CN111252871B - Device for removing colloid impurities under action of static field force coupled with multistage partition plates and water power - Google Patents
Device for removing colloid impurities under action of static field force coupled with multistage partition plates and water power Download PDFInfo
- Publication number
- CN111252871B CN111252871B CN202010128456.1A CN202010128456A CN111252871B CN 111252871 B CN111252871 B CN 111252871B CN 202010128456 A CN202010128456 A CN 202010128456A CN 111252871 B CN111252871 B CN 111252871B
- Authority
- CN
- China
- Prior art keywords
- water
- impurities
- field force
- plate
- sedimentation
- 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.)
- Active
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 119
- 239000012535 impurity Substances 0.000 title claims abstract description 85
- 230000009471 action Effects 0.000 title claims abstract description 20
- 238000005192 partition Methods 0.000 title abstract description 23
- 230000003068 static effect Effects 0.000 title abstract 2
- 239000000084 colloidal system Substances 0.000 title description 22
- 238000004062 sedimentation Methods 0.000 claims abstract description 65
- 239000010802 sludge Substances 0.000 claims abstract description 46
- 238000000034 method Methods 0.000 claims abstract description 41
- 239000010865 sewage Substances 0.000 claims abstract description 31
- 230000005684 electric field Effects 0.000 claims abstract description 26
- 230000008569 process Effects 0.000 claims abstract description 23
- 238000012545 processing Methods 0.000 claims abstract description 8
- 230000005686 electrostatic field Effects 0.000 claims description 16
- 230000008878 coupling Effects 0.000 claims description 14
- 238000010168 coupling process Methods 0.000 claims description 14
- 238000005859 coupling reaction Methods 0.000 claims description 14
- 238000013459 approach Methods 0.000 claims description 3
- 238000005352 clarification Methods 0.000 claims description 3
- 230000006698 induction Effects 0.000 claims description 3
- 238000005191 phase separation Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims 1
- 239000002245 particle Substances 0.000 abstract description 25
- 230000002349 favourable effect Effects 0.000 abstract description 8
- 230000005611 electricity Effects 0.000 abstract 1
- 239000000701 coagulant Substances 0.000 description 9
- 238000005345 coagulation Methods 0.000 description 8
- 230000015271 coagulation Effects 0.000 description 8
- 230000005484 gravity Effects 0.000 description 8
- 238000000926 separation method Methods 0.000 description 8
- 150000002500 ions Chemical class 0.000 description 5
- 239000013049 sediment Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000000416 hydrocolloid Substances 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 238000001179 sorption measurement Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000005202 decontamination Methods 0.000 description 2
- 230000003588 decontaminative effect Effects 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 230000005653 Brownian motion process Effects 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000005537 brownian motion Methods 0.000 description 1
- 230000005591 charge neutralization Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000001647 drug administration Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 239000003864 humus Substances 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 239000011241 protective layer Substances 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000010408 sweeping Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/02—Fluid flow conditions
- C02F2301/028—Tortuous
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
技术领域technical field
本发明属于原水中胶体杂质去除技术领域,更具体地,涉及一种静电场力耦合多级隔板水力作用去除胶体杂质的装置。The invention belongs to the technical field of colloidal impurity removal in raw water, and more particularly relates to a device for removing colloidal impurities by electrostatic field force coupling multi-stage separator hydraulic action.
背景技术Background technique
原水中的杂质按尺寸大小可分为溶解质、胶体以及悬浮物。溶解质是呈真溶液的离子或分子。悬浮物颗粒较大,水静止时,密度较小的悬浮物浮于水面,密度较大的则下沉,所以这类杂质比较好去除。胶体颗粒主要是细小的泥沙、矿物质等无机物和腐殖质等有机物,是许多分子和离子的集合体。这些微粒的表面积很大,有很强的吸附力,许多病菌和细菌等微生物附着在其表面,是原水处理中最主要去除的杂质,也是比较难去除的。The impurities in raw water can be divided into dissolved matter, colloid and suspended matter according to size. Solutes are ions or molecules that are in true solution. The particles of suspended solids are larger. When the water is still, suspended solids with smaller density float on the water surface, while those with higher density sink. Therefore, such impurities are easier to remove. Colloidal particles are mainly inorganic substances such as fine sediment and minerals, and organic substances such as humus, which are aggregates of many molecules and ions. These particles have a large surface area and a strong adsorption force, and many microorganisms such as germs and bacteria adhere to their surface, which are the most important impurities to be removed in raw water treatment, and are also relatively difficult to remove.
水中胶体杂质,粒径微小能发生布朗运动,因具有很强的吸附性其表面常吸附离子而带电,同类胶体因带相同的电荷相斥,在水中难以碰撞聚集成较大的颗粒进行下沉去除。同时,胶粒的水化外壳,形成了保护层,也减少了胶体聚结的可能性,因此胶体颗粒的动力学稳定性强,能在长期分散悬浮存在。所以胶体颗粒不能靠过滤、浮选或重力沉淀的方式去除,虽然胶体在长时间的放置下,会逐渐聚沉,但这个时间非常漫长。Colloidal impurities in water, with small particle size, can undergo Brownian motion. Because of its strong adsorption, its surface often adsorbs ions and is charged. Similar colloids repel each other due to the same charge, so it is difficult to collide and aggregate into larger particles in water for sinking. remove. At the same time, the hydration shell of the colloidal particles forms a protective layer, which also reduces the possibility of colloidal agglomeration, so the colloidal particles have strong dynamic stability and can be dispersed and suspended for a long time. Therefore, colloidal particles cannot be removed by filtration, flotation or gravity sedimentation. Although the colloid will gradually settle after being placed for a long time, the time is very long.
