CN204752506U - Mud -water separation system - Google Patents
Mud -water separation system Download PDFInfo
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- CN204752506U CN204752506U CN201520320997.9U CN201520320997U CN204752506U CN 204752506 U CN204752506 U CN 204752506U CN 201520320997 U CN201520320997 U CN 201520320997U CN 204752506 U CN204752506 U CN 204752506U
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- mud
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- water separation
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 69
- 238000000926 separation method Methods 0.000 title claims abstract description 41
- 238000004062 sedimentation Methods 0.000 claims abstract description 20
- 238000002156 mixing Methods 0.000 claims abstract description 19
- 238000000746 purification Methods 0.000 claims abstract description 12
- 239000007788 liquid Substances 0.000 claims description 28
- 238000012806 monitoring device Methods 0.000 claims description 13
- 239000002893 slag Substances 0.000 claims description 4
- 230000032258 transport Effects 0.000 claims description 4
- 238000012544 monitoring process Methods 0.000 claims description 3
- 238000001514 detection method Methods 0.000 claims 2
- 238000001914 filtration Methods 0.000 abstract description 3
- 239000003818 cinder Substances 0.000 abstract 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 4
- 235000011941 Tilia x europaea Nutrition 0.000 description 4
- 239000004571 lime Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011085 pressure filtration Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
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- Treatment Of Sludge (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及一种可将泥水进行分离处理的泥水分离系统。 The utility model relates to a mud-water separation system capable of separating mud water.
背景技术 Background technique
传统泥浆分离系统一般包括絮凝池、泥浆压滤装置和排水装置,其中泥浆进入絮凝池后需要人工投入絮凝剂和石灰等,由于絮凝剂和石灰与泥浆的混合需要较为均匀才能够达到理想的泥水分离分层效果,但是人工搅拌混合基本达不到均匀混合的要求。 The traditional mud separation system generally includes a flocculation tank, a mud filter press device and a drainage device. After the mud enters the flocculation tank, flocculant and lime need to be manually added. Because the mixing of the flocculant and lime with the mud needs to be relatively uniform to achieve the ideal muddy water Separation and stratification effect, but manual stirring and mixing basically cannot meet the requirements of uniform mixing.
实用新型内容 Utility model content
鉴于背景技术存在的不足,本实用新型所要解决的技术问题是提供一种能够更好地实现泥水分离的泥水分离系统。 In view of the deficiencies in the background technology, the technical problem to be solved by the utility model is to provide a mud-water separation system that can better realize mud-water separation.
本实用新型是采取如下技术方案来完成的:泥水分离系统,包括混合装置、泥水分离罐、压滤装置、沉淀池和净化池;所述泥水分离罐包括主罐体,主罐体内带有内腔,所述主罐体内腔上部设置有多个过滤吸水端,过滤吸水端带有网格支架和滤布,多个过滤吸水端并联于吸水管上,吸水管配置有吸水泵;所述主罐体上端设置有螺旋环绕的盘管,所述盘管的外端与第一泥浆输送管导通,所述主罐体内固定设置有与盘管内端连接的下行管道,下行管道的末端朝向内腔开口,所述第一泥浆输送管中固定设置有螺旋输送带,螺旋输送带的外端配置有泥浆输送泵,所述主罐体的下端带有排泥出口;所述混合装置与第一泥浆输送管连接,所述吸水管与沉淀池连接,沉淀池下部连接有第二泥浆输送管,第二泥浆输送管与混合装置连接,所述沉淀池上部通过管道与净化池连接,所述排泥出口与压滤装置通过管道连接,压滤装置的排渣口正对泥块输送带,所述压滤装置的出水管与沉淀池连接。 The utility model is completed by adopting the following technical solutions: a mud-water separation system, including a mixing device, a mud-water separation tank, a filter press device, a sedimentation tank and a purification tank; the mud-water separation tank includes a main tank body with an internal cavity, the upper part of the inner cavity of the main tank is provided with a plurality of filter suction ends, the filter suction ends are provided with grid supports and filter cloths, and the plurality of filter suction ends are connected in parallel on the water suction pipe, and the water suction pipe is equipped with a water suction pump; the main tank The upper end of the tank body is provided with a spiral coil pipe, and the outer end of the coil pipe is connected to the first mud delivery pipe. The main tank body is fixed with a downpipe connected to the inner end of the coil pipe, and the end of the downpipe pipe faces inward. cavity opening, the first mud delivery pipe is fixed with a screw conveyor belt, the outer end of the screw conveyor belt is equipped with a mud delivery pump, and the lower end of the main tank has a mud discharge outlet; the mixing device and the first The mud delivery pipe is connected, the suction pipe is connected to the sedimentation tank, the second mud delivery pipe is connected to the lower part of the sedimentation tank, the second mud delivery pipe is connected to the mixing device, the upper part of the sedimentation tank is connected to the purification tank through a pipeline, and the drainage The mud outlet is connected to the filter press device through pipelines, the slag outlet of the filter press device is facing the mud block conveyor belt, and the water outlet pipe of the filter press device is connected to the sedimentation tank.
