CN202671263U - Water treatment system with secondary reverse osmosis concentrated water branch reflux - Google Patents
Water treatment system with secondary reverse osmosis concentrated water branch reflux Download PDFInfo
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- CN202671263U CN202671263U CN201220318576.9U CN201220318576U CN202671263U CN 202671263 U CN202671263 U CN 202671263U CN 201220318576 U CN201220318576 U CN 201220318576U CN 202671263 U CN202671263 U CN 202671263U
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- reverse osmosis
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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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Abstract
本实用新型公开了一种具有二级反渗透浓水分路回流的水处理系统,包括原水箱、一级反渗透组件和二级反渗透组件,在一级反渗透组件的出水口和二级反渗透组件的进水口之间设有高压泵,二级反渗透组件的浓水出口具有两条分路,一条分路与原水箱相连,另一条与高压泵的进水口相连。本实用新型将二级反渗透浓水分设两条不同的支路,使得一部分二级反渗透浓水回流至高压泵的进水口,可以提高二级反渗透膜表面流速,提高出水水质,还可以节省大量加碱费用;另一部分二级反渗透浓水回流至原水箱,这部分回流经混合后可以降低原水含盐量,避免因PH值增加对系统的影响,降低了维护保养的成本,提高了生产的效率。
The utility model discloses a water treatment system with two-stage reverse osmosis concentrated water circuit backflow, which comprises a raw water tank, a primary reverse osmosis component and a secondary reverse osmosis component. A high-pressure pump is arranged between the water inlets of the osmosis components, and the concentrated water outlet of the secondary reverse osmosis component has two branches, one branch is connected with the raw water tank, and the other is connected with the water inlet of the high-pressure pump. The utility model sets two different branches for the concentrated water of the secondary reverse osmosis, so that part of the concentrated water of the secondary reverse osmosis flows back to the water inlet of the high-pressure pump, which can increase the surface flow velocity of the secondary reverse osmosis membrane and improve the quality of the effluent. Save a lot of alkali addition costs; another part of the secondary reverse osmosis concentrated water returns to the raw water tank, and this part of the backflow can reduce the salt content of the raw water after mixing, avoiding the impact on the system due to the increase of the PH value, reducing the maintenance cost and improving the efficiency of production.
Description
技术领域 technical field
本实用新型涉及水处理设备的技术领域,尤其是一种具有二级反渗透浓水分路回流的水处理系统。The utility model relates to the technical field of water treatment equipment, in particular to a water treatment system with two-stage reverse osmosis concentrated water circuit backflow.
背景技术 Background technique
在公知的水处理技术领域,一级反渗透产水需进入二级反渗透系统,由于一级反渗透产水的电导率已经很低,而二级反渗透的回收率一般也比较高,所以二级反渗透的浓水的电导仪一般比原水电导率都要低很多,传统工艺在对二级反渗透浓水进行回用时是将二级反渗透浓水全部回流至原水箱,这样避免了二级反渗透浓水的排放浪费,但由于该浓水PH值较高,一般达到9-10,该水的回用对原水PH值有所影响,影响反渗透处理效果,而且在实际使用过程中容易造成一级反渗透膜的结垢从而造成膜元件的损坏,同时也给维护保养带了一些困难,增加生产成本。In the known field of water treatment technology, the first-stage reverse osmosis product water needs to enter the second-stage reverse osmosis system. Since the conductivity of the first-stage reverse osmosis product water is already very low, and the recovery rate of the second-stage reverse osmosis is generally relatively high, so The conductivity meter of the concentrated water of the secondary reverse osmosis is generally much lower than that of the raw water. The traditional process is to return all the concentrated water of the secondary reverse osmosis to the raw water tank when reusing the concentrated water of the secondary reverse osmosis, so as to avoid The discharge of the secondary reverse osmosis concentrated water is wasteful, but due to the high pH value of the concentrated water, generally reaching 9-10, the reuse of this water will affect the pH value of the raw water, affecting the effect of reverse osmosis treatment, and in the actual use process It is easy to cause fouling of the first-stage reverse osmosis membrane and damage the membrane elements. At the same time, it also brings some difficulties to maintenance and increases production costs.
