CN202265462U - Energy recovery and desalination system by plunger pump - Google Patents
Energy recovery and desalination system by plunger pump Download PDFInfo
- Publication number
- CN202265462U CN202265462U CN2011203673541U CN201120367354U CN202265462U CN 202265462 U CN202265462 U CN 202265462U CN 2011203673541 U CN2011203673541 U CN 2011203673541U CN 201120367354 U CN201120367354 U CN 201120367354U CN 202265462 U CN202265462 U CN 202265462U
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- pressure
- energy recovery
- reverse osmosis
- pump
- osmosis membrane
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- 238000011084 recovery Methods 0.000 title claims abstract description 32
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 43
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 22
- 239000012528 membrane Substances 0.000 claims abstract description 19
- 239000013505 freshwater Substances 0.000 claims abstract description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- 238000001914 filtration Methods 0.000 claims 4
- 230000003139 buffering effect Effects 0.000 claims 2
- 238000000034 method Methods 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000010586 diagram Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
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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采用柱塞泵的能量回收淡化系统,旨在提供一种工作稳定、成本较低、工艺结构简化的采用柱塞泵的能量回收淡化系统。本实用新型包括能量回收装置(5)及依次连接的供水泵(1)、预处理装置(2)、柱塞式高压泵(3)、反渗透膜组件(4),所述能量回收装置(5)设有低压进水口(51)、高压出水口(52)、高压进水口(53)、低压排放口(54),所述低压进水口(51)与预处理装置(2)连接,所述高压出水口(52)与柱塞式高压泵(3)连接,高压进水口(53)与反渗透膜组件(4)连接,低压排放口(54)为浓水排放口,反渗透膜组件(4)连接有淡水口(41)。本实用新型可广泛应用于反渗透苦咸水淡化制造领域。
The utility model discloses an energy recovery and desalination system using a plunger pump, aiming at providing an energy recovery and desalination system using a plunger pump with stable operation, low cost and simplified process structure. The utility model comprises an energy recovery device (5), a water supply pump (1), a pretreatment device (2), a plunger type high-pressure pump (3), and a reverse osmosis membrane module (4) connected in sequence. The energy recovery device ( 5) A low-pressure water inlet (51), a high-pressure water outlet (52), a high-pressure water inlet (53), and a low-pressure discharge port (54) are provided, and the low-pressure water inlet (51) is connected to the pretreatment device (2). The high-pressure water outlet (52) is connected to the plunger type high-pressure pump (3), the high-pressure water inlet (53) is connected to the reverse osmosis membrane module (4), the low-pressure discharge port (54) is the concentrated water discharge port, and the reverse osmosis membrane module (4) It is connected with a fresh water port (41). The utility model can be widely used in the field of reverse osmosis brackish water desalination manufacturing.
Description
技术领域 technical field
本实用新型涉及一种采用柱塞泵的能量回收淡化系统。 The utility model relates to an energy recovery and desalination system adopting a plunger pump.
背景技术 Background technique
在反渗透系统中越来越注重能量回收功能的应用,能量回收装置的合理应用能够节约部分能源,以达到节能的目标,在现有的能量回收系统中,高压泵的应用基本上以离心式高压泵为主,辅助离心式增压泵及能量回收装置,组成整套系统,此种能量回收装置所采用的高压离心泵利用变频控制,流量及压力比较难以控制,因此工作状态不稳定,且在运行中存在成本较高、工艺相对复杂的技术缺陷。 In the reverse osmosis system, more and more attention is paid to the application of energy recovery function. The reasonable application of energy recovery device can save part of the energy to achieve the goal of energy saving. In the existing energy recovery system, the application of high-pressure pump is basically based on centrifugal high-pressure The pump is the main part, and the auxiliary centrifugal booster pump and energy recovery device form a complete system. The high-pressure centrifugal pump used in this energy recovery device is controlled by frequency conversion, and the flow and pressure are difficult to control, so the working state is unstable. There are technical defects such as high cost and relatively complicated process.
实用新型内容 Utility model content
本实用新型所要解决的技术问题是克服现有技术的不足,提供一种工作稳定、成本较低、工艺结构简化的采用柱塞泵的能量回收淡化系统。 The technical problem to be solved by the utility model is to overcome the deficiencies of the prior art and provide an energy recovery and desalination system using a plunger pump with stable operation, low cost and simplified process structure.