本实用新型提供的泥水分离系统具有以下优点:1、设置了首次泥水分离后的沉淀池和净化池,使泥水得到更好地净化处理,且沉淀后产生的泥土可循环进行分离和压滤处理,提高分离效果;2、泥水分离罐的螺旋盘管和泥浆输送管中的螺旋输送带使泥浆与絮凝剂等的均匀混合效果更好,有利于泥水分离的进行;3、采用罐体分离泥浆能够方便定量输入泥浆、输出水和泥,提高了泥水分离的效率,可增加分离后的水的排出量;4、吸水管上配置了具有过滤功能的过滤吸水端,使排出的水更干净,可不经沉淀等处理即可使用。 The mud-water separation system provided by the utility model has the following advantages: 1. The sedimentation tank and the purification tank after the first mud-water separation are set, so that the mud water can be better purified, and the mud produced after sedimentation can be recycled for separation and pressure filtration treatment , improve the separation effect; 2. The spiral coil of the mud-water separation tank and the spiral conveyor belt in the mud conveying pipe make the mud and flocculant evenly mixed better, which is conducive to the separation of mud and water; 3. Use tanks to separate mud It can conveniently and quantitatively input mud, output water and mud, improve the efficiency of mud-water separation, and increase the discharge of separated water; 4. The suction pipe is equipped with a filter suction end with filtering function to make the discharged water cleaner. It can be used without treatment such as precipitation.
附图说明 Description of drawings
本实用新型有如下附图: The utility model has following drawings:
图1本实用新型提供的泥水分离罐的结构示意图。 Fig. 1 is a schematic structural view of the mud-water separation tank provided by the utility model.
图2为本实用新型提供的泥水分离系统的结构原理方框图。 Fig. 2 is a structural and principle block diagram of the mud-water separation system provided by the utility model.
具体实施方式 Detailed ways
附图表示了本实用新型的技术方案及其实施例,下面再结合附图进一步描述其实施例的各有关细节及其工作原理。 The accompanying drawings show the technical solution of the utility model and its embodiments, and the details and working principles of the embodiments will be further described below in conjunction with the accompanying drawings.
参照图1、图2所示,本实用新型提供的泥水分离系统,包括混合装置1、泥水分离罐2、压滤装置3、沉淀池4和净化池5,混合装置1一般为带搅拌功能的泥浆池;所述泥水分离罐2包括主罐体6,主罐体6内带有内腔,所述主罐体6内腔上部设置有多个过滤吸水端7,过滤吸水端7带有网格支架71和滤布72,滤布72包裹在网格支架71外围,多个过滤吸水端7并联于吸水管8上,吸水管8配置有吸水泵10;所述主罐体6上端设置有螺旋环绕的盘管11,所述盘管11的外端与第一泥浆输送管12导通,所述主罐体6内固定设置有与盘管11内端连接的下行管道13,盘管11由外而内环绕并在主罐体6上端中心向下与下行管道13连接,下行管道13的末端朝向内腔开口,所述下行管道13的开口端设置有喇叭形出口14,过滤吸水端7的进入口处于喇叭形出口14的上方,所述第一泥浆输送管12中固定设置有螺旋输送带15,螺旋输送带15的外端配置有泥浆输送泵16,所述主罐体6的下端带有排泥出口17;所述混合装置1与第一泥浆输送管12连接,所述吸水管8与沉淀池4连接,沉淀池4下部连接有第二泥浆输送管18,第二泥浆输送管18与混合装置1连接,所述沉淀池4上部通过管道与净化池5连接,所述排泥出口17与压滤装置3通过管道连接,压滤装置3的排渣口正对泥块输送带19,所述压滤装置3的出水管20与沉淀池4连接。 Referring to Fig. 1 and shown in Fig. 2, the mud-water separation system provided by the utility model includes a mixing device 1, a mud-water separation tank 2, a filter press device 3, a settling tank 4 and a purification tank 5, and the mixing device 1 is generally a mixer with a stirring function. Mud pool; the mud-water separation tank 2 includes a main tank body 6 with an inner cavity, the upper part of the main tank body 6 inner cavity is provided with a plurality of filter suction ends 7, and the filter suction end 7 has a net grid support 71 and filter cloth 72, the filter cloth 72 is wrapped around the periphery of the grid support 71, a