CN202379825U - Two-stage reverse osmosis device - Google Patents
Two-stage reverse osmosis device Download PDFInfo
- Publication number
- CN202379825U CN202379825U CN2011205456811U CN201120545681U CN202379825U CN 202379825 U CN202379825 U CN 202379825U CN 2011205456811 U CN2011205456811 U CN 2011205456811U CN 201120545681 U CN201120545681 U CN 201120545681U CN 202379825 U CN202379825 U CN 202379825U
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- CN
- China
- Prior art keywords
- reverse osmosis
- osmosis device
- water
- stage
- stage reverse
- 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
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- 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
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本实用新型公开了一种二级反渗透装置，包括依次管道连接的一级高压泵（1）、一级反渗透器（2）、二级高压泵（3）和二级反渗透器（4），所述的一级反渗透器（2）和二级高压泵（4）之间还设置有一个储水罐（5），二级反渗透器（4）的浓水排口（6）通过管道连接到储水罐（5），浓水排口（6）上设置有一个止回阀（8），储水罐（5）上还管道连接有一个碱液罐（8）。本实用新型的有益效果是：通过在向一级渗透器出的淡水通过脱气和添加碱液，从而减少了水中的CO2含量，使得导电率低于1μs/cm，满足了制药生产中所需纯水的要求，而且将二级浓水再次利用，避免产生浪费和污染。
The utility model discloses a two-stage reverse osmosis device, which comprises a first-stage high-pressure pump (1), a first-stage reverse osmosis device (2), a second-stage high-pressure pump (3) and a second-stage reverse osmosis device (4) which are sequentially connected by pipelines ), a water storage tank (5) is also arranged between the first-stage reverse osmosis device (2) and the second-stage high-pressure pump (4), and the concentrated water outlet (6) of the second-stage reverse osmosis device (4) It is connected to the water storage tank (5) through a pipeline, a check valve (8) is arranged on the concentrated water outlet (6), and an lye tank (8) is also connected to the water storage tank (5) by pipeline. The beneficial effects of the utility model are: by degassing and adding lye to the fresh water going out of the first-stage permeator, thereby reducing the CO2 content in the water, making the conductivity lower than 1 μs/cm, meeting the requirements in pharmaceutical production Pure water is required, and the secondary concentrated water is reused to avoid waste and pollution.
Description
Technical field
The utility model relates to a kind of purified water production equipment, particularly relates to a kind of two-pass reverse osmosis device.
Background technology
In the pharmaceutical manufacturing process, often need to use pure water pollution-free, free from foreign meter to carry out the preparation of soup.Current, use the two-pass reverse osmosis device to produce pure water more, the efficient of two-pass reverse osmosis device desalination is very high, but but can not remove the CO in anhydrating
2, the pure water electric conductivity of producing is too high, does not meet the requirement of required pure water in the pharmaceutical industry, and the two-pass reverse osmosis device produces general direct the secondary concentrated water drainage is bled off in process of production, has caused very big waste and pollution.
The utility model content
The purpose of the utility model promptly is to overcome the deficiency of present technology, and a kind of two-pass reverse osmosis device is provided, and the pure water that solves existing two-pass reverse osmosis device production is because of CO
2Too high levels causes the too high problem of electric conductivity, and the dense water of secondary is utilized once more, avoids producing waste and pollution.
The utility model is realized through following technical scheme: the two-pass reverse osmosis device; Comprise one-level HPP, first-stage reverse osmosis device, secondary HPP and the two-pass reverse osmosis device of pipe connection successively; Also be provided with a water tank between described first-stage reverse osmosis device and the secondary HPP; To water tank, concentrated water drainage mouth place is provided with a vacuum breaker to the concentrated water drainage mouth of two-pass reverse osmosis device through pipe connection, and going back pipe connection on the water tank has an alkali liquid tank.
The ingress of said one-level HPP is provided with a ultra-fine filter.
Pipeline is provided with a de-gassing vessel between said first-stage reverse osmosis device and the water tank.
Be provided with a volume pump between said alkali liquid tank and the water tank.
The beneficial effect of the utility model is: through at the fresh water that goes out to the one-level permeator through the degassing with add alkali lye, thereby reduced the CO in the water
2Content makes electric conductivity be lower than 1 μ s/cm, has satisfied the requirement of required pure water in the pharmaceutical manufacturing, and the dense water of secondary is utilized once more, has avoided producing waste and pollution.
Description of drawings
Fig. 1 is the structural representation of the utility model;
Among the figure, 1-one-level HPP, 2-first-stage reverse osmosis device, 3-secondary HPP, 4-two-pass reverse osmosis device, 5-water tank, 6-concentrated water drainage mouth, 7-vacuum breaker, 8-alkali liquid tank, 9-ultra-fine filter, 10-de-gassing vessel, 11-volume pump.
