water quality, in the time of again can be because of water quality deterioration, produce the defective technical problem of bringing potential safety hazard etc. to production of quality.
Above-mentioned technical problem of the present utility model is mainly solved by following technical proposals:
A kind of series-parallel connection reverse osmosis system of the present utility model, comprise pretreatment water tank, described pretreatment water tank is connected with lift pump A by pipeline, lift pump A is connected with reverse osmosis system A, reverse osmosis system A is communicated with water tank A, the outlet of water tank A is connected with lift pump B by pipeline, lift pump B is connected with reverse osmosis system B, reverse osmosis system B is communicated with water tank B, the exit of water tank A is provided with the first valve, the second valve, the exit of water tank B is provided with the 3rd valve, reverse osmosis system A, the ingress of reverse osmosis system B connects by pipeline, and this section of pipeline is provided with the 4th valve.The utility model can be realized two kinds of operational modes by the combination between each valve and water tank transitional function, a kind of pattern is: reverse osmosis system A produces water and enters reverse osmosis system B, be that reverse osmosis system A moves as first-stage reverse osmosis, reverse osmosis system B moves as two-pass reverse osmosis, and the operational mode of A and B is series operation; Another kind of pattern is: total water inlet enters respectively reverse osmosis system A and reverse osmosis system B, and now reverse osmosis system A and reverse osmosis system B are that the operational mode of A and B is parallel running as first-stage reverse osmosis operation.
As preferably, the ingress of described reverse osmosis system A is provided with 5 μ m cartridge filters.The effect of 5 μ m cartridge filters is to hold back the particle that is greater than 5 μ m that former water brings, to prevent that it from entering reverse osmosis system.This particle may puncture reverse osmosis membrane assembly after high-pressure pump is accelerated, and causes the situation of a large amount of leakage salt, scratches the impeller of high-pressure pump simultaneously.
As preferably, the ingress of described reverse osmosis system B is provided with medicine system.When reverse osmosis system B moves as two-pass reverse osmosis, this medicine system can regulate the water inlet pH value that enters reverse osmosis system B, meets the requirement of feed water by reverse osmosis water quality to pH.
As preferably, between described lift pump A and the outlet of lift pump B, by pipeline, be connected, this section of pipeline is provided with the 5th valve.Whether can control like this lift pump B water out needs through cartridge filter.
As preferably, between described lift pump A and the import of lift pump B, by pipeline, be connected, this section of pipeline is provided with the 6th valve.Can control like this water tank A wet concentration out selects and enters lift pump A and lift pump B or enter separately lift pump B.
As preferably, the exit of described pretreatment water tank is provided with the 7th valve.
Therefore, the utility model can reduce water source, exerting oneself changes the impact that reverse osmosis operating load is changed; Frequent start-stop while avoiding series operation.Operation is controlled simple, saves water treatment system investment cost, guarantees reverse osmosis system also steady running when other factors affects, simple and reasonable for structure.
Accompanying drawing explanation
Accompanying drawing 1 is a kind of structural representation of the present utility model.
Component, position and numbering in figure: pretreatment water tank 1, lift pump A2, reverse osmosis system A3, water tank A4, lift pump B5, reverse osmosis system B6, water tank B7, the first valve 8, the second valve 9, the 3rd valve 10, the 4th valve 11, cartridge filter 12, medicine system 13, the 5th valve 14, the 6th valve 15, the 7th valve 16.
Embodiment
Below by embodiment, and by reference to the accompanying drawings, the technical solution of the utility model is described in further detail.
Embodiment: a kind of series-parallel connection reverse osmosis system of this example, as Fig. 1, comprise pretreatment water tank 1, the exit of pretreatment water tank is provided with the 7th valve 16.Pretreatment water tank is connected with lift pump A2 by pipeline, lift pump A is connected with reverse osmosis system A3, reverse osmosis system A is communicated with water tank A4, the outlet of water tank A is connected with lift pump B5 by pipeline, lift pump B is connected with reverse osmosis system B6, reverse osmosis system B is communicated with water tank B7, the exit of water tank A is provided with the first valve 8, the second valve 9, the exit of water tank B is provided with the 3rd valve 10, the ingress of reverse osmosis system A, reverse osmosis system B connects by pipeline, and this section of pipeline is provided with the 4th valve 11.The ingress of reverse osmosis system A is provided with cartridge filter 12.The ingress of reverse osmosis system B is provided with medicine system 13.Between the outlet of lift pump A and lift pump B, by pipeline, be connected, this section of pipeline is provided with the 5th valve 14.Between the import of lift pump A and lift pump B, by pipeline, be connected, this section of pipeline is provided with the 6th valve 15.
Series operation pattern: close the 6th valve 15, the 5th valve 14, the 4th valve 11, the first valve 8, open the 7th valve 16, the second valve 9, the 3rd valve 10, through pretreated former water, through the 7th valve 16---lift pump A2---cartridge filter 12---reverse osmosis system A3---water tank A4---the second valve 9---lift pump B5----reverse osmosis system B6----water tank B7-----the 3rd valve 10, go next stage system.