实用新型内容 Utility model content
本实用新型要解决的技术问题是:提供一种能够充分利用二级反渗透浓水且不会损坏膜元件的水处理系统。The technical problem to be solved by the utility model is to provide a water treatment system that can make full use of the secondary reverse osmosis concentrated water without damaging the membrane elements.
本实用新型解决其技术问题所采用的技术方案是:一种具有二级反渗透浓水分路回流的水处理系统,包括原水箱、一级反渗透组件和二级反渗透组件,在所述的一级反渗透组件的出水口和二级反渗透组件的进水口之间设有高压泵,所述的二级反渗透组件的浓水出口具有两条分路,一条分路与原水箱相连,另一条与高压泵的进水口相连。The technical solution adopted by the utility model to solve the technical problem is: a water treatment system with two-stage reverse osmosis concentrated water circuit backflow, including a raw water tank, a primary reverse osmosis component and a secondary reverse osmosis component. A high-pressure pump is provided between the water outlet of the primary reverse osmosis component and the water inlet of the secondary reverse osmosis component. The concentrated water outlet of the secondary reverse osmosis component has two shunts, one of which is connected to the raw water tank, The other is connected to the water inlet of the high pressure pump.
进一步的,为了方便调节二级反渗透浓水指向原水箱的流量,本实用新型在所述的二级反渗透组件的浓水出口与原水箱相连的分路上设有回流阀。Further, in order to conveniently adjust the flow rate of the secondary reverse osmosis concentrated water to the raw water tank, the utility model is provided with a return valve on the branch road where the concentrated water outlet of the secondary reverse osmosis component is connected to the raw water tank.
进一步的,为了方便调节二级反渗透浓水指向高压泵进水口的流量,本实用新型在所述的二级反渗透组件的浓水出口与高压泵的进水口相连的分路上设有回流阀。Further, in order to conveniently adjust the flow rate of the secondary reverse osmosis concentrated water pointing to the water inlet of the high-pressure pump, the utility model is provided with a return valve on the branch road where the concentrated water outlet of the secondary reverse osmosis component is connected to the water inlet of the high-pressure pump .
本实用新型的有益效果是:本实用新型将二级反渗透浓水分设两条不同的支路,使得一部分二级反渗透浓水回流至高压泵的进水口,可以提高二级反渗透膜表面流速,减少浓差极化,提高出水水质,另由于此二级反渗透浓水PH值较高,一般达到9-10,而一级反渗透出水因二氧化碳气体无法去除导致PH值较低,一般为6-6.5,因此该部分浓水回流可以节省甚至省略二级反渗透进水的加碱,从而节省大量加碱费用;另一部分二级反渗透浓水回流至原水箱,这部分回流经混合后可以降低原水含盐量,同时另由于回流的浓水量减少,使高PH值浓水对原水PH值的影响大大减少,可避免因PH值增加对系统的影响,如膜结垢堵塞等,降低了维护保养的成本,提高了生产的效率。The beneficial effects of the utility model are: the utility model sets two different branches for the secondary reverse osmosis concentrated water, so that a part of the secondary reverse osmosis concentrated water flows back to the water inlet of the high-pressure pump, which can improve the surface of the secondary reverse osmosis membrane. The flow rate can reduce the concentration polarization and improve the effluent water quality. In addition, the PH value of the secondary reverse osmosis concentrated water is relatively high, generally reaching 9-10, while the PH value of the primary reverse osmosis effluent is low due to the inability to remove carbon dioxide gas. 6-6.5, so this part of the concentrated water backflow can save or even omit the alkali addition of the secondary reverse osmosis feed water, thereby saving a lot of alkali addition costs; another part of the secondary reverse osmosis concentrated water is returned to the original water tank, and this part of the return flow is mixed Finally, the salt content of the raw water can be reduced. At the same time, due to the reduction of the concentrated water backflow, the impact of the concentrated water with a high pH value on the pH value of the raw water is greatly reduced, and the impact on the system due to the increase in the pH value can be avoided, such as membrane fouling and blockage. The cost of maintenance is reduced and the efficiency of production is improved.
