CN203976507U - The water treatment system that reverse osmosis is degassed - Google Patents
The water treatment system that reverse osmosis is degassed Download PDFInfo
- Publication number
- CN203976507U CN203976507U CN201420337902.XU CN201420337902U CN203976507U CN 203976507 U CN203976507 U CN 203976507U CN 201420337902 U CN201420337902 U CN 201420337902U CN 203976507 U CN203976507 U CN 203976507U
- Authority
- CN
- China
- Prior art keywords
- reverse osmosis
- tubular fibre
- membrane component
- circulation tube
- degassing membrane
- 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 - Lifetime
Links
- 238000001223 reverse osmosis Methods 0.000 title claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 18
- 238000007872 degassing Methods 0.000 claims abstract description 25
- 239000000835 fiber Substances 0.000 claims abstract description 25
- 239000012528 membrane Substances 0.000 claims abstract description 22
- 230000000694 effects Effects 0.000 abstract description 5
- 238000010276 construction Methods 0.000 abstract description 3
- 238000004140 cleaning Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to a kind of water treatment system, relates in particular to the degassed water treatment system of a kind of reverse osmosis, is applicable to water and purifies.Comprise first-stage reverse osmosis, two-pass reverse osmosis, tubular fibre degassing membrane component and circulation tube, described first-stage reverse osmosis is connected with precision safety strainer, in described circulation tube, be provided with tubular fibre degassing membrane component, one end of described circulation tube is connected with precision safety strainer, the other end of described circulation tube is connected with two-pass reverse osmosis, in described circulation tube, be provided with recycle pump, one end of described tubular fibre degassing membrane component is connected with inlet end, and the other end of described tubular fibre degassing membrane component is connected with exhaust side.The water treatment system compact construction that reverse osmosis is degassed, improves treatment effect.
Description
Technical field
The utility model relates to a kind of water treatment system, relates in particular to the degassed water treatment system of a kind of reverse osmosis, is applicable to water and purifies.
Background technology
Prior art water treating equipment are wide in variety, and same equipment volume is increasing, and the effect that can reach is not very desirable.
Chinese patent 201310341147.2, discloses a kind of aerating system that can on-line cleaning, for sewage treatment industry.It comprises the diaphragm that is provided with self-closing micropore, and described diaphragm is tubular, and in tubular film, being provided with can the reciprocating stay cord in left and right, is installed with the hairbrush that can clean diaphragm on stay cord.Complex structure, treatment effect is undesirable.
Utility model content
The utility model is mainly to solve the deficiencies in the prior art, and a kind of compact construction is provided, and can effectively carry out purifying treatment to water, reaches the degassed water treatment system of reverse osmosis of use standard.
Above-mentioned technical problem of the present utility model is mainly solved by following technical proposals:
The water treatment system that a kind of reverse osmosis is degassed, comprise first-stage reverse osmosis, two-pass reverse osmosis, tubular fibre degassing membrane component and circulation tube, described first-stage reverse osmosis is connected with precision safety strainer, in described circulation tube, be provided with tubular fibre degassing membrane component, one end of described circulation tube is connected with precision safety strainer, the other end of described circulation tube is connected with two-pass reverse osmosis, in described circulation tube, be provided with recycle pump, one end of described tubular fibre degassing membrane component is connected with inlet end, the other end of described tubular fibre degassing membrane component is connected with exhaust side.
As preferably, described tubular fibre degassing membrane component is composed in parallel by 5 tubular fibre degassing films.
First-stage reverse osmosis produces water and is delivered to tubular fibre degassing membrane component through precision safety strainer,
Through the degassed two-pass reverse osmosis of delivering to.
It is gas purging formula that tubular fibre degassing membrane component adopts degassed mode, and source of the gas is oil-free compressed air.
Tubular fibre degassing membrane component is realized internal recycle to increase hydraulic detention time through recycle pump, improves degasifying effect.