水中胶体一般带负电,传统的去除水中胶体杂质方式是投加混凝剂(如聚合氯化铝)和助凝剂(如聚丙烯酰胺),使水中胶体形成大的絮凝体而通过重力沉淀去除。其主要机理之一就是吸附电中和作用,即混凝剂在水中水解出带正电的离子,中和胶体颗粒的负电荷,使胶体颗粒呈电中性状态,从而消除胶体颗粒之间的静电排斥作用,同时通过搅拌方式增加胶体之间的碰撞,使之絮凝成体积较大的絮凝体而从水中沉淀分离。混凝的其他机理还有吸附架桥、网捕卷扫作用等。混凝过程受多种因素的影响,如混凝剂的种类、水温(水温低不利于絮凝体形成)、pH值和碱度以及杂质的性质、组成和浓度等,以及絮凝阶段的速度梯度控制,这些因素和环节操作控制不好都会影响整个混凝效果。从混凝剂本身来看,有些混凝剂具有腐蚀性,要考虑设备、装置防腐措施;混凝剂粗制品中含有较高的不溶于水的杂质,废渣较多,使用麻烦。加之现在原水中污染物种类越来越多,混凝剂的投加也易引发二次污染。混凝剂的制备和投加方式要配有一套溶药、配药和投药的装置设备,难容药剂还需要加热促进溶解。混凝之后形成的絮凝体还需再设置沉淀池来进行重力沉淀去除,沉淀池的占地面积是相当大的,而现在用地情况紧张和昂贵。综上所述,现有传统处理原水胶体杂质的方式主要采用投药混凝处理的方法去除其中的胶体杂质,虽然能达到去除的效果,但过程冗长繁琐,易造成二次污染,产生过多污泥,增加环境负担。因此,研制开发利用电场耦合多级隔板加快胶体颗粒沉降的去除装置,不仅能提高胶体杂质沉降效率、降低药耗,运行过程实现自动排泥保证装置连续运行,对我国原水处理降低基建及运行成本、提高效率有现实意义。Colloids in water are generally negatively charged. The traditional way to remove colloid impurities in water is to add coagulants (such as polyaluminum chloride) and coagulants (such as polyacrylamide), so that colloids in water form large flocs and are removed by gravity precipitation . One of its main mechanisms is adsorption charge neutralization, that is, the coagulant hydrolyzes positively charged ions in water, neutralizes the negative charge of the colloidal particles, and makes the colloidal particles in an electrically neutral state, thereby eliminating the colloidal particles. At the same time, the collision between the colloids is increased by stirring, so that they flocculate into larger flocs and are precipitated and separated from the water. Other mechanisms of coagulation include adsorption bridging, net capture and sweeping, etc. The coagulation process is affected by many factors, such as the type of coagulant, water temperature (low water temperature is not conducive to floc formation), pH and alkalinity, as well as the nature, composition and concentration of impurities, etc., as well as velocity gradient control in the flocculation stage , These factors and poor link operation control will affect the entire coagulation effect. From the point of view of the coagulant itself, some coagulants are corrosive, and anti-corrosion measures for equipment and devices should be considered; the crude coagulant product contains high water-insoluble impurities, and there are many waste residues, which are troublesome to use. In addition, there are more and more types of pollutants in raw water, and the addition of coagulants can easily lead to secondary pollution. The preparation and dosing method of the coagulant should be equipped with a set of equipment for dissolving, dispensing and dosing. The flocs formed after coagulation need to be further set up in a sedimentation tank for gravity sedimentation removal. The area of the sedimentation tank is quite large, and now the land is tense and expensive. To sum up, the existing traditional methods of treating raw hydrocolloid impurities mainly use the method of drug administration and coagulation to remove the colloid impurities. Although the removal effect can be achieved, the process is tedious and cumbersome, and it is easy to cause secondary pollution and excessive pollution. Mud, increasing the burden on the environment. Therefore, the research and development of a removal device that utilizes electric field coupled with multi-stage separators to accelerate the sedimentation of colloidal particles can not only improve the sedimentation efficiency of colloidal impurities, reduce the consumption of chemicals, but also realize the automatic sludge discharge during the operation process to ensure the continuous operation of the device, and reduce the infrastructure and operation of raw water treatment in my country. cost and improve efficiency have practical significance.
发明内容SUMMARY OF THE INVENTION
为了解决上述现有技术存在的不足和缺点,本发明目的在于提供了一种静电场力耦合多级隔板水力作用去除胶体杂质的装置。该装置利用胶体颗粒表面荷负电的特性,巧设多级隔板导流,形成更有利的水力学条件,使胶体颗粒都能处于更有利沉降的条件,提高胶体杂质沉降效率,降低药耗,运行过程实现自动排泥保证装置连续运行。In order to solve the above-mentioned deficiencies and shortcomings of the prior art, the purpose of the present invention is to provide a device for removing colloidal impurities by electrostatic field force coupling multi-stage separator hydraulic action. The device utilizes the characteristics of negative charge on the surface of colloidal particles, and cleverly sets up multi-stage baffles for diversion to form more favorable hydraulic conditions, so that colloidal particles can be in more favorable conditions for sedimentation, improve the sedimentation efficiency of colloidal impurities, and reduce drug consumption. The operation process realizes automatic sludge discharge to ensure the continuous operation of the device.