本实用新型所采用的技术方案是:本实用新型包括供水泵、预处理装置、反渗透膜组件,所述采用柱塞泵的能量回收淡化系统还包括柱塞式高压泵、能量回收装置,所述供水泵、预处理装置、柱塞式高压泵、反渗透膜组件依次连接,所述能量回收装置设有低压进水口、高压出水口、高压进水口、低压排放口,所述低压进水口与所述预处理装置连接,所述高压出水口与所述柱塞式高压泵连接,高压进水口与所述反渗透膜组件连接,所述低压排放口为浓水排放口,所述反渗透膜组件连接有淡水口。 The technical scheme adopted by the utility model is: the utility model includes a water supply pump, a pretreatment device, and a reverse osmosis membrane module, and the energy recovery and desalination system using a plunger pump also includes a plunger type high-pressure pump and an energy recovery device. The water supply pump, pretreatment device, plunger-type high-pressure pump, and reverse osmosis membrane module are sequentially connected, and the energy recovery device is provided with a low-pressure water inlet, a high-pressure water outlet, a high-pressure water inlet, and a low-pressure discharge port. The low-pressure water inlet and The pretreatment device is connected, the high-pressure water outlet is connected to the plunger type high-pressure pump, the high-pressure water inlet is connected to the reverse osmosis membrane module, the low-pressure discharge port is a concentrated water discharge port, and the reverse osmosis membrane The components are connected with a fresh water port.
所述柱塞式高压泵与所述反渗透膜组件之间设有缓冲管路。 A buffer pipeline is provided between the plunger type high-pressure pump and the reverse osmosis membrane module.
所述能量回收装置与缓冲管路之间设有增压泵。 A booster pump is provided between the energy recovery device and the buffer pipeline.
所述预处理装置包括一级过滤装置,所述一级过滤装置包括依次连接的多介质过滤器、活性炭过滤器。 The pretreatment device includes a primary filter device, and the primary filter device includes a multimedia filter and an activated carbon filter connected in sequence.
所述预处理装置还包括二级过滤装置,所述二级过滤装置包括依次连接的保安过滤器和精密过滤器。 The pretreatment device also includes a secondary filter device, and the secondary filter device includes a security filter and a precision filter connected in sequence.
本实用新型的有益效果是:本实用新型中所采用的高压柱塞泵属于定量类型泵,流量恒定,只要设定好转速,流量就保持不变,工作状态稳定可靠,电器控制及变频设置比较简单,与现有的离心高压泵相比,本实用新型的高压柱塞泵的性价比较高,工作运行时稳定性好,并且工艺结构得到有效简化和优化,整体运行成本较低。 The beneficial effects of the utility model are: the high-pressure plunger pump used in the utility model belongs to the quantitative type pump, the flow rate is constant, as long as the speed is set, the flow rate remains unchanged, the working state is stable and reliable, and the electrical control and frequency conversion settings are relatively Simple, compared with the existing centrifugal high-pressure pump, the high-pressure plunger pump of the utility model has higher cost performance, better stability during operation, and the process structure is effectively simplified and optimized, and the overall operating cost is lower.
附图说明 Description of drawings
图1是本实用新型的方框示意图; Fig. 1 is a schematic block diagram of the utility model;
图2是本实用新型另一方框示意图 Fig. 2 is another block diagram of the utility model
图3是本实用新型的连接结构示意图。 Fig. 3 is a schematic diagram of the connection structure of the present invention.