Therefore, the water treatment system that reverse osmosis of the present utility model is degassed, compact construction, improves treatment effect.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
Below by embodiment, and by reference to the accompanying drawings, the technical solution of the utility model is described in further detail.
Embodiment 1: as shown in Figure 1, the water treatment system that a kind of reverse osmosis is degassed, comprise first-stage reverse osmosis 1, two-pass reverse osmosis 2, tubular fibre degassing membrane component 3 and circulation tube 4, described first-stage reverse osmosis 1 is connected with precision safety strainer 5, in described circulation tube 4, be provided with tubular fibre degassing membrane component 3, one end of described circulation tube 4 is connected with precision safety strainer 5, the other end of described circulation tube 4 is connected with two-pass reverse osmosis 2, in described circulation tube 4, be provided with recycle pump 6, one end of described tubular fibre degassing membrane component 3 is connected with inlet end 7, the other end of described tubular fibre degassing membrane component 3 is connected with exhaust side 8.
Described tubular fibre degassing membrane component 3 is composed in parallel by 5 tubular fibre degassing films.
Claims (2)
1. the water treatment system that reverse osmosis is degassed, it is characterized in that: comprise first-stage reverse osmosis (1), two-pass reverse osmosis (2), tubular fibre degassing membrane component (3) and circulation tube (4), described first-stage reverse osmosis (1) is connected with precision safety strainer (5), in described circulation tube (4), be provided with tubular fibre degassing membrane component (3), one end of described circulation tube (4) is connected with precision safety strainer (5), the other end of described circulation tube (4) is connected with two-pass reverse osmosis (2), in described circulation tube (4), be provided with recycle pump (6), one end of described tubular fibre degassing membrane component (3) is connected with inlet end (7), the other end of described tubular fibre degassing membrane component (3) is connected with exhaust side (8).
2. the degassed water treatment system of reverse osmosis according to claim 1, is characterized in that: described tubular fibre degassing membrane component (3) is composed in parallel by 5 tubular fibre degassing films.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420337902.XU CN203976507U (en) | 2014-06-24 | 2014-06-24 | The water treatment system that reverse osmosis is degassed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420337902.XU CN203976507U (en) | 2014-06-24 | 2014-06-24 | The water treatment system that reverse osmosis is degassed |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203976507U true CN203976507U (en) | 2014-12-03 |
Family
ID=51973971
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420337902.XU Expired - Lifetime CN203976507U (en) | 2014-06-24 | 2014-06-24 | The water treatment system that reverse osmosis is degassed |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203976507U (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104556571A (en) * | 2014-12-25 | 2015-04-29 | 武汉凯迪工程技术研究总院有限公司 | Recycling treatment process and system for wastewater in Fischer-Tropsch synthesis reaction |
| CN106256781A (en) * | 2015-06-18 | 2016-12-28 | 中国石油化工股份有限公司 | A kind of reinjection treatment method up to standard of oil gas field wastewater with high concentration of sulfide |
| CN106256780A (en) * | 2015-06-18 | 2016-12-28 | 中国石油化工股份有限公司 | A kind of reinjection treatment method up to standard of the wastewater with high concentration of sulfide of oil gas field |
| CN106256784A (en) * | 2015-06-18 | 2016-12-28 | 中国石油化工股份有限公司 | A kind of recycling processing method of wastewater with high concentration of sulfide |