本发明的目的通过下述技术方案来实现:The object of the present invention is achieved through the following technical solutions:
一种静电场力耦合多级隔板水力作用去除胶体杂质的装置,所述装置包括沉降室和电场发生装置,所述沉降室内设有多级导流隔板和排污装置,所述多级导流隔板分为上隔板和下隔板,所述上隔板和下隔板之间错开排布,将所述沉降室间隔成若干个彼此连通的处理单元;在所述沉降室的顶端两侧分别设有进水口和出水口;所述排污装置设置在所述处理单元的底端,所述电场发生装置设有阳极板和阴极板,所述阳极板平行设置在所述沉降室的外部底端,所述阴极板平行设置在所述沉降室的外部顶端,所述阳极板和阴极板通过外电源连接。A device for removing colloidal impurities by electrostatic field force coupling multi-stage separator hydraulic action, the device comprises a settling chamber and an electric field generating device, the settling chamber is provided with a multi-stage flow-guiding separator and a sewage discharge device, the multi-stage guide The flow baffle is divided into an upper baffle and a lower baffle, and the upper baffle and the lower baffle are staggered and arranged to separate the settling chamber into several processing units that communicate with each other; at the top of the settling chamber The two sides are respectively provided with a water inlet and a water outlet; the sewage device is arranged at the bottom end of the treatment unit, the electric field generating device is provided with an anode plate and a cathode plate, and the anode plate is arranged in parallel at the bottom of the sedimentation chamber. At the outer bottom end, the cathode plate is arranged in parallel at the outer top end of the sedimentation chamber, and the anode plate and the cathode plate are connected through an external power source.
优选地,所述上隔板的底端与所述沉降室的内部底端的距离为d1,所述上隔板和下隔板的间距为d2,d1与d2满足d1=(1.4~1.7)*d2。Preferably, the distance between the bottom end of the upper partition plate and the inner bottom end of the sedimentation chamber is d 1 , the distance between the upper partition plate and the lower partition plate is d 2 , and d 1 and d 2 satisfy d 1 =( 1.4 to 1.7)*d 2 .
进一步地,所述上隔板的底端为三角结构。Further, the bottom end of the upper baffle is a triangular structure.
进一步地,所述下隔板的顶端与所述沉降室的内部顶端的距离为d3,d3与所述出水口的直径相同。Further, the distance between the top end of the lower partition plate and the inner top end of the settling chamber is d 3 , and d 3 is the same as the diameter of the water outlet.
优选地,所述上隔板和下隔板的长度均为所述沉降室的高度的3/5~3/4。Preferably, the lengths of the upper baffle and the lower baffle are both 3/5 to 3/4 of the height of the sedimentation chamber.
进一步地,所述排污装置包括排泥斜板、排泥凹槽和排泥管;所述排泥斜板设置在所述沉降室的内部底端,所述排泥斜板的低端与所述排泥凹槽连接,所述排泥管与所述排泥凹槽连接,在所述排泥管上设置阀门,能自动控制所述排泥管的关启,实现自动排泥。Further, the sewage discharge device includes a mud discharge inclined plate, a mud discharge groove and a mud discharge pipe; the mud discharge inclined plate is arranged at the inner bottom end of the sedimentation chamber, and the lower end of the mud discharge inclined plate is connected to the bottom end of the mud discharge inclined plate. The mud discharge groove is connected, the mud discharge pipe is connected with the mud discharge groove, and a valve is arranged on the mud discharge pipe, which can automatically control the closing and opening of the mud discharge pipe to realize automatic mud discharge.
更进一步地,所述排泥斜板的斜率为3~5%;所述排泥凹槽的斜率为2~4%。Further, the slope of the mud discharge inclined plate is 3-5%; the slope of the mud discharge groove is 2-4%.
进一步地,所述排污装置还包括浊度传感器,所述浊度传感器设置在所述排泥管的进口上端;所述浊度传感器与自动排污控制装置连接,自动控制所述阀门的启动和关闭。Further, the sewage discharge device further includes a turbidity sensor, and the turbidity sensor is arranged at the upper end of the inlet of the mud discharge pipe; the turbidity sensor is connected to an automatic sewage discharge control device to automatically control the start and close of the valve. .
更进一步地,所述自动排污控制装置包括单片机、马达和电源,所述马达和浊度传感器并联于所述单片机的工作端,所述单片机连于所述电源。Furthermore, the automatic sewage control device includes a single-chip microcomputer, a motor and a power supply, the motor and the turbidity sensor are connected in parallel with the working end of the single-chip microcomputer, and the single-chip microcomputer is connected to the power supply.
