CN205988682U - A kind of enter liquid distributor for salt water preprocessor - Google Patents
A kind of enter liquid distributor for salt water preprocessor Download PDFInfo
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- CN205988682U CN205988682U CN201620965845.9U CN201620965845U CN205988682U CN 205988682 U CN205988682 U CN 205988682U CN 201620965845 U CN201620965845 U CN 201620965845U CN 205988682 U CN205988682 U CN 205988682U
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Abstract
本实用新型涉及一种用于盐水预处理器的进液分布器。本实用新型包括盐水预处理器的中心桶、进液管、环管以及布液管,所述布液管为两组,相对排布于中心桶外壁,每组布液管由两个单管组成并且呈V形排布,所述布液管出液口与中心桶相切连接;所述环管与布液管进液口连接,进液管与环管连接。盐水经过本实用新型的环管产生环流,通过布液管进入中心桶并发生涡流撞击混合,保证盐水混合均匀,实现盐水较好的絮凝、沉降、分离,从而保证盐水的精制效果。
The utility model relates to a liquid inlet distributor used for a salt water preprocessor. The utility model comprises a central barrel of a salt water preprocessor, a liquid inlet pipe, a ring pipe and a liquid distribution pipe. The liquid distribution pipes are two groups, which are relatively arranged on the outer wall of the central barrel. Each group of liquid distribution pipes consists of two single pipes. Composed and arranged in a V shape, the liquid outlet of the liquid distribution pipe is connected tangentially to the central barrel; the ring pipe is connected to the liquid inlet of the liquid distribution pipe, and the liquid inlet pipe is connected to the ring pipe. The brine passes through the ring pipe of the utility model to generate circulation, and enters the central barrel through the liquid distribution pipe, where eddy current impacts and mixes to ensure that the brine is evenly mixed, and realizes better flocculation, sedimentation, and separation of the brine, thereby ensuring the refining effect of the brine.
Description
技术领域technical field
本实用新型涉及一种用于盐水预处理器的进液分布器。The utility model relates to a liquid inlet distributor used for a salt water preprocessor.
背景技术Background technique
在离子膜氯碱生产中,盐水预处理器对盐水的精制过程是至关重要的工序,精制效果的好坏直接影响产品的质量和产量;现有的盐水预处理器一般采用单一进液,易发生进液不均造成预处理器絮凝和澄清区域出现偏流,部分区域盐水精制过程不理想,导致整体絮凝、漂浮、澄清效果不佳的情况,存在盐水精制效果不佳、设备利用效率不理想的缺陷。In ion-exchange membrane chlor-alkali production, the brine preprocessor is a crucial process for the brine refining process, and the quality of the refining effect directly affects the quality and output of the product; The occurrence of uneven liquid inlet causes bias flow in the flocculation and clarification area of the preprocessor, and the brine refining process in some areas is not ideal, resulting in poor overall flocculation, floating, and clarification effects. There are problems such as poor brine refining effect and unsatisfactory equipment utilization efficiency defect.
实用新型内容Utility model content
本实用新型的目的是针对现有技术存在的问题提供一种进液均匀的进液分布器。The purpose of the utility model is to provide a liquid-inlet distributor with uniform liquid-inlet aiming at the problems existing in the prior art.
本实用新型的具体技术方案如下:The concrete technical scheme of the utility model is as follows:
一种用于盐水预处理器的进液分布器,包括盐水预处理器的中心桶、进液管、环管以及布液管,所述布液管为两组,相对排布于中心桶外壁,每组布液管由两个单管组成并且呈V形排布,所述布液管出液口与中心桶相切连接;所述环管与布液管进液口连接,进液管与环管连接;A liquid inlet distributor for a brine preconditioner, including a central barrel, a liquid inlet pipe, a ring pipe, and a liquid distribution pipe for a brine preconditioner, the liquid distribution pipes are in two groups, arranged relatively on the outer wall of the central barrel , each group of liquid distribution pipes is composed of two single pipes and arranged in a V shape, the liquid outlet of the liquid distribution pipe is connected tangentially to the central barrel; the ring pipe is connected to the liquid inlet of the liquid distribution pipe, and the liquid inlet pipe connected to the ring pipe;
所述进液管数量为二,进液管与环管相切连接;The number of the liquid inlet pipes is two, and the liquid inlet pipes are connected tangentially to the annular pipe;
所述各进液管的切线方向相同。The tangent directions of the liquid inlet pipes are the same.