附图说明 Description of drawings
下面结合附图和实施例对本实用新型进一步说明。Below in conjunction with accompanying drawing and embodiment the utility model is further described.
图1是本实用新型的结构示意图。Fig. 1 is a structural representation of the utility model.
图中:1.原水箱,2.一级反渗透组件,3.二级反渗透组件,4.高压泵。In the figure: 1. Raw water tank, 2. Primary reverse osmosis component, 3. Secondary reverse osmosis component, 4. High pressure pump.
具体实施方式 Detailed ways
现在结合附图对本实用新型作进一步详细的说明。这些附图均为简化的示意图,仅以示意方式说明本实用新型的基本结构,因此其仅显示与本实用新型有关的构成。Now in conjunction with accompanying drawing, the utility model is described in further detail. These drawings are all simplified schematic diagrams, and only schematically illustrate the basic structure of the utility model, so they only show the configurations related to the utility model.
如图1所示的本实用新型一种具有二级反渗透浓水分路回流的水处理系统,包括原水箱1、一级反渗透组件2和二级反渗透组件3,在所述的一级反渗透组件2的出水口和二级反渗透组件3的进水口之间设有高压泵4,所述的二级反渗透组件3的浓水出口具有两条分路,一条分路与原水箱1相连,另一条与高压泵4的进水口相连;同时所述的二级反渗透组件3的浓水出口与原水箱1相连的分路上设有回流阀,所述的二级反渗透组件3的浓水出口与高压泵4的进水口相连的分路上也设有回流阀。As shown in Figure 1, a water treatment system of the present utility model with two-stage reverse osmosis concentrated water circuit backflow includes a
以上述依据本实用新型的理想实施例为启示,通过上述的说明内容,相关工作人员完全可以在不偏离本项实用新型技术思想的范围内,进行多样的变更以及修改。本项实用新型的技术性范围并不局限于说明书上的内容,必须要根据权利要求范围来确定其技术性范围。Inspired by the above ideal embodiment according to the utility model, through the above description content, relevant staff can completely make various changes and modifications within the scope of not deviating from the technical idea of the utility model. The technical scope of this utility model is not limited to the content in the description, but must be determined according to the scope of the claims.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201220318576.9U CN202671263U (en) | 2012-06-30 | 2012-06-30 | Water treatment system with secondary reverse osmosis concentrated water branch reflux |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201220318576.9U CN202671263U (en) | 2012-06-30 | 2012-06-30 | Water treatment system with secondary reverse osmosis concentrated water branch reflux |
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| CN202671263U true CN202671263U (en) | 2013-01-16 |
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| CN201220318576.9U Expired - Fee Related CN202671263U (en) | 2012-06-30 | 2012-06-30 | Water treatment system with secondary reverse osmosis concentrated water branch reflux |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103752155A (en) * | 2013-12-31 | 2014-04-30 | 上海宝钢磁业有限公司 | Method for spraying and neutralizing by wastewater generated in pure water preparation |
| CN112811699A (en) * | 2021-01-27 | 2021-05-18 | 恒安(重庆)生活用纸有限公司 | Reverse osmosis purification backwater device |
-
2012
- 2012-06-30 CN CN201220318576.9U patent/CN202671263U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103752155A (en) * | 2013-12-31 | 2014-04-30 | 上海宝钢磁业有限公司 | Method for spraying and neutralizing by wastewater generated in pure water preparation |
| CN112811699A (en) * | 2021-01-27 | 2021-05-18 | 恒安(重庆)生活用纸有限公司 | Reverse osmosis purification backwater device |
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| 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 |
Granted publication date: 20130116 Termination date: 20150630 |
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| EXPY | Termination of patent right or utility model |
