[go: up one dir, main page]

CN216236207U - A multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment - Google Patents

A multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment Download PDF

Info

Publication number
CN216236207U
CN216236207U CN202122898103.2U CN202122898103U CN216236207U CN 216236207 U CN216236207 U CN 216236207U CN 202122898103 U CN202122898103 U CN 202122898103U CN 216236207 U CN216236207 U CN 216236207U
Authority
CN
China
Prior art keywords
flocculation
tank
precipitation
water inlet
landfill leachate
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 - Fee Related
Application number
CN202122898103.2U
Other languages
Chinese (zh)
Inventor
周俊华
杜克
黄柠
詹庆宁
梁正义
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangxi Jiangyi Environmental Technology Co ltd
Original Assignee
Guangxi Jiangyi Environmental Technology Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Guangxi Jiangyi Environmental Technology Co ltd filed Critical Guangxi Jiangyi Environmental Technology Co ltd
Priority to CN202122898103.2U priority Critical patent/CN216236207U/en
Application granted granted Critical
Publication of CN216236207U publication Critical patent/CN216236207U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The utility model discloses a multi-stage flocculation and precipitation system suitable for garbage leachate pretreatment, which comprises a water inlet pump, a water inlet pipe, a multi-stage flocculation and precipitation tank, a dosing system, a stirrer, a flow meter, a PLC (programmable logic controller) control system and a water outlet, wherein the water inlet pump supplies garbage leachate to the multi-stage flocculation and precipitation tank through the water inlet pipe; a dosing system, a stirrer and a water outlet are arranged on the multi-stage flocculation sedimentation tank, and the dosing system and the water inlet pump are controlled by a PLC control system; the flowmeter is arranged on the water inlet pipe. The flocculation sedimentation system designed by the utility model implements multi-stage flocculation and multi-stage sedimentation, so that the consumption of a flocculating agent can be reduced, and the flocculation sedimentation effect can be improved; the PLC control system realizes multi-party linkage, has high automation degree, is simple and convenient to operate and saves manpower; can simultaneously remove suspended matters, hardness, heavy metals and macromolecular organic matters in the leachate, and greatly reduces the full-quantization treatment difficulty of the leachate.

Description

一种适用于垃圾渗滤液预处理的多级絮凝沉淀系统A multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment

技术领域technical field

本实用新型属于污水处理沉淀池技术领域,尤其涉及一种适用于垃圾渗滤液预处理的多级絮凝沉淀系统。The utility model belongs to the technical field of sewage treatment sedimentation tanks, in particular to a multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment.

背景技术Background technique

絮凝过程是工业用水和生活污水处理中最基本也是极为重要的处理过程,通过向水中投加一些药剂(通常称为絮凝剂及助凝剂),使水中难以沉淀的颗粒能互相聚合而形成胶体,然后与水体中的杂质结合形成更大的絮凝体。絮凝体具有强大吸附力,不仅能吸附悬浮物,还能吸附部分细菌和溶解性物质。絮凝体通过吸附,体积增大而下沉。絮凝沉淀工艺在水处理上的应用已有几百年的历史,与其他物理化学方法相比具有出水水质好、工艺运行稳定可靠、经济实用、操作简便等优点。但是,现有絮凝沉淀池对垃圾渗滤液预处理的适用性较差,这是由于垃圾渗滤液污染物种类多、浓度高,水质、水量变化较大,传统絮凝沉淀池不仅消耗更多的絮凝剂,而且絮凝效果也较差,导致后续各工艺污染物消减干扰因素多,进而全量化处理难度增大。为此,设计研发垃圾渗滤液专用的絮凝沉淀池,将有助于渗滤液的预处理效果,进而为垃圾渗滤液全量化处理打下基础。The flocculation process is the most basic and extremely important treatment process in the treatment of industrial water and domestic sewage. By adding some chemicals (usually called flocculants and coagulants) to the water, the particles that are difficult to settle in the water can polymerize with each other to form colloids. , which then combine with impurities in the water body to form larger flocs. The floc has a strong adsorption force, which can not only absorb suspended solids, but also absorb some bacteria and dissolved substances. The flocs increase in volume and sink through adsorption. Compared with other physical and chemical methods, the flocculation and sedimentation process has been applied in water treatment for hundreds of years. However, the existing flocculation and sedimentation tanks have poor applicability to landfill leachate pretreatment. This is due to the large variety of pollutants in landfill leachate, high concentrations, and large changes in water quality and water volume. Traditional flocculation and sedimentation tanks not only consume more flocculation and sedimentation tanks. In addition, the flocculation effect is also poor, which leads to many factors that interfere with the reduction of pollutants in the subsequent processes, and furthermore, the difficulty of full quantification treatment increases. To this end, the design and development of a special flocculation sedimentation tank for landfill leachate will contribute to the pretreatment effect of the leachate, thereby laying the foundation for the full-scale treatment of landfill leachate.