本实用新型具有以下有益效果:The utility model has the following beneficial effects:
盐水经过环管产生环流,通过布液管进入中心桶并发生涡流撞击混合,保证盐水混合均匀,实现盐水较好的絮凝、沉降、分离,从而保证盐水的精制效果。The brine passes through the ring pipe to generate a circulation, and enters the central barrel through the liquid distribution pipe, where vortex impacts and mixes to ensure that the brine is evenly mixed, and achieve better flocculation, sedimentation, and separation of the brine, thereby ensuring the refining effect of the brine.
附图说明Description of drawings
图1为本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
具体实施方式detailed description
如图1所示一种用于盐水预处理器的进液分布器,包括盐水预处理器的中心桶1、进液管2、环管3以及布液管4,所述布液管4为两组,相对排布于中心桶1外壁,每组布液管4由两个单管组成并且呈V形排布,所述布液管4出液口与中心桶1相切连接;所述环管3与布液管4进液口连接,进液管2与环管3连接,所述进液管2数量为二,进液管2与环管3相切连接,所述各进液管2的切线方向相同。As shown in Figure 1, a liquid inlet distributor for the brine preconditioner includes a central barrel 1 of the brine preconditioner, a liquid inlet pipe 2, a ring pipe 3 and a liquid distribution pipe 4, and the liquid distribution pipe 4 is Two groups are relatively arranged on the outer wall of the central barrel 1, and each group of liquid distribution pipes 4 is composed of two single pipes and arranged in a V shape, and the liquid outlets of the liquid distribution pipes 4 are connected tangentially to the central barrel 1; The ring pipe 3 is connected to the liquid inlet of the liquid distribution pipe 4, and the liquid inlet pipe 2 is connected to the ring pipe 3. The number of the liquid inlet pipes 2 is two, and the liquid inlet pipe 2 is connected to the ring pipe 3 tangentially. The tangents of tube 2 are in the same direction.
盐水通过进液管2输送至环管3内并沿环管3环形流动,环管3内的盐水通过布液管4输送进入中心桶1后继续保持环形进液状态,两组相对排布的布液管4输送的盐水在中心桶1内撞击形成涡流并最终均匀混合,解决了传统盐水预处理器进液不均而造成的整体絮凝、漂浮、澄清效果不佳的问题。The brine is transported into the ring pipe 3 through the liquid inlet pipe 2 and flows circularly along the ring pipe 3. The brine in the ring pipe 3 is sent into the central barrel 1 through the liquid distribution pipe 4 and then continues to maintain a circular liquid inlet state. Two groups of relatively arranged The brine transported by the liquid distribution pipe 4 collides in the central barrel 1 to form a vortex and finally mixes evenly, which solves the problem of poor overall flocculation, floating and clarification effects caused by uneven liquid intake in the traditional brine preprocessor.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620965845.9U CN205988682U (en) | 2016-08-29 | 2016-08-29 | A kind of enter liquid distributor for salt water preprocessor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620965845.9U CN205988682U (en) | 2016-08-29 | 2016-08-29 | A kind of enter liquid distributor for salt water preprocessor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205988682U true CN205988682U (en) | 2017-03-01 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620965845.9U Expired - Fee Related CN205988682U (en) | 2016-08-29 | 2016-08-29 | A kind of enter liquid distributor for salt water preprocessor |
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| Country | Link |
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| CN (1) | CN205988682U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109437380A (en) * | 2018-12-12 | 2019-03-08 | 重庆交通大学 | A kind of hydraulic cyclone formula sewage-treatment plant |
| CN113262655A (en) * | 2021-05-17 | 2021-08-17 | 华融化学股份有限公司 | Salt dissolving device capable of continuously providing crude salt water with stable concentration |
-
2016
- 2016-08-29 CN CN201620965845.9U patent/CN205988682U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109437380A (en) * | 2018-12-12 | 2019-03-08 | 重庆交通大学 | A kind of hydraulic cyclone formula sewage-treatment plant |
| CN113262655A (en) * | 2021-05-17 | 2021-08-17 | 华融化学股份有限公司 | Salt dissolving device capable of continuously providing crude salt water with stable concentration |
| CN113262655B (en) * | 2021-05-17 | 2022-11-01 | 华融化学股份有限公司 | Salt dissolving device capable of continuously providing crude salt water with stable concentration |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20170301 |