plurality of filter water suction ends 7 are connected in parallel on the water suction pipe 8, and the water suction pipe 8 is equipped with a water suction pump 10; the upper end of the main tank body 6 is provided with A spiral coil 11, the outer end of the coil 11 is in communication with the first mud delivery pipe 12, the main tank body 6 is fixed with a downpipe 13 connected to the inner end of the coil 11, the coil 11 Surrounded from the outside to the inside and connected downwards at the center of the upper end of the main tank body 6 to the downpipe 13, the end of the downpipe 13 opens toward the inner cavity, the open end of the downpipe 13 is provided with a trumpet-shaped outlet 14, and the filter suction end 7 The inlet is above the trumpet-shaped outlet 14, the first mud delivery pipe 12 is fixedly provided with a screw conveyor belt 15, the outer end of the screw conveyor belt 15 is equipped with a mud delivery pump 16, and the lower end of the main tank body 6 With a mud discharge outlet 17; the mixing device 1 is connected to the first mud delivery pipe 12, the water suction pipe 8 is connected to the sedimentation tank 4, the second mud delivery pipe 18 is connected to the lower part of the sedimentation tank 4, and the second mud delivery pipe 18 is connected to the mixing device 1, the upper part of the sedimentation tank 4 is connected to the purification tank 5 through a pipeline, the mud discharge outlet 17 is connected to the filter press device 3 through a pipeline, and the slag discharge port of the filter press device 3 is facing the mud conveyor belt 19. The outlet pipe 20 of the filter press device 3 is connected to the sedimentation tank 4 .
参照图1所示,为了使泥水分离装置的工作更加自动化,所述内腔内设置有液位监测装置21,液位监测装置21处于过滤吸水端7上方,液位检测装置21与所述泥浆输送泵16的控制装置连接,控制装置一般为PLC等,所述主罐体6内腔内泥浆的液位低于液位监测装置21的临界液位时,所述泥浆输送泵16持续工作输送泥浆,所述内腔内泥浆的液位高于或等于液位监测装置21的监测液位时,所述泥浆输送泵16停止工作并不再输送泥浆。通过液位监测装置21可以使泥浆的注入更加有针对性,有利于实现水、泥的排出与泥浆的注入实现平衡,有利于提高工作效率。 With reference to shown in Figure 1, in order to make the work of mud-water separation device more automatic, liquid level monitoring device 21 is arranged in the described inner chamber, and liquid level monitoring device 21 is above the filter suction end 7, and liquid level detecting device 21 is connected with described mud The control device of the delivery pump 16 is connected, and the control device is generally PLC, etc. When the liquid level of the mud in the inner cavity of the main tank body 6 is lower than the critical liquid level of the liquid level monitoring device 21, the mud delivery pump 16 continues to work and deliver For mud, when the liquid level of the mud in the inner cavity is higher than or equal to the monitoring liquid level of the liquid level monitoring device 21, the mud delivery pump 16 stops working and no longer transports mud. Through the liquid level monitoring device 21, the injection of mud can be more targeted, which is beneficial to achieve a balance between the discharge of water and mud and the injection of mud, and is conducive to improving work efficiency.