实用新型内容Utility model content

本实用新型针对上述现有技术的不足,发明了一种适用于垃圾渗滤液预处理的多级絮凝沉淀系统。Aiming at the deficiencies of the above-mentioned prior art, the utility model invents a multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment.

为了实现上述目的本实用新型采用如下的技术方案:In order to achieve the above object, the utility model adopts the following technical scheme:

一种适用于垃圾渗滤液预处理的多级絮凝沉淀系统,包括进水泵、进水管、多级絮凝沉淀池、加药系统、搅拌器、流量计、PLC控制系统和出水口,所述的进水泵通过进水管为多级絮凝沉淀池供垃圾渗透液;所述的多级絮凝沉淀池上设置有加药系统、搅拌器和出水口,所述的加药系统和进水泵通过PLC控制系统控制;所述的流量计设置在进水管上。A multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment, comprising an inlet pump, a water inlet pipe, a multi-stage flocculation sedimentation tank, a dosing system, a mixer, a flow meter, a PLC control system and a water outlet, the inlet The water pump supplies waste permeate to the multi-stage flocculation sedimentation tank through the water inlet pipe; the multi-stage flocculation sedimentation tank is provided with a dosing system, an agitator and a water outlet, and the dosing system and the inlet water pump are controlled by a PLC control system; The flow meter is arranged on the water inlet pipe.

进一步,所述的多级絮凝沉淀池由多组反应单元串联组成;所述的反应单元包括反应槽、沉淀槽和隔板,所述的反应槽与沉淀槽之间通过隔板隔开;所述的反应槽上连接有加药系统和独立安装有搅拌器,可以根据渗滤液的情况选择安装反应单元的数量。Further, the multi-stage flocculation sedimentation tank is composed of multiple groups of reaction units connected in series; the reaction unit includes a reaction tank, a sedimentation tank and a partition, and the reaction tank and the sedimentation tank are separated by a partition; The reaction tank is connected with a dosing system and an agitator is installed independently, and the number of installed reaction units can be selected according to the situation of the leachate.

进一步,所述的隔板由两块墙板组成,两块所述的墙板错位安装,其中一块墙板朝下安装,另一块朝上安装,两者左右错位,反应槽内的液体从两块墙板之间的缝隙由下往上流向沉淀槽。Further, the partition plate is composed of two wall panels, and the two wall panels are installed in dislocation, one of the wall panels is installed downward, and the other is installed upward, and the two are dislocated from left to right, and the liquid in the reaction tank is removed from the two walls. The gap between the wall panels flows from bottom to top to the sedimentation tank.

进一步,所述的加药系统包括絮凝剂罐、加药管和计量泵,所述的絮凝剂罐通过加药管与反应槽连通,絮凝剂罐上连接有多根加药管,可以为多个反应槽提供絮凝剂;所述的加药管上设置有计量泵,计量泵受PLC控制系统的控制。Further, the dosing system includes a flocculant tank, a dosing pipe and a metering pump, the flocculant tank is communicated with the reaction tank through the dosing pipe, and a plurality of dosing pipes are connected to the flocculant tank, which can be multiple Each reaction tank provides a flocculant; the dosing pipe is provided with a metering pump, and the metering pump is controlled by a PLC control system.

进一步,所述的PLC控制系统同时控制多个计量泵和多个搅拌器,由同一个控制系统控制整个多级絮凝沉淀系统的作业。Further, the PLC control system simultaneously controls multiple metering pumps and multiple agitators, and the same control system controls the operation of the entire multi-stage flocculation and sedimentation system.

进一步,所述的多级絮凝沉淀池采用推流式进水,即可避免再次提升污水的能耗,又能减少对絮凝后混合液的扰动,增加絮凝效果。Further, the multi-stage flocculation sedimentation tank adopts push-flow inflow water, which can avoid increasing the energy consumption of sewage again, and can also reduce the disturbance to the mixed liquid after flocculation, and increase the flocculation effect.