一种实现所述的静电场力耦合多级隔板水力作用去除胶体杂质的装置的方法,包括如下具体步骤:A method for realizing the device for removing colloidal impurities by the electrostatic field force coupling multi-stage separator hydraulic action, comprising the following specific steps:
S1.将污水先从沉降室的进水口注入沉降室,顺着多级导流隔板往下流动,随水流靠近沉降室底端的阳极板,使杂质从水中分离,澄清后水流则继续顺着多级导流隔板往上流动,这个过程水中杂质受到电场力作用继续往下沉淀,与水流方向相反,发生相背向分离,再次澄清的水从下隔板上部流过,经过沉降室的多级串联的的处理单元反复处理去除胶体杂质后,澄清水从沉降室的出水口流出;S1. The sewage is first injected into the sedimentation chamber from the water inlet of the sedimentation chamber, and flows down along the multi-stage diversion baffle, and approaches the anode plate at the bottom of the sedimentation chamber with the water flow to separate impurities from the water. After clarification, the water flow continues to follow The multi-level deflector baffles flow upward. In this process, the impurities in the water continue to settle down under the action of the electric field force, which is opposite to the direction of the water flow, and the phase separation occurs. The re-clarified water flows from the upper part of the lower baffle and passes through the sedimentation chamber After the multi-stage series-connected treatment units repeatedly process and remove colloidal impurities, the clarified water flows out from the water outlet of the sedimentation chamber;
S2.同时沉淀的杂质污泥沿着排泥斜板滑向排泥凹槽,当排泥凹槽的杂质沉淀过多,排污装置通过浊度传感器感应自动控制排泥管上阀门的开启和关闭,再由经排泥管排出,实现水处理过程中的自动排泥。S2. At the same time, the sedimented impurity sludge slides to the sludge discharge groove along the sludge discharge inclined plate. When the impurities in the sludge discharge groove are too much, the sewage device automatically controls the opening and closing of the valve on the sludge discharge pipe through the turbidity sensor induction. , and then discharged through the sludge discharge pipe to realize automatic sludge discharge in the process of water treatment.
本发明利用外加电场作用力,根据原水胶体杂质的带电特性迫使胶体沉降实现从水中分离,同时依据沉降过程的理论,巧设多级隔板导流,形成更有利的水力学条件,使胶体颗粒都能处于更有利沉降的条件,极大提高去污效率,提高出水水质。对于沉淀在底部的高浓度沉淀物,通过设置斜坡、斜槽以及自动排污系统实现沉淀杂质的智能排出,整个沉降装置能自行连续运转,达到去污排污的目的。The present invention utilizes the force of an external electric field to force the colloid to settle to realize separation from water according to the charged characteristics of the raw hydrocolloid impurities, and at the same time, according to the theory of the settling process, multi-stage baffles are skillfully set up to guide the flow to form more favorable hydraulic conditions, so that the colloid particles can be separated from the water. All can be in more favorable conditions for sedimentation, greatly improving the decontamination efficiency and improving the effluent quality. For the high-concentration sediment deposited at the bottom, the intelligent discharge of sedimented impurities is realized by setting up slopes, inclined grooves and an automatic sewage system. The entire settling device can run continuously by itself to achieve the purpose of sewage removal.
与传统的不主动消除胶体电荷的方法相反,本发明去除水中胶体的原理是利用胶体颗粒的带电性,外加静电场耦合多级隔板,使其在静电场力作用下加快沉降而从水中分离出来,同时也能去除部分溶解质离子杂质。由于水中胶体一般带有负电荷,本发明装置设计的场强方向竖直向下,即带有正电荷的正极板在下,带有负电荷的负极板在上,两块金属板平行放置。原水从电场中流过,水中胶体所受的电场力方向竖直向下,与重力方向一致,胶体所受的向下合力更大而更易发生沉降,从而实现从水中分离。研究人员曾用过外加电场方法处理煤泥颗粒,但其水流方向是简单地平行向前推进的,上层水体永远处于上层,其中的煤泥颗粒可能来不及沉淀便随出水一起排出,得不到去除,同时也浪费了容积的空间。Contrary to the traditional method of not actively eliminating the colloid charge, the principle of the present invention to remove the colloid in water is to use the electrification of the colloid particles and add an electrostatic field to couple the multi-stage separator, so that it can accelerate the sedimentation and separate from the water under the action of the electrostatic field force. At the same time, it can also remove part of the solute ion impurities. Since colloids in water generally have negative charges, the field strength direction of the device of the present invention is designed vertically downward, that is, the positive plate with positive charge is below, the negative plate with negative charge is above, and the two metal plates are placed in parallel. When the raw water flows through the electric field, the direction of the electric field force on the colloid in the water is vertically downward, which is consistent with the direction of gravity. Researchers have used the method of external electric field to treat coal slime particles, but the direction of water flow is simply forward in parallel, and the upper water body is always in the upper layer, and the coal slime particles in it may be discharged together with the effluent before it settles and cannot be removed. , while also wasting volume space.
本发明利用原水胶体颗粒带电的特性,外加电场,使其受到竖直向下的电场力,与重力方向一致,竖直向下合力增大,从而更快发生沉降分离。设置了多级隔板,引导水流,保证水中的胶体颗粒全部都能流经下方受到最强的电场力,保证全部受到最佳去除效果作用,更快得到去除。同等容积下,隔板的设置极大提高了胶体颗粒的沉降效果,显著提高出水的水质。在排泥管上设置自动排泥系统控制阀门的关闭和启动,实现自动排泥,使装置能连续运行地工作。The invention utilizes the charged characteristic of the raw hydrocolloid particles, and applies an electric field to make them subject to a vertical downward electric field force, which is consistent with the direction of gravity, and the vertical downward resultant force increases, so that sedimentation and separation occur faster. A multi-stage separator is set up to guide the water flow, ensuring that all the colloidal particles in the water can flow through the bottom and receive the strongest electric field force, ensuring that they all receive the best removal effect and are removed faster. Under the same volume, the setting of the separator greatly improves the sedimentation effect of colloidal particles and significantly improves the quality of the effluent. An automatic sludge discharge system is set on the sludge discharge pipe to control the closing and start of the valve to realize automatic sludge discharge, so that the device can work continuously.