| CN106256778A (en) * | 2015-06-18 | 2016-12-28 | 中国石油化工股份有限公司 | A kind of process for deep desulphurization of oil gas field wastewater with high concentration of sulfide |
| CN106256782A (en) * | 2015-06-18 | 2016-12-28 | 中国石油化工股份有限公司 | A kind of processing method of oil gas field wastewater with high concentration of sulfide |
| CN106698733A (en) * | 2015-11-12 | 2017-05-24 | 中国石油化工股份有限公司 | Deep desulfurization method for high-sulfur-containing wastewater of oil and gas field |
| CN107285503A (en) * | 2016-04-11 | 2017-10-24 | 中国石油化工股份有限公司 | Oil gas field wastewater with high concentration of sulfide reduces standard discharge method |
| CN107285504A (en) * | 2016-04-11 | 2017-10-24 | 中国石油化工股份有限公司 | Oil gas field wastewater with high concentration of sulfide reduces standard discharge processing method |
| CN107285505A (en) * | 2016-04-11 | 2017-10-24 | 中国石油化工股份有限公司 | A kind of oil gas field wastewater with high concentration of sulfide reduces standard discharge method |
-
2014
- 2014-06-24 CN CN201420337902.XU patent/CN203976507U/en not_active Expired - Lifetime
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104556571A (en) * | 2014-12-25 | 2015-04-29 | 武汉凯迪工程技术研究总院有限公司 | Recycling treatment process and system for wastewater in Fischer-Tropsch synthesis reaction |
| CN106256781A (en) * | 2015-06-18 | 2016-12-28 | 中国石油化工股份有限公司 | A kind of reinjection treatment method up to standard of oil gas field wastewater with high concentration of sulfide |
| CN106256780A (en) * | 2015-06-18 | 2016-12-28 | 中国石油化工股份有限公司 | A kind of reinjection treatment method up to standard of the wastewater with high concentration of sulfide of oil gas field |
| CN106256784A (en) * | 2015-06-18 | 2016-12-28 | 中国石油化工股份有限公司 | A kind of recycling processing method of wastewater with high concentration of sulfide |
| CN106256778A (en) * | 2015-06-18 | 2016-12-28 | 中国石油化工股份有限公司 | A kind of process for deep desulphurization of oil gas field wastewater with high concentration of sulfide |
| CN106256782A (en) * | 2015-06-18 | 2016-12-28 | 中国石油化工股份有限公司 | A kind of processing method of oil gas field wastewater with high concentration of sulfide |
| CN106698733A (en) * | 2015-11-12 | 2017-05-24 | 中国石油化工股份有限公司 | Deep desulfurization method for high-sulfur-containing wastewater of oil and gas field |
| CN107285503A (en) * | 2016-04-11 | 2017-10-24 | 中国石油化工股份有限公司 | Oil gas field wastewater with high concentration of sulfide reduces standard discharge method |
| CN107285504A (en) * | 2016-04-11 | 2017-10-24 | 中国石油化工股份有限公司 | Oil gas field wastewater with high concentration of sulfide reduces standard discharge processing method |
| CN107285505A (en) * | 2016-04-11 | 2017-10-24 | 中国石油化工股份有限公司 | A kind of oil gas field wastewater with high concentration of sulfide reduces standard discharge method |
| CN107285504B (en) * | 2016-04-11 | 2020-02-18 | 中国石油化工股份有限公司 | Method for treating high-sulfur-content wastewater in oil and gas field by reducing injection and reaching standard |
| CN107285505B (en) * | 2016-04-11 | 2020-02-18 | 中国石油化工股份有限公司 | Method for emission of high-sulfur-content wastewater of oil and gas field by reducing injection and reaching standard |
| CN107285503B (en) * | 2016-04-11 | 2020-02-18 | 中国石油化工股份有限公司 | Method for discharging high-sulfur-content wastewater of oil and gas field after injection reduction and reaching standards |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: Hangzhou City, Zhejiang Province, 311201 blocks south of Xiaoshan economic and Technological Development Zone Hengsheng Road No. 1 Patentee after: SONGYUAN MACHINERY MANUFACTURING Co.,Ltd. Address before: Hangzhou City, Zhejiang Province, 311201 blocks south of Xiaoshan economic and Technological Development Zone Hengsheng Road No. 1 Patentee before: HANGZHOU PINERICH MACHINERY MANUFACTURING CO.,LTD. |
|
| CX01 | Expiry of patent term |
Granted publication date: 20141203 |