进一步,所述的多级絮凝沉淀池内的反应槽和沉淀槽沿液体流动方向有效水深依次降低,避免前后槽内混合液再次混合,影响处理效果。Further, the effective water depth of the reaction tank and the sedimentation tank in the multi-stage flocculation sedimentation tank decreases sequentially along the liquid flow direction, so as to avoid the mixed liquid in the front and rear tanks from being mixed again, which affects the treatment effect.

进一步,所述的反应槽的体积比沉淀槽的体积小,反应槽小可以让絮凝剂与渗滤液中污染物充分反应成核,在空间比较大的沉淀槽内持续反应形成大的絮凝体,实现泥水快速沉淀分离。Further, the volume of the reaction tank is smaller than that of the sedimentation tank, and the small reaction tank can allow the flocculant to fully react with the pollutants in the leachate to form nucleation, and continue to react in the sedimentation tank with a relatively large space to form large flocs. To achieve rapid sedimentation and separation of mud and water.

进一步,还包括液位计,所述的液位计安装在液位最低的沉淀槽内;液位计与PLC控制系统电信连接,PLC控制系统根据液位计监测的数据控制进水泵的工作,液位计用于监测沉淀槽内的液位情况,PLC控制系统通过液位计监测到的数据对进水泵、计量泵和搅拌器进行智能控制。Further, it also includes a liquid level gauge, which is installed in the sedimentation tank with the lowest liquid level; the liquid level gauge is telecommunicationly connected with the PLC control system, and the PLC control system controls the work of the inlet pump according to the data monitored by the liquid level gauge, The liquid level gauge is used to monitor the liquid level in the sedimentation tank, and the PLC control system intelligently controls the feed pump, metering pump and agitator through the data monitored by the liquid level gauge.

进一步,所述的液位计为超声波液位计、浮球液位计或压机变送器Further, the liquid level gauge is an ultrasonic level gauge, a float level gauge or a press transmitter

本实用新型的优点在于:本实用新型设计的絮凝沉淀系统实行多级絮凝、多级沉淀,既能减少絮凝剂用量,又能增加絮凝沉淀效果;且每个反应槽均采用上端进水下端出水形式,絮凝剂从上端加入,相邻两槽体内渗滤液处理互不干扰;PLC控制系统实现多方联动,自动化程度高,操作简便,节省人力;能同时去除渗滤液中的悬浮物、硬度、重金属及大分子有机物,极大降低渗滤液全量化处理难度。The advantages of the utility model are: the flocculation and precipitation system designed by the utility model implements multi-stage flocculation and multi-stage precipitation, which can not only reduce the amount of flocculant, but also increase the effect of flocculation and precipitation; Form, the flocculant is added from the upper end, and the leachate treatment in the adjacent two tanks does not interfere with each other; the PLC control system realizes multi-party linkage, high degree of automation, easy operation, and labor saving; it can simultaneously remove suspended solids, hardness, and heavy metals in the leachate. And macromolecular organic matter, which greatly reduces the difficulty of fully quantitative treatment of leachate.

附图说明Description of drawings

图1是本实用新型一种适用于垃圾渗滤液预处理的多级絮凝沉淀系统的正视结构示意图。Figure 1 is a schematic front view of a multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment according to the present invention.

具体实施方式Detailed ways

以下结合附图对本实用新型进行详细说明:Below in conjunction with accompanying drawing, the utility model is described in detail:

在本实用新型的描述中,需要说明的是,“左”、“右”、“上”、“下”“左”、“右”等指示的方位或位置关系为基于附图所示的方位或位置关系,或者是该实用新型产品使用时惯常摆放的方位或位置关系,仅是为了便于描述本实用新型和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以及特定的方位构造和操作,因此不能理解为对本实用新型的限制。In the description of the present invention, it should be noted that the orientations or positional relationships indicated by "left", "right", "up", "down", "left", "right", etc. are based on the orientations shown in the accompanying drawings Or positional relationship, or the orientation or positional relationship that the utility model product is usually placed in use, is only for the convenience of describing the present utility model and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, And the specific orientation configuration and operation, therefore, should not be construed as a limitation of the present invention.