本发明上隔板的底端与沉降室底部之间的距离要比隔板间的距离大,即水流的底部水平通道要比水流的竖直通道宽。根据v=Q/A(Q为流量,A为水流通道横截面积,v为流速),Q同样,A越大则v越小。沉降室底部流速减少则其水力停留时间越长,更加有力与胶体杂质的充分沉降。上隔板的底端设计成三角结构,是为了防止水流发生短流直接绕过隔板而沿隔板往上流,从而导致其中的胶体杂质来不及沉淀,该结构同时能够防止已沉降的胶体杂质被再次掀起。The distance between the bottom end of the upper partition plate and the bottom of the sedimentation chamber is larger than the distance between the partition plates, that is, the bottom horizontal channel of the water flow is wider than the vertical channel of the water flow. According to v=Q/A (Q is the flow rate, A is the cross-sectional area of the water flow channel, and v is the flow velocity), Q is the same, the larger the A, the smaller the v. The lower the flow velocity at the bottom of the sedimentation chamber, the longer the hydraulic retention time, and the more powerful and sufficient sedimentation of colloidal impurities. The bottom end of the upper baffle is designed as a triangular structure, in order to prevent the short flow of the water flow from bypassing the baffle and flowing upward along the baffle, thus causing the colloidal impurities in it to settle too late. This structure can also prevent the settled colloidal impurities from being deposited. set off again.
所述上隔板与所述沉降室的底部之间的距离要大于隔板间的距离,保证水流在底部时流变小,利于水中胶体的沉降,同时防止流速变大而引起底部已沉降的杂质掀起重新回到水体中。阴极板在所述沉降室的外部顶端,阳极板在所述沉降室的外部底端,阳极板和阴极板位置不可调换。水体中胶体一般带负电,目前去除水中胶体杂质的混凝方法也是直接默认水中胶体为负电性,这里的污泥就是沉淀下来的胶体杂质,所以也带负电。要保证水中带负电的胶体杂质受到的电场力竖值向下,与重力方向一致,使胶体杂质受到最大的向下合力,更好地发生沉降从水中脱离。The distance between the upper clapboard and the bottom of the sedimentation chamber should be greater than the distance between the clapboards, to ensure that the flow of water at the bottom becomes smaller, which is conducive to the settlement of colloids in the water, and at the same time prevents the flow rate from becoming larger and causing the bottom to settle. Impurities are lifted back into the water body. The cathode plate is at the outer top of the sedimentation chamber, the anode plate is at the outer bottom of the sedimentation chamber, and the positions of the anode plate and the cathode plate cannot be exchanged. Colloids in water are generally negatively charged. At present, the coagulation method to remove colloidal impurities in water also directly defaults to the negative charge of colloids in water. The sludge here is the colloidal impurities that have settled down, so it is also negatively charged. It is necessary to ensure that the vertical value of the electric field force on the negatively charged colloidal impurities in the water is downward, which is consistent with the direction of gravity, so that the colloidal impurities are subjected to the maximum downward force, and the sedimentation and separation from the water are better.
与现有技术相比,本发明具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
1.本发明根据原水胶体杂质的带电特性,利用外加电场作用力迫使胶体沉降实现从水中分离,同时依据沉降过程的理论,巧设多级隔板导流,形成更有利的水力学条件,使胶体颗粒都能处于更有利沉降的条件,极大提高去污效率,保障出水水质。对于沉淀在底部的高浓度沉淀物,设置斜坡、斜槽以及自动排污系统实现沉淀杂质的智能排出,整个沉降装置能自行连续运转,达到净化水质排出沉淀污泥的目的。1. According to the charged characteristics of raw hydrocolloid impurities, the present invention utilizes the force of an external electric field to force colloid sedimentation to realize separation from water, and at the same time, according to the theory of sedimentation process, skillfully set up multi-stage baffles for diversion to form more favorable hydraulic conditions, so that The colloidal particles can be in more favorable conditions for sedimentation, which greatly improves the decontamination efficiency and ensures the quality of the effluent. For the high-concentration sediment that settles at the bottom, slopes, chutes and automatic sewage systems are set up to realize the intelligent discharge of precipitated impurities.
2.本发明采用上下错开排布的多级导流隔板,改变沉降水力条件,可增大水力的停留时间,改善沉降的结构性能,提高胶体杂质在装置中的沉降效率,同时显著提高了胶体杂质去除率和容积利用率,有效减少占地面积。多级导流隔板可使水流向下从底部流过,起到导流的作用,保证水中全部胶体杂质都更加靠近正极板,所受电场力更强,能更快速沉降而从水中分离。在水流向上运动的过程中,水与其中胶体杂质发生相对运动,促进杂质与水的分离。如此多级过程极大提高胶体杂质去除率,保证出水水质。2. The present invention adopts the multi-level diversion baffles arranged up and down staggered to change the hydraulic conditions of settlement, which can increase the hydraulic retention time, improve the structural performance of the settlement, improve the settlement efficiency of colloidal impurities in the device, and at the same time significantly improve the sedimentation efficiency. The colloidal impurity removal rate and volume utilization rate can effectively reduce the floor space. The multi-level diversion baffle can make the water flow downward from the bottom, and play the role of diversion, ensuring that all colloidal impurities in the water are closer to the positive plate, the electric field force is stronger, and it can settle more quickly and separate from the water. During the upward movement of the water flow, the water and the colloidal impurities in it move relative to each other, which promotes the separation of the impurities and the water. Such a multi-stage process greatly improves the removal rate of colloidal impurities and ensures the quality of the effluent.