Parallel running pattern: close the second valve 9, open the 7th valve 16, the 6th valve 15, the 5th valve 14, the 4th valve 11, the first valve 8, the 3rd valve 10, through pretreated former water, through the 7th valve 16-----lift pump A2----cartridge filter 12-----reverse osmosis system A3-----water tank A4-----the first valve 8, go next stage system.
Valve 14----cartridge filter 12--the 4th valve 11---reverse osmosis system B6---water tank B7-----the 3rd valve 10------goes next stage system to the 7th valve 16-----the 6th valve 15----lift pump B5---the 5th.
In addition, native system can arrange 8 cover reverse osmosis units, is divided into A group and B group (every group has 4 cover reverse osmosis units).When raw water quality is poor, A group and the series operation of B group, B group is as two-pass reverse osmosis, and A organizes the reverse osmosis rate of recovery 75%, the B group reverse osmosis rate of recovery 80%.When raw water quality is better, A group and B sets in parallel operation, two groups of reverse osmosis rate of recovery are 75%.
When considering source quality fluctuation, when raw water quality is poor (inwelling season), A group and the series operation of B group, A group design permeant flux is 16.25-20LMH, B group design permeant flux is 35.41LMH; When raw water quality is better, A group and B sets in parallel operation, A group design permeant flux is 24.18LMH, B group design permeant flux is 24.08LMH.The benefit of this design is: the A group most of the time is more easily polluted than the reverse osmosis of B group as first-stage reverse osmosis, should select lower permeant flux to reduce contaminated risk; And when two groups of reverse osmosis parallel runnings, the permeant flux of two groups of reverse osmosiss is more balanced.
The foregoing is only specific embodiment of the utility model, but constitutional features of the present utility model is not limited to this, any those skilled in the art is in field of the present utility model, and the variation of doing or modification are all encompassed among the scope of the claims of the present utility model.
Claims (6)
1. a series-parallel connection reverse osmosis system, comprise pretreatment water tank (1), it is characterized in that described pretreatment water tank (1) is connected with lift pump A(2 by pipeline), lift pump A is connected with reverse osmosis system A(3), reverse osmosis system A is communicated with water tank A(4), the outlet of water tank A is connected with lift pump B(5 by pipeline), lift pump B is connected with reverse osmosis system B(6), reverse osmosis system B is communicated with water tank B(7), the exit of water tank A is provided with the first valve (8), the second valve (9), the exit of water tank B is provided with the 3rd valve (10), reverse osmosis system A, the ingress of reverse osmosis system B connects by pipeline, and this section of pipeline is provided with the 4th valve (11).
2. a kind of series-parallel connection reverse osmosis system according to claim 1, is characterized in that described reverse osmosis system A(3) ingress be provided with cartridge filter (12).
3. a kind of series-parallel connection reverse osmosis system according to claim 1 and 2, is characterized in that described reverse osmosis system B(6) ingress be provided with medicine system (13).
4. a kind of series-parallel connection reverse osmosis system according to claim 1 and 2, is characterized in that described lift pump A(2) with lift pump B(5) outlet between by pipeline, be connected, this section of pipeline is provided with the 5th valve (14).
5. a kind of series-parallel connection reverse osmosis system according to claim 1 and 2, is characterized in that described lift pump A(2) with lift pump B(5) import between by pipeline, be connected, this section of pipeline is provided with the 6th valve (15).
6. a kind of series-parallel connection reverse osmosis system according to claim 1 and 2, is characterized in that the exit of described pretreatment water tank (1) is provided with the 7th valve (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320587148.0U CN203513381U (en) | 2013-09-23 | 2013-09-23 | Serial-parallel reverse osmosis system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320587148.0U CN203513381U (en) | 2013-09-23 | 2013-09-23 | Serial-parallel reverse osmosis system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203513381U true CN203513381U (en) | 2014-04-02 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320587148.0U Expired - Lifetime CN203513381U (en) | 2013-09-23 | 2013-09-23 | Serial-parallel reverse osmosis system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203513381U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109485211A (en) * | 2019-01-22 | 2019-03-19 | 北京博鑫精陶环保科技有限公司 | Sewage disposal system and sewage treatment process |
-
2013
- 2013-09-23 CN CN201320587148.0U patent/CN203513381U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109485211A (en) * | 2019-01-22 | 2019-03-19 | 北京博鑫精陶环保科技有限公司 | Sewage disposal system and sewage treatment process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201010 Address after: No.99, Huaxing Road, Xihu District, Hangzhou City, Zhejiang Province Patentee after: Zhejiang Tiandi Environmental Protection Technology Co.,Ltd. Address before: 311203, 19 floor, building 1, Pacific Plaza, No. 451 Jincheng Road, Xiaoshan District, Zhejiang, Hangzhou Patentee before: ZHEJIANG DONGFA ENVIRONMENTAL PROTECTION ENGINEERING Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140402 |
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| CX01 | Expiry of patent term |