CN201347372Y - Water PH adjustable reverse osmosis device - Google Patents
Water PH adjustable reverse osmosis device Download PDFInfo
- Publication number
- CN201347372Y CN201347372Y CNU2008201676986U CN200820167698U CN201347372Y CN 201347372 Y CN201347372 Y CN 201347372Y CN U2008201676986 U CNU2008201676986 U CN U2008201676986U CN 200820167698 U CN200820167698 U CN 200820167698U CN 201347372 Y CN201347372 Y CN 201347372Y
- Authority
- CN
- China
- Prior art keywords
- reverse osmosis
- water
- osmosis device
- conductivity
- produced
- Prior art date
- 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 - Fee Related
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 63
- 238000001223 reverse osmosis Methods 0.000 title claims abstract description 51
- 239000002455 scale inhibitor Substances 0.000 claims abstract description 4
- 238000010979 pH adjustment Methods 0.000 abstract description 2
- 239000003513 alkali Substances 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
一种产水PH可调节反渗透装置,在具有阻垢剂投加装置、保安滤器、高压泵和反渗透器组成的反渗透装置中,特别在保安滤器前进水管上,设置一套PH调节装置,用于调节反渗透进水PH,进而达到调节反渗透产水PH的目的。实践证明,采用本实用新型在达到反渗透产水PH要求的基础上,同时可使其产水电导率达到要求值。
A PH-adjustable reverse osmosis device for produced water. In the reverse osmosis device composed of a scale inhibitor dosing device, a security filter, a high-pressure pump and a reverse osmosis device, a set of PH adjustment devices is arranged especially on the water inlet pipe of the security filter. , used to adjust the pH of reverse osmosis feed water, and then achieve the purpose of adjusting the pH of reverse osmosis product water. Practice has proved that the utility model can make the conductivity of the produced water reach the required value on the basis of meeting the PH requirement of the reverse osmosis produced water.
Description
技术领域 technical field
本实用新型涉及一种反渗透膜法制纯水装置。The utility model relates to a reverse osmosis membrane pure water device.
背景技术 Background technique
目前使用反渗透膜装置制造纯水已较为普遍,它具有处理水质范围宽、出水水质好、环保等特点。但当反渗透产水PH不能达到要求时,目前使用的方法是直接对反渗透产水进行加酸或加碱处理,以达到要求的产水PH;但对反渗透产水直接进行加酸或加碱处理时,将导致反渗透产水电导率上升,使反渗透产水水质变差,出现反渗透产水PH达到了要求,而反渗透产水电导率则出现超标现象。At present, it is more common to use reverse osmosis membrane devices to produce pure water. It has the characteristics of wide range of water quality, good effluent quality, and environmental protection. However, when the pH of the reverse osmosis product water cannot meet the requirements, the currently used method is to directly add acid or alkali to the reverse osmosis product water to achieve the required pH of the product water; but directly add acid or alkali to the reverse osmosis product water Adding alkali will increase the conductivity of the reverse osmosis product water, making the quality of the reverse osmosis product water worse, and the pH of the reverse osmosis product water will meet the requirements, while the conductivity of the reverse osmosis product water will exceed the standard.
发明内容 Contents of the invention
本实用新型拟解决的技术问题是,在对反渗透产水进行PH调节时,使反渗透产水PH达到要求的前提下,同时使反渗透产水电导率指标达到要求。The technical problem to be solved by the utility model is to adjust the pH of the reverse osmosis produced water, and at the same time make the reverse osmosis produced water conductivity index meet the requirement under the premise that the pH of the reverse osmosis produced water meets the requirements.
本实用新型的技术解决方案是:在以管道顺序连接的阻垢剂投加装置、保安滤器、高压泵、反渗透器组成的反渗透装置中,特别在反渗透器进水侧设置一套PH调节装置,用于调节反渗透器进水PH。The technical solution of the utility model is: in the reverse osmosis device composed of the antiscalant dosing device, security filter, high-pressure pump and reverse osmosis device connected in sequence by pipelines, a set of pH The adjusting device is used to adjust the pH of the reverse osmosis water.