3.本发明的上隔板的底端为三角形结构,以防止水流发生短流,绕过隔板直接往上流动,从而导致胶体杂质来不及发生沉淀的问题。3. The bottom end of the upper clapboard of the present invention has a triangular structure to prevent the water flow from short-circuiting, bypassing the clapboard and directly flowing upward, thereby causing the problem that the colloidal impurities are too late to precipitate.
4.随着胶体颗粒的不断沉降,沉淀的底泥越来越多,需要进行排放清除,本发明利用浊度传感仪和单片机实现排泥管上阀门的开启和关闭,可实现自动排泥。4. With the continuous settling of colloidal particles, more and more sediments are deposited, which needs to be discharged and removed. The present invention utilizes a turbidity sensor and a single-chip microcomputer to realize the opening and closing of the valve on the mud discharge pipe, which can realize automatic mud discharge. .
5.相对于传统混凝沉淀过程去除原水中胶体悬浮杂质的方法,本发明无需过多投加药剂,不造成二次污染,不产生额外的沉淀污泥,不增加污泥处理负担。装置操作运行简单,无需混凝药剂溶解、配制和投加等操作控制过程以及设置相应的池子,也不需再设占地面积较大的沉淀池另外进行沉淀。充分利用胶体本身带电特性,巧设结构外加电场将其去除。5. Compared with the method of removing colloidal suspended impurities in raw water in the traditional coagulation and sedimentation process, the present invention does not need to add too many chemicals, does not cause secondary pollution, does not generate additional sedimentary sludge, and does not increase the burden of sludge treatment. The operation of the device is simple, and there is no need for operation control processes such as coagulation agent dissolution, preparation and dosing, as well as the setting of corresponding pools, and there is no need to set up a larger area of the sedimentation tank for additional sedimentation. Make full use of the charged characteristics of the colloid itself, and cleverly set up the structure and apply an electric field to remove it.
附图说明Description of drawings
图1为本发明的静电场力耦合多级隔板水力作用去除胶体杂质的装置的结构示意图;1 is a schematic structural diagram of a device for removing colloidal impurities by electrostatic field force coupling multi-stage separator hydraulic action of the present invention;
图2为本发明装置的左剖面图;Fig. 2 is the left sectional view of the device of the present invention;
图3为本发明的装置中自动排污控制系统示意图。FIG. 3 is a schematic diagram of the automatic sewage control system in the device of the present invention.
具体实施方式Detailed ways
下面结合具体实施例进一步说明本发明的内容,但不应理解为对本发明的限制。若未特别指明,实施例中所用的技术手段为本领域技术人员所熟知的常规手段。除非特别说明,本发明采用的试剂、方法和设备为本技术领域常规试剂、方法和设备。The content of the present invention is further described below in conjunction with specific embodiments, but should not be construed as a limitation of the present invention. Unless otherwise specified, the technical means used in the examples are conventional means well known to those skilled in the art. Unless otherwise specified, the reagents, methods and equipment used in the present invention are conventional reagents, methods and equipment in the technical field.
实施例1Example 1
图1为本发明的静电场力耦合多级隔板水力作用去除胶体杂质的装置的结构示意图。如1图所示,所述装置包括沉降室9和电场发生装置6,所述沉降室9内设有多级导流隔板2和排污装置,所述多级导流隔板2分为上隔板和下隔板,所述上隔板和下隔板之间错开排布,将所述沉降室间隔成若干个彼此连通的处理单元;在所述沉降室9的顶端两侧分别设有进水口1和出水口3;所述排污装置12设置在所述处理单元的底端,所述电场发生装置设有阳极板5和阴极板4,所述阳极板5平行设置在所述沉降室9的外部底端,所述阴极板4平行设置在所述沉降室9的外部顶端,使水中带负电胶体杂质所受的电场力竖直向下,与重力方向一致,增大向下其沉降的合力,所述阳极板5和阴极板4通过外电源连接。FIG. 1 is a schematic structural diagram of a device for removing colloidal impurities by electrostatic field force coupling multi-stage separator hydraulic action according to the present invention. As shown in Figure 1, the device includes a settling
→↑↓代表水流方向,采用上下错开排布的多级隔板,增大了水力的停留时间,显著提高胶体杂质去除率,容积利用率高,减少占地面积。改变沉降水力条件,改善沉降的结构性能,提高胶体杂质在装置中的沉降效率,同时提高容积利用率。导流隔板使水流向下从沉降室的底部流过,保证水中全部胶体杂质都更加靠近正极板,所受电场力更强,能更快速沉降而从水中分离。在水流向上运动的过程中,水与其中胶体杂质发生相对运动,促进杂质与水的分离。如此多级过程极大提高胶体杂质去除率,保证出水水质。→↑↓ represents the direction of water flow. The multi-stage separators arranged up and down are staggered, which increases the hydraulic retention time, significantly improves the removal rate of colloidal impurities, and has high volume utilization rate and reduced floor space. Change the hydraulic conditions of sedimentation, improve the structural performance of sedimentation, improve the sedimentation efficiency of colloidal impurities in the device, and improve the volume utilization rate. The diversion baffle makes the water flow downward from the bottom of the sedimentation chamber to ensure that all the colloidal impurities in the water are closer to the positive plate, and the electric field force is stronger, which can settle faster and separate from the water. During the upward movement of the water flow, the water and the colloidal impurities in it move relative to each other, which promotes the separation of the impurities and the water. Such a multi-stage process greatly improves the removal rate of colloidal impurities and ensures the quality of the effluent.