如图1所示,一种适用于垃圾渗滤液预处理的多级絮凝沉淀系统,包括进水泵1、进水管2、多级絮凝沉淀池、加药系统、搅拌器3、流量计4、PLC控制系统5、出水口6和液位计13,整个多级絮凝沉淀池为加强槽钢池体,内外涂覆防腐材料。所述的多级絮凝沉淀池由多组反应单元串联组成;反应单元包括反应槽7、沉淀槽8和隔板9,反应槽7与沉淀槽8之间通过隔板9隔开,反应槽7位于左边,沉淀槽8位于右边,反应槽7的体积比沉淀槽8的体积小,小的反应槽7能够让渗滤液中的杂质与絮凝剂混合得更充分,大的沉淀槽方便絮凝体的沉淀。反应槽7和沉淀槽8除了宽度(从图中看横向距离为宽度,竖向距离为高)不一样外其它尺寸(长、高)都一样。隔板9由两块墙板组成,两块所述的墙板错位安装,在隔板9的作用下液体由下往上流向沉淀槽8;两块墙板的间距为5cm。所述的反应槽7上连接有药系统和独立安装有搅拌器3,搅拌器3包括搅拌电机和搅拌叶,搅拌器3朝下安装在反应槽7的顶上。所述的进水泵1通过进水管2为多级絮凝沉淀池供垃圾渗透液,所述的流量计4设置在进水管2上。进水管2安装在多级絮凝沉淀池的左边即最左边的反应槽7的上部,所述的出水口6安装在多级絮凝沉淀池的右边即最右边的沉淀槽的下部,多级絮凝沉淀池内的液体从左往右流动。多级絮凝沉淀池采用推流式进水,沿液体流动方向有效水深依次降低,采用上端进水,下端出水形式,且自进水至出水,絮凝剂从上端加入。在最右端的沉淀槽8的上部安装有液位计13,所述的加药系统、进水泵1、搅拌器3、液位计13和流量计4与PLC控制系统5电性连接。所述的PLC控制系统5能根据液位计13监测的数据高于预设的高水位时控制进水泵1停止工作,数据低于预设的低水位时控制进水泵1启动。As shown in Figure 1, a multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment includes an inlet pump 1, a water inlet pipe 2, a multi-stage flocculation sedimentation tank, a dosing system, a mixer 3, a flow meter 4, a PLC The control system 5, the water outlet 6 and the liquid level gauge 13, the entire multi-stage flocculation sedimentation tank is a reinforced channel steel tank body, and the inside and outside are coated with anti-corrosion materials. The multi-stage flocculation sedimentation tank is composed of multiple groups of reaction units connected in series; the reaction unit includes a reaction tank 7, a sedimentation tank 8 and a partition 9, and the reaction tank 7 and the sedimentation tank 8 are separated by a partition 9, and the reaction tank 7 On the left, the sedimentation tank 8 is on the right, the volume of the reaction tank 7 is smaller than the volume of the sedimentation tank 8, the small reaction tank 7 can make the impurities in the leachate and the flocculant mix more fully, and the large sedimentation tank is convenient for flocculation. precipitation. The other dimensions (length and height) of the reaction tank 7 and the precipitation tank 8 are the same except for the width (the horizontal distance is the width and the vertical distance is the height when viewed from the figure). The partition board 9 is composed of two wall boards, and the two wall boards are installed in dislocation. Under the action of the partition board 9, the liquid flows from bottom to top to the sedimentation tank 8; the distance between the two wall boards is 5cm. The reaction tank 7 is connected with a drug system and independently installed with a stirrer 3 . The agitator 3 includes a stirring motor and a stirring blade. The agitator 3 is installed on the top of the reaction tank 7 facing downwards. The inlet water pump 1 supplies the waste permeate to the multi-stage flocculation sedimentation tank through the inlet pipe 2 , and the flow meter 4 is arranged on the inlet pipe 2 . The water inlet pipe 2 is installed on the left side of the multi-stage flocculation sedimentation tank, that is, the upper part of the leftmost reaction tank 7, and the water outlet 6 is installed on the right side of the multi-level flocculation sedimentation tank, that is, the lower part of the rightmost sedimentation tank. The liquid in the pool flows from left to right. The multi-stage flocculation sedimentation tank adopts the push-flow water inlet, and the effective water depth decreases in turn along the liquid flow direction. A liquid level gauge 13 is installed on the upper part of the sedimentation tank 8 at the far right end. The dosing system, the feed pump 1 , the agitator 3 , the liquid level gauge 13 and the flow meter 4 are electrically connected with the PLC control system 5 . The PLC control system 5 can control the intake pump 1 to stop working according to the data monitored by the liquid level gauge 13 when it is higher than the preset high water level, and control the intake pump 1 to start when the data is lower than the preset low water level.