本实用新型的有益效果是,由于在反渗透器进水中进行PH调节,而反渗透器中的反渗透膜能截留进水的大部分离子,因而其对反渗透产水电导率影响较小。故对反渗透进水PH进行调节,从而引起了反渗透产水PH发生了变化,能在反渗透产水PH达到要求的前提下,其反渗透产水电导率也同时达到要求。The beneficial effect of the utility model is that since the PH adjustment is carried out in the feed water of the reverse osmosis device, and the reverse osmosis membrane in the reverse osmosis device can intercept most of the ions in the feed water, it has little influence on the conductivity of the reverse osmosis produced water . Therefore, the pH of the reverse osmosis feed water is adjusted, which causes the pH of the reverse osmosis product water to change. Under the premise that the pH of the reverse osmosis product water meets the requirements, the conductivity of the reverse osmosis product water also meets the requirements.
附图说明 Description of drawings
附图为本实用新型总体结构示意图。Accompanying drawing is the utility model overall structure schematic diagram.
具体实施方式 Detailed ways
下面结合附图对本实用新型作进一步说明。Below in conjunction with accompanying drawing, the utility model is further described.
如附图;从预处理系统得到的预处理水(1)作为原水,通过管道(2),在阻垢剂投加装置(11)投加阻垢剂后,进入保安滤器(3),再由保安滤器(3)进入高压泵(4),由高压泵(4)加压后,通过泵出口管(5),送至反渗透器(6),经反渗透器(6)处理后,产出的纯水通过管道(7)成外供纯水(8),处理后的浓水通过排放管(9),排放至浓水池(10);而本实用新型中,特别在保安滤器(3)的进水管路(2)上,设置一套PH调节装置(12),用于调节反渗透进水PH,进而以达到调节反渗透产水PH的目的。As shown in the accompanying drawing; the pretreated water (1) obtained from the pretreatment system is used as raw water, passes through the pipeline (2), and after the scale inhibitor is added to the scale inhibitor dosing device (11), it enters the security filter (3), and then Enter the high-pressure pump (4) from the security filter (3), after being pressurized by the high-pressure pump (4), it is sent to the reverse osmosis device (6) through the pump outlet pipe (5), and after being treated by the reverse osmosis device (6), The pure water of output becomes external supply pure water (8) through pipeline (7), and the concentrated water after the treatment is discharged into concentrated water pool (10) through discharge pipe (9); 3) On the water inlet pipeline (2), a set of pH adjusting device (12) is provided for adjusting the pH of the reverse osmosis feed water, and then achieve the purpose of adjusting the pH of the reverse osmosis produced water.
下面为本实用新型与普通反渗透装置具体实施情况。The following is the specific implementation of the utility model and the common reverse osmosis device.
实施例一:Embodiment one:
对于给定的原水水源,要求反渗透装置产水PH≥6.5,电导率≤10μs/cm。For a given source of raw water, it is required that the water produced by the reverse osmosis device has a pH ≥ 6.5 and a conductivity ≤ 10 μs/cm.
由上表可见,在相同原水条件下,本实用新型反渗透装置在达到要求的产水PH时,其产水电导率降低,水质提高,这时由于在反渗透器进水中加碱后,降低了溶于原水中的气体对反渗透产水电导率的影响,这就使反渗透产水的PH和电导率同时达到了要求;而普通型反渗透装置在达到要求的产水PH时,其产水电导率上升,达到了12.3μs/cm,不能达到要求的反渗透产水电导率。It can be seen from the above table that under the same raw water conditions, when the reverse osmosis device of the present invention reaches the required pH of the produced water, the conductivity of the produced water decreases and the water quality improves. Reduce the influence of gas dissolved in raw water on the conductivity of reverse osmosis product water, which makes the PH and conductivity of reverse osmosis product water meet the requirements at the same time; The conductivity of the product water has risen to 12.3μs/cm, which cannot meet the required conductivity of the reverse osmosis product water.