具体实施方式 Detailed ways
如图1、图3所示,本实用新型包括供水泵1、预处理装置2、反渗透膜组件4,所述采用柱塞泵的能量回收淡化系统还包括柱塞式高压泵3、能量回收装置5,所述供水泵1、预处理装置2、柱塞式高压泵3、反渗透膜组件4依次连接,所述能量回收装置5设有低压进水口51、高压出水口52、高压进水口53、低压排放口54,所述低压进水口51与所述预处理装置2连接,所述高压出水口52与所述柱塞式高压泵3连接,高压进水口53与所述反渗透膜组件4连接,所述低压排放口54为浓水排放口,所述反渗透膜组件4连接有淡水口41。
As shown in Figures 1 and 3, the utility model includes a
如图2所示,所述柱塞式高压泵3与所述反渗透膜组件4之间设有缓冲管路31。所述能量回收装置5与缓冲管路31之间设有增压泵32,用于增大压力,提高效率。
As shown in FIG. 2 , a
所述预处理装置2包括一级过滤装置,所述一级过滤装置包括依次连接的多介质过滤器21、活性炭过滤器22。
The
所述预处理装置2还包括二级过滤装置,所述二级过滤装置包括依次连接的保安过滤器23和精密过滤器24。
The
实施时,由所述供水泵1接通电源进行供水,原水经过所述预处理装置2中的多介质过滤器21、活性碳过滤器22、保安过滤器23、精密过滤器24依次进行过滤,然后分流,其中一部分原水进入所述柱塞式高压泵3加压;另一部分原水经过能量回收装置5低压进水口51进入能量回收装置,通过能量回收装置5和浓水压力交换成高压原水,通过能量回收装置5高压出水口52进入增压泵32增压与柱塞式高压泵3出水一起进入反渗透膜组件4进行淡化处理,所产生的淡水经淡水口41储存,所产淡水可达到国家生活用水水质要求,所产水的浓水经能量回收装置5的高压进水口53与原水交换压力后通过能量回收装置低压排放口54排放。
During implementation, the
本实用新型可广泛应用于反渗透苦咸水淡化制造领域。 The utility model can be widely used in the field of reverse osmosis brackish water desalination manufacturing.
Claims (5)
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203673541U CN202265462U (en) | 2011-09-30 | 2011-09-30 | Energy recovery and desalination system by plunger pump |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203673541U CN202265462U (en) | 2011-09-30 | 2011-09-30 | Energy recovery and desalination system by plunger pump |
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| CN202265462U true CN202265462U (en) | 2012-06-06 |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102838186A (en) * | 2012-07-31 | 2012-12-26 | 朱荣辉 | Membrane seawater desalination pressurization and energy recovery integrated method and device |
| CN102951704A (en) * | 2012-11-14 | 2013-03-06 | 中冶海水淡化投资有限公司 | Reverse osmosis seawater desalination process and device thereof |
| CN103910442A (en) * | 2013-01-08 | 2014-07-09 | 株式会社日立制作所 | Fresh water system |
| CN104341050A (en) * | 2013-07-26 | 2015-02-11 | 中国电力工程顾问集团公司 | Seawater desalination system and method |
| CN104386782A (en) * | 2014-11-21 | 2015-03-04 | 陕西省石油化工研究设计院 | Energy-saving high-salt reverse osmosis device |
| CN104667749A (en) * | 2015-02-14 | 2015-06-03 | 张英华 | Energy recoverer and method for increasing water yield of reverse osmosis sea water desalination device |
| CN104671351A (en) * | 2013-12-02 | 2015-06-03 | 株式会社日立制作所 | Sea water desalination system |
-
2011
- 2011-09-30 CN CN2011203673541U patent/CN202265462U/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102838186A (en) * | 2012-07-31 | 2012-12-26 | 朱荣辉 | Membrane seawater desalination pressurization and energy recovery integrated method and device |
| CN102951704A (en) * | 2012-11-14 | 2013-03-06 | 中冶海水淡化投资有限公司 | Reverse osmosis seawater desalination process and device thereof |
| CN102951704B (en) * | 2012-11-14 | 2014-07-09 | 中冶海水淡化投资有限公司 | Reverse osmosis seawater desalination process and device thereof |
| CN103910442A (en) * | 2013-01-08 | 2014-07-09 | 株式会社日立制作所 | Fresh water system |
| CN104341050A (en) * | 2013-07-26 | 2015-02-11 | 中国电力工程顾问集团公司 | Seawater desalination system and method |
| CN104341050B (en) * | 2013-07-26 | 2016-08-10 | 中国电力工程顾问集团有限公司 | Seawater desalination system and method |
| CN104671351A (en) * | 2013-12-02 | 2015-06-03 | 株式会社日立制作所 | Sea water desalination system |
| CN104386782A (en) * | 2014-11-21 | 2015-03-04 | 陕西省石油化工研究设计院 | Energy-saving high-salt reverse osmosis device |
| CN104667749A (en) * | 2015-02-14 | 2015-06-03 | 张英华 | Energy recoverer and method for increasing water yield of reverse osmosis sea water desalination device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C53 | Correction of patent of invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Zhan Xiangdong Inventor after: Shi Junjie Inventor after: Ji Wei Inventor after: Guo Xuguo Inventor before: Shi Junjie |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: SHI JUNJIE TO: ZHAN XIANGDONG SHI JUNJIE QU WEI GUO XUGUO |
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| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120606 |