参照图1、图2所示,本实用新型还提供了采用上述泥水分离系统进行泥浆循环泥水分离的方法,包括A、将泥浆输入混合装置1中并逐步投入絮凝剂和石灰;B、将混合装置1中的泥浆通过泥浆输送泵16输送到泥水分离罐2中,泥浆通过第一泥浆输送管12注入到盘管11中,泥浆经由盘管11在下行管道13的螺旋输送带15中缓慢下行,到达喇叭形出口14后泥浆沿喇叭形出口14向外扩散并落入内腔;C、所述泥浆进入内腔后在絮凝剂和石灰的作用下,泥浆出现上下分层,上层为水下层为泥,上层的水在吸水泵10的作用下通过过滤吸水端7过滤并由吸水管8排入沉淀池,过滤吸水端7已对泥水分离罐2中的水过滤一遍,所述下层的泥通过排泥出口17排到压滤装置18中;D、沉淀池4中的水在经过一定时间衬垫后出现泥浆沉淀,上层的水通过管道输送到净化池5中进行净化处理,下层的泥浆通过第二泥浆输送管18重新注入到混合装置1中再次进行泥水分离处理;E、输送到压滤装置3中的泥经过压滤处理后形成泥块和水,水被出水管20输送到沉淀池4中,沉淀池4中的水在经过一定时间衬垫后出现泥浆沉淀,上层的水通过管道输送到净化池5中进行净化处理,下层的泥浆通过第二泥浆输送管18重新注入到混合装置1中再次进行泥水分离处理,泥块通过排渣口排到泥块输送带19上运走。 With reference to Fig. 1, shown in Fig. 2, the utility model also provides the method that adopts above-mentioned mud-water separation system to carry out mud circulation mud-water separation, comprises A, mud is input in mixing device 1 and gradually drops into flocculant and lime; B, mixing The mud in the device 1 is sent to the mud-water separation tank 2 through the mud delivery pump 16, and the mud is injected into the coil pipe 11 through the first mud delivery pipe 12, and the mud slowly descends in the spiral conveyor belt 15 of the down pipe 13 through the coil pipe 11 After reaching the horn-shaped outlet 14, the mud diffuses outwards along the horn-shaped outlet 14 and falls into the inner cavity; C, after the mud enters the inner cavity, under the action of flocculant and lime, the mud appears up and down, and the upper layer is the underwater layer For mud, the water in the upper layer is filtered through the filter suction end 7 under the action of the suction pump 10 and is discharged into the sedimentation tank by the suction pipe 8. The filter suction end 7 has filtered the water in the mud-water separation tank 2 once, and the mud in the lower layer Discharge in the filter press device 18 through the mud discharge outlet 17; D, the water in the settling tank 4 appears mud precipitation after a certain period of time liner, the water of the upper layer is transported in the purification tank 5 by pipeline and carries out purification treatment, the mud of the lower floor Re-inject into the mixing device 1 through the second mud delivery pipe 18 and carry out the mud-water separation treatment again; E, the mud delivered to the filter press device 3 forms mud lumps and water after the press filter treatment, and the water is transported to the sediment by the outlet pipe 20 In the pool 4, the water in the sedimentation tank 4 will deposit mud after a certain period of time, and the water in the upper layer will be transported to the purification tank 5 through pipelines for purification treatment, and the mud in the lower layer will be re-injected into the mixing tank 5 through the second mud delivery pipe 18. In the device 1, the mud-water separation process is carried out again, and the mud block is discharged on the mud block conveyor belt 19 through the slag discharge port to be transported away.
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520320997.9U CN204752506U (en) | 2015-05-19 | 2015-05-19 | Mud -water separation system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520320997.9U CN204752506U (en) | 2015-05-19 | 2015-05-19 | Mud -water separation system |
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| Publication Number | Publication Date |
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| CN204752506U true CN204752506U (en) | 2015-11-11 |
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| CN201520320997.9U Expired - Fee Related CN204752506U (en) | 2015-05-19 | 2015-05-19 | Mud -water separation system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104961321A (en) * | 2015-05-19 | 2015-10-07 | 温州大学 | Mud-water separation system and slurry circulation mud-water separation method |
| CN108635952A (en) * | 2018-05-30 | 2018-10-12 | 成都金玉雄辉建筑工程有限公司 | Device for separating mud and water |
-
2015
- 2015-05-19 CN CN201520320997.9U patent/CN204752506U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104961321A (en) * | 2015-05-19 | 2015-10-07 | 温州大学 | Mud-water separation system and slurry circulation mud-water separation method |
| CN108635952A (en) * | 2018-05-30 | 2018-10-12 | 成都金玉雄辉建筑工程有限公司 | Device for separating mud and water |
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| 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: 20151111 Termination date: 20170519 |