本实施方式的加药系统包括絮凝剂罐10、加药管11和计量泵12,絮凝剂罐10通过加药管11与反应槽7连通,每一个反应槽7拥有单独的加药管11。在加药管11上设置有计量泵12,通过PLC控制系统5控制计量泵12的加药量和加药时间。PLC控制系统5同时控制多个计量泵12,实现统一管理控制。所述的PLC控制系统5能实现进水泵1启动时计量泵12和搅拌器3均启动,进水泵1停止时,计量泵12停止,搅拌器3延时一定时间再停止。PLC控制系统5的可以同时控制多个计量泵12和多个搅拌器3,计量泵12和搅拌器13也可以根据需要进行非同步控制。The dosing system of this embodiment includes a flocculant tank 10 , a dosing pipe 11 and a metering pump 12 . The flocculant tank 10 communicates with the reaction tank 7 through the dosing pipe 11 , and each reaction tank 7 has a separate dosing pipe 11 . A metering pump 12 is arranged on the dosing pipe 11 , and the dosing amount and dosing time of the dosing pump 12 are controlled by the PLC control system 5 . The PLC control system 5 simultaneously controls a plurality of metering pumps 12 to realize unified management and control. The PLC control system 5 can realize that both the metering pump 12 and the agitator 3 are started when the inlet pump 1 is started, and when the inlet pump 1 is stopped, the metering pump 12 is stopped, and the agitator 3 stops after a certain time delay. The PLC control system 5 can control multiple metering pumps 12 and multiple mixers 3 at the same time, and the metering pumps 12 and mixers 13 can also be asynchronously controlled as required.

所述进水泵1为耐腐蚀的潜水泵或自吸离心泵中。所述的液位计13为超声波液位计、浮球液位计或压机变送器。The inlet pump 1 is a corrosion-resistant submersible pump or a self-priming centrifugal pump. The liquid level gauge 13 is an ultrasonic level gauge, a float level gauge or a press transmitter.

尽管上文对本实用新型的具体实施方案进行了详细的描述和说明,但应该指明的是,我们可以对上述实施方案进行各种改变和修改,但这些都不脱离本实用新型的精神和所附的权利要求所记载的范围。Although the specific embodiments of the present invention have been described and illustrated in detail above, it should be pointed out that various changes and modifications can be made to the above-mentioned embodiments, but these do not depart from the spirit of the present invention and the appended the scope of the claims.

Claims (10)