所述上隔板的底端与所述沉降室9的内部底端的距离为d1,所述上隔板和下隔板的间距为d2,d1与d2满足d1=(1.4~1.7)*d2。所述上隔板与所述沉降室的底部之间的距离要大于隔板间的距离,保证水流在底部时流变小,利于水中胶体的沉降,同时防止流速变大而引起底部已沉降的杂质掀起重新回到水体中。The distance between the bottom end of the upper partition plate and the inner bottom end of the
所述上隔板的底端为三角结构,以防止水流发生短流,绕过隔板直接往上流动,导致胶体杂质来不及发生沉淀的问题。The bottom end of the upper baffle is a triangular structure to prevent the water flow from short-circuiting, bypassing the baffle and directly flowing upwards, resulting in the problem that the colloidal impurities are too late to precipitate.
所述下隔板的顶端与所述沉降室9的内部顶端的距离为d3,d3与所述出水口3的直径相同。The distance between the top end of the lower partition plate and the inner top end of the settling
所述上隔板和下隔板的长度均为所述沉降室9的高度的3/5~3/4。The lengths of the upper and lower partitions are both 3/5 to 3/4 of the height of the
图2为本发明装置的左剖面图,如图2所示,所述排污装置包括排泥斜板13、排泥凹槽14和排泥管10;所述排泥斜板13设置在所述沉降室9的内部底端,所述排泥斜板13的低端与所述排泥凹槽14连接,所述排泥管10与所述排泥凹槽14连接,在所述排泥管10上设置阀门11,能自动控制所述排泥管的关启,实现自动排泥。Fig. 2 is a left sectional view of the device of the present invention. As shown in Fig. 2, the sewage discharge device includes a mud discharge inclined
所述排泥斜板13的斜率为3~5%;所述排泥凹槽14的斜率为2~4%。The slope of the mud discharge inclined
所述排污装置还包括浊度传感器15,所述浊度传感器15设置在所述排泥管10的进口上端;所述浊度传感器15与自动排污控制装置12连接,自动控制所述阀门11的启动和关闭,实现自动排泥,使装置能连续运行地工作。The sewage discharge device also includes a
所述自动排污控制装置12包括单片机、马达和电源,所述马达和浊度传感器15并联于所述单片机的工作端,所述单片机连于所述电源。The automatic
工作原理如图3所示,所述马达和浊度传感器并联连单片机下一工作端,所述单片机连于所述电源,所述浊度传感器15设置在所述排泥管10的进口上端;对于沉淀在底部的高浓度沉淀物,设置排泥斜板13、排泥凹槽14以及自动排污控制装置12实现沉淀杂质的智能排出,整个沉降装置能连续运转,达到去污排污的目的。The working principle is shown in FIG. 3 , the motor and the turbidity sensor are connected in parallel to the next working end of the single-chip microcomputer, the single-chip microcomputer is connected to the power supply, and the
工作时,水先从上面的进水口1流入沉降室9,为了防止进水水流扰动掀起底部沉淀的杂质,进水口1设置在沉降室9的上部,顺着多级导流隔板2往下流动,随水流靠近沉降室9底端的阳极板5,在底部流动过程中带负电的胶体杂质受到电场力作用,并在沉降室9的底部发生沉淀使杂质从水中分离。澄清后水流则继续顺着多级导流隔板2往上流动,这个过程水中杂质受到电场力作用继续往下沉淀,与水流方向相反,发生相背向分离,再次澄清的水从下隔板上部流过,接着进行下一级的反复处理,经过多级串联的沉降室处理单元去除胶体杂质后,澄清水从装置末端的出水口3流出。沉淀下来的杂质污泥沿着排泥斜板13滑向排泥凹槽14,再由经排泥管10排除。排泥管口上阀门的关闭和启动由污泥排污系统自动控制。随着胶体杂质的不断沉淀,底部的浊度慢慢增大,当增大到一定数值,排泥管10的阀门11打开,随着高浊度的沉淀污水不断外排,底部水中浊度慢慢下降,当下降到一定浊度,则阀门11关闭。整个装置集胶体杂质分离和沉淀以及污泥自动排放等功能于一身,效率高,占地面积小,装置简单,对原水处理具有很重要的现实意义。When working, the water first flows into the
实施例2Example 2
如图1所示,→↑↓代表水流方向,水流从左往右推走过程中,是一下一上反复进行三次,即沉降室9内部可分为三个串联的相同的处理单元,也就是每一个上隔板所对应的空间对一级处理单元,总共有三级,每一级处理单元设一个排污装置。所述排污装置还包括浊度传感器15,所述浊度传感器15设置在所述排泥管10的进口上端;所述浊度传感器15与自动排污控制装置12连接,自动控制所述阀门11的启动和关闭,实现自动排泥,使装置能连续运行地工作。As shown in Figure 1, →↑↓ represents the direction of water flow. During the process of water flow pushing away from left to right, it is repeated three times from one to the other, that is, the interior of the
所述排泥斜板13的低端与所述排泥凹槽14连接,所述排泥管10设在每级处理单元中排泥斜板13的低端,并与所述排泥凹槽14连接,根据重力原理,污泥排向低处,在所述排泥管10上设置阀门11,能自动控制所述排泥管的关启,实现自动排泥。The lower end of the mud discharge inclined
如果上下隔板的长度为沉降室9高度的3/5,排泥斜板13的斜率为4%,斜坡下端排泥凹槽14向排泥管18倾斜(斜率2%)。原水从进水口1流入,随着渠道竖直往下流,水中胶体杂质也跟着靠近阳极板5,水流在隔板下面流速减缓变小,胶体杂质此时快速得到沉降。而后向上流动,此过程水与其中胶体杂质发生相对运动,促进杂质与水的分离,如此多级过程沉降使原水得到净化,处理后的从排出口3排出,进入其他的后续处理单元。沉淀下来的杂质顺着底部斜坡滑向排泥凹槽14,通过排泥凹槽14继续滑向排泥管10。当排泥斜板13的杂质沉淀过多,浊度变大,通过浊度传感器15的感应,控制排泥管的闸阀11的开启,当浊度下降后,控制闸阀11自动关闭,实现自动排泥,保证原水处理过程的连续运行。If the length of the upper and lower baffles is 3/5 of the height of the
上述实施例为本发明较佳的实施方式,但本发明的实施方式并不受上述实施例的限制,其他的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合和简化,均应为等效的置换方式,都包含在本发明的保护范围之内。The above-mentioned embodiments are preferred embodiments of the present invention, but the embodiments of the present invention are not limited by the above-mentioned embodiments, and any other changes, modifications, substitutions, combinations and The simplification should be equivalent replacement manners, which are all included in the protection scope of the present invention.