实施例二:Embodiment two:
对于给定的原水水源,要求反渗透装置产水PH≤5.5,电导率≤10μs/cm。For a given source of raw water, it is required that the water produced by the reverse osmosis device has a pH ≤ 5.5 and a conductivity ≤ 10 μs/cm.
由上表可见,在相同原水条件下,本实用新型反渗透装置在达到要求的产水PH时,其产水电导率上升,水质降低,但仍能达到要求反渗透产水电导率;而普通型反渗透装置在达到要求的产水PH时,其产水电导率上升较大,达到了10.1μs/cm,不能达到要求的反渗透产水电导率。It can be seen from the above table that under the same raw water conditions, when the reverse osmosis device of the present invention reaches the required pH of the produced water, the conductivity of the produced water increases and the water quality decreases, but the required conductivity of the reverse osmosis produced water can still be achieved; When the type reverse osmosis device reaches the required pH of the product water, the conductivity of the product water rises greatly, reaching 10.1μs/cm, which cannot meet the required conductivity of the product water of reverse osmosis.
通过以上实例说明,本实用新型能使反渗透产水同时达到要求的产水PH和电导率的指标。Through the above examples, the utility model can make the reverse osmosis produced water meet the required pH and conductivity indexes of the produced water at the same time.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2008201676986U CN201347372Y (en) | 2008-11-20 | 2008-11-20 | Water PH adjustable reverse osmosis device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2008201676986U CN201347372Y (en) | 2008-11-20 | 2008-11-20 | Water PH adjustable reverse osmosis device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201347372Y true CN201347372Y (en) | 2009-11-18 |
Family
ID=41366846
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNU2008201676986U Expired - Fee Related CN201347372Y (en) | 2008-11-20 | 2008-11-20 | Water PH adjustable reverse osmosis device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201347372Y (en) |
-
2008
- 2008-11-20 CN CNU2008201676986U patent/CN201347372Y/en not_active Expired - Fee Related
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103553212B (en) | A kind of high formaldehyde high concentrated organic wastewater biological treatment | |
CN202379821U (en) | Reverse osmosis water-saving device | |
CN204265580U (en) | novel ultra-pure water machine | |
CN101428913A (en) | Reverse osmosis water production process | |
CN101734756A (en) | System for automatically adjusting PH of reverse osmosis produced water | |
CN202754858U (en) | Water filter device | |
CN201439496U (en) | A reverse osmosis equipment for advanced treatment of industrial wastewater | |
CN201144167Y (en) | End-stage product water return type reverse osmosis device | |
CN201424394Y (en) | Reverse osmosis water quality automatic control system | |
CN202729930U (en) | Minitype reverse osmosis system | |
CN201347372Y (en) | Water PH adjustable reverse osmosis device | |
CN201801433U (en) | Concentrated water recovering system | |
CN201099634Y (en) | Energy-saving and water-saving two-stage reverse osmosis device | |
CN204173990U (en) | Reverse osmosis water purifying plant | |
CN204454802U (en) | A kind of film condensing device of improvement | |
CN2494822Y (en) | Secondary reverse osmosis water purifier | |
CN202671263U (en) | Water treatment system with secondary reverse osmosis concentrated water branch reflux | |
CN100594188C (en) | Water-saving improved process for anti-penetration water purifier | |
CN205442865U (en) | Seawater desalination's treatment facility | |
CN205528200U (en) | Novel system pure water reverse osmosis system | |
CN201525785U (en) | Commercial reverse osmosis water purifier with high recovery rate | |
CN207347194U (en) | One kind automation twin-stage adjusts chemicals dosing plant | |
CN205933483U (en) | Phosphate coating wastewater processing system | |
CN201670770U (en) | A double-membrane water purification device | |
CN204356116U (en) | A kind of high salt sewage hyperconcentration desalting treatment device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
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: 20091118 Termination date: 20111120 |