1. The multi-stage flocculation and precipitation system suitable for landfill leachate pretreatment is characterized by comprising a water inlet pump (1), a water inlet pipe (2), a multi-stage flocculation and precipitation tank, a dosing system, a stirrer (3), a flow meter (4), a PLC (programmable logic controller) control system (5) and a water outlet (6), wherein the water inlet pump (1) supplies landfill leachate to the multi-stage flocculation and precipitation tank through the water inlet pipe (2); the multistage flocculation sedimentation tank is provided with a dosing system, a stirrer (3) and a water outlet (6), and the dosing system and the water inlet pump (1) are controlled by a PLC control system (5); the flowmeter (4) is arranged on the water inlet pipe (2).
2. The multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment of claim 1, wherein the multi-stage flocculation sedimentation tank is composed of a plurality of groups of reaction units connected in series; the reaction unit comprises a reaction tank (7), a precipitation tank (8) and a partition plate (9), wherein the reaction tank (7) is separated from the precipitation tank (8) through the partition plate (9); the reaction tank (7) is connected with a dosing system and is independently provided with a stirrer (3).
3. The multistage flocculation and precipitation system for the pretreatment of landfill leachate according to claim 2, wherein the partition (9) is composed of two wall panels, and the two wall panels are installed in a staggered manner.
4. The multistage flocculation and precipitation system suitable for landfill leachate pretreatment according to claim 3, wherein the dosing system comprises a flocculant tank (10), a dosing pipe (11) and a metering pump (12), the flocculant tank (10) is communicated with the reaction tank (7) through the dosing pipe (11); the dosing pipe (11) is provided with a metering pump (12).
5. The multistage flocculation and precipitation system for landfill leachate pretreatment of claim 4, wherein the PLC control system (5) controls a plurality of metering pumps (12) and a plurality of agitators (3) simultaneously.
6. The multi-stage flocculation and sedimentation system for landfill leachate pretreatment of claim 5, wherein the multi-stage flocculation and sedimentation tank adopts plug flow type influent water.
7. The multistage flocculation and precipitation system suitable for landfill leachate pretreatment of claim 6, wherein the effective water depth of the reaction tank (7) and the precipitation tank (8) in the multistage flocculation and precipitation tank is sequentially reduced along the liquid flowing direction.
8. The multistage flocculation and precipitation system for landfill leachate pretreatment of claim 7, wherein the volume of the reaction tank (7) is smaller than the volume of the precipitation tank (8).
9. The multistage flocculation and precipitation system suitable for landfill leachate pretreatment of any of claims 1-8, characterized in that, further comprising a liquid level meter (13), wherein the liquid level meter (13) is installed in the precipitation tank (8) with the lowest liquid level; the liquid level meter (13) is in telecommunication connection with the PLC control system (5), and the PLC control system (5) controls the work of the water inlet pump (1) according to data monitored by the liquid level meter (13).
10. The multistage flocculation and precipitation system suitable for landfill leachate pretreatment of claim 9, wherein the level meter (13) is an ultrasonic level meter, a floating ball level meter or a press transducer.
CN202122898103.2U 2021-11-24 2021-11-24 A multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment Expired - Fee Related CN216236207U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202122898103.2U CN216236207U (en) 2021-11-24 2021-11-24 A multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202122898103.2U CN216236207U (en) 2021-11-24 2021-11-24 A multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment

Publications (1)

Publication Number Publication Date
CN216236207U true CN216236207U (en) 2022-04-08

Family

ID=80957066

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202122898103.2U Expired - Fee Related CN216236207U (en) 2021-11-24 2021-11-24 A multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment

Country Status (1)

Country Link
CN (1) CN216236207U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114772796A (en) * 2022-05-25 2022-07-22 江苏明湖生物能源科技有限公司 Multi-impurity sewage sedimentation promoting device and working method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114772796A (en) * 2022-05-25 2022-07-22 江苏明湖生物能源科技有限公司 Multi-impurity sewage sedimentation promoting device and working method thereof

Similar Documents

Publication Publication Date Title
WO2020029571A1 (en) Rising-flow speed varying hydrolytic acidification reactor
CN203355383U (en) Coagulative precipitation tank
CN216236207U (en) A multi-stage flocculation sedimentation system suitable for landfill leachate pretreatment
CN207713466U (en) A kind of electric flocculation high dense settling pond
CN203845894U (en) Laboratory inorganic wastewater treatment device
CN101323489A (en) Sea water advanced pretreatment apparatus
CN106315969A (en) Integrated wastewater treatment equipment of IBR (integral biological reactor) and treatment process
CN102874910B (en) A coagulation-sedimentation integrated treatment method and treatment device thereof
CN101343100A (en) Duplex treatment device for building construction wastewater
CN201147649Y (en) Adjustable low-energy consumption highly-effective water power mix coagulation reactor
CN201268648Y (en) Multifunctional universal sewage treatment system
CN217757087U (en) Sewage treatment pool
CN105330105B (en) The flocculation integrated device of inorganic-organic microbial
CN202139129U (en) Epoxy resin waste water pretreatment device
CN201713389U (en) Pre-treatment system for thermal seawater desalination
CN106380019B (en) Novel water purifies device
CN201151690Y (en) Apparatus for treating waste water using solid micro-electrolyzing filler
CN213446615U (en) Ethylene-vinyl acetate copolymer adhesive wastewater treatment device
CN212102313U (en) A high-efficient sewage treatment device of integration for highway construction
CN116040833A (en) High-concentration fluorine-containing wastewater unit coupling deep purification system and technology
CN211770693U (en) High-efficient coagulating sedimentation device of waste water
CN210480920U (en) Air floatation system with sludge backflow function
CN204803186U (en) Waste water treatment integration equipment of IBR reactor
CN207632642U (en) A kind of sewage-treatment plant of self-loopa
CN212655650U (en) Petrochemical effluent disposal system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20220408

CF01 Termination of patent right due to non-payment of annual fee