Embodiment
Below in conjunction with accompanying drawing the utility model is done further to specify:
As shown in Figure 1; The two-pass reverse osmosis device; Comprise one-level HPP 1, first-stage reverse osmosis device 2, secondary HPP 3 and the two-pass reverse osmosis device 4 of pipe connection successively, also be provided with a water tank 5 between described first-stage reverse osmosis device 2 and the secondary HPP 4, the concentrated water drainage mouth 6 of two-pass reverse osmosis device 4 arrives water tank 5 through pipe connection; Concentrated water drainage mouth 6 places are provided with a vacuum breaker 7, and going back pipe connection on the water tank 5 has an alkali liquid tank 8.
The ingress of said one-level HPP 1 is provided with a ultra-fine filter 9, and water inlet is filtered earlier, has increased the work-ing life of counter-osmosis device.
Pipeline is provided with a de-gassing vessel 10 between said first-stage reverse osmosis device 2 and the water tank 5, the fresh water that first-stage reverse osmosis device 2 is produced outgas processings, the CO in the minimizing water earlier
2Content, the throwing amount of minimizing alkali lye.
Be provided with a volume pump 11 between said alkali liquid tank 8 and the water tank 5, can reach the quantitative input of alkali lye.
The principle of work of the utility model: after water filters through ultra-fine filter 9; Be transported to first-stage reverse osmosis device 2 through one-level HPP 1 and handle, the one-level fresh water of the production of first-stage reverse osmosis device 2 is transported to water tank 5 after the de-gassing vessel degassing, and the water in the water tank 5 is carried out after pH value measures; Dropping into alkali lye through volume pump 11 neutralizes; Secondary HPP 3 is transported to the water in the water tank 5 and carries out primary treatment in the two-pass reverse osmosis device 4 again, and the secondary fresh water that two-pass reverse osmosis device 4 is produced promptly is qualified pure water, and the dense water of secondary that two-pass reverse osmosis device 4 is produced is back in the water tank 5 again and utilizes once more; Not only save resource; Reduce discharging, and the pH value of the dense water of secondary is higher than the pH value of one-level fresh water, can reduces the injected volume of alkali lye.
Claims (4)
1. two-pass reverse osmosis device; Comprise one-level HPP (1), first-stage reverse osmosis device (2), secondary HPP (3) and the two-pass reverse osmosis device (4) of pipe connection successively; It is characterized in that: also be provided with a water tank (5) between described first-stage reverse osmosis device (2) and the secondary HPP (4); The concentrated water drainage mouth (6) of two-pass reverse osmosis device (4) arrives water tank (5) through pipe connection; Concentrated water drainage mouth (6) locates to be provided with a vacuum breaker (7), and going back pipe connection on the water tank (5) has an alkali liquid tank (8).
2. two-pass reverse osmosis device according to claim 1 is characterized in that: the ingress of said one-level HPP (1) is provided with a ultra-fine filter (9).
3. two-pass reverse osmosis device according to claim 1 is characterized in that: pipeline is provided with a de-gassing vessel (10) between said first-stage reverse osmosis device (2) and the water tank (5).
4. two-pass reverse osmosis device according to claim 1 is characterized in that: be provided with a volume pump (11) between said alkali liquid tank (8) and the water tank (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205456811U CN202379825U (en) | 2011-12-23 | 2011-12-23 | Two-stage reverse osmosis device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205456811U CN202379825U (en) | 2011-12-23 | 2011-12-23 | Two-stage reverse osmosis device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202379825U true CN202379825U (en) | 2012-08-15 |
Family
ID=46628342
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205456811U Expired - Fee Related CN202379825U (en) | 2011-12-23 | 2011-12-23 | Two-stage reverse osmosis device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202379825U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103771562A (en) * | 2012-10-19 | 2014-05-07 | 中国石油化工股份有限公司 | Advanced treatment and reuse method of high-temperature nitrochlorobenzene wastewater |
| CN113045020A (en) * | 2021-04-06 | 2021-06-29 | 北京康安高分子开发中心 | Two-stage reverse osmosis water purifier |
-
2011
- 2011-12-23 CN CN2011205456811U patent/CN202379825U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103771562A (en) * | 2012-10-19 | 2014-05-07 | 中国石油化工股份有限公司 | Advanced treatment and reuse method of high-temperature nitrochlorobenzene wastewater |
| CN103771562B (en) * | 2012-10-19 | 2015-11-25 | 中国石油化工股份有限公司 | A kind of nitro-chlorobenzene hot wastewater advanced treatment and reuse method |
| CN113045020A (en) * | 2021-04-06 | 2021-06-29 | 北京康安高分子开发中心 | Two-stage reverse osmosis water purifier |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120815 Termination date: 20171223 |