Claims (7)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010128456.1A CN111252871B (en) | 2020-02-28 | 2020-02-28 | Device for removing colloid impurities under action of static field force coupled with multistage partition plates and water power |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202010128456.1A CN111252871B (en) | 2020-02-28 | 2020-02-28 | Device for removing colloid impurities under action of static field force coupled with multistage partition plates and water power |
Publications (2)
Publication Number | Publication Date |
---|---|
CN111252871A CN111252871A (en) | 2020-06-09 |
CN111252871B true CN111252871B (en) | 2022-06-03 |
Family
ID=70944498
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202010128456.1A Active CN111252871B (en) | 2020-02-28 | 2020-02-28 | Device for removing colloid impurities under action of static field force coupled with multistage partition plates and water power |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN111252871B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112010500B (en) * | 2020-08-12 | 2022-10-14 | 阳江职业技术学院 | Internal circulation aquaculture water efficient purification device and use method thereof |
CN112813922B (en) * | 2021-01-06 | 2022-05-17 | 西南科技大学 | Active-passive debris flow water-stone separation-energy dissipation disaster reduction device |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1980002716A1 (en) * | 1979-05-31 | 1980-12-11 | Sredneaziat Nii Prirod Gaza | Device for rectification of drilling mud |
CN102757143A (en) * | 2012-08-14 | 2012-10-31 | 成都凯迈科技有限公司 | Well drilling wastewater flocculation precipitation treatment device and wastewater treating method |
CN202538432U (en) * | 2012-04-12 | 2012-11-21 | 安徽理工大学 | 'Three in one' alternating electric field accelerated slime water settling tank |
CN103086574A (en) * | 2013-02-27 | 2013-05-08 | 青岛理工大学 | Aquatic product processing wastewater treatment equipment |
CN105609847A (en) * | 2016-03-01 | 2016-05-25 | 大连理工大学 | Apparatus for realizing surplus sludge disposal and membrane filtration through coupled single-chamber inclined-plate multi-positive-electrode microbial fuel cell |
CN205653285U (en) * | 2016-06-01 | 2016-10-19 | 北京中科奥倍超声波技术研究院 | Ultrasonic coupling multipole formula electrocoagulation - electric superficial reaction unit |
CN110183068A (en) * | 2019-07-12 | 2019-08-30 | 天津市政公路设备工程有限公司 | A kind of food and drink waste water integration advanced treatment reactor |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE1009810A3 (en) * | 1995-12-07 | 1997-08-05 | Hugues A F Lahaut | Psychrometric probe with inter-meshed combs |
CN101229527B (en) * | 2008-01-07 | 2011-06-22 | 北京交通大学 | An electric field separation method and device for inorganic non-metallic colloidal particles |
CN101274791A (en) * | 2008-04-18 | 2008-10-01 | 北京工业大学 | Apparatus for Accelerating Sludge Settling Using Vertical Electrostatic Field |
CN101570369A (en) * | 2008-04-30 | 2009-11-04 | 北京锦奥华荣科技有限公司 | Method and device for purifying drinking water of polluted water source |
CN101880982A (en) * | 2009-05-06 | 2010-11-10 | 马顺根 | Vessel equipment for precipitation separation of water, printing ink and sludge |
CN102503069A (en) * | 2011-11-10 | 2012-06-20 | 天津大学 | Device and method for dehydrating and pelletizing sludge under synergic action of electric field and pressure |
CN203208732U (en) * | 2013-03-06 | 2013-09-25 | 宋建华 | Sand trap |
CN103545577B (en) * | 2013-09-30 | 2015-07-29 | 刘甲祥 | A kind of metal air fuel cell with cone-shaped metal anode |
CN203540208U (en) * | 2013-10-19 | 2014-04-16 | 甘肃酒钢集团宏兴钢铁股份有限公司 | Coking wastewater treatment device |
CN105417834A (en) * | 2015-12-30 | 2016-03-23 | 马鞍山清净环保科技有限公司 | Magnetorheological fluid recycling device and control method and component manufacturing method thereof |
CN106892487A (en) * | 2017-03-17 | 2017-06-27 | 上海复禹环境科技有限公司 | Vertical type cylinder type transverse direction flow-guiding type automatic scraping dirt electro-chemical water processing system |
CN207451727U (en) * | 2017-08-22 | 2018-06-05 | 福建微水环保股份有限公司 | A kind of sewage disposal anoxic pool structure |
CN109928468A (en) * | 2017-12-18 | 2019-06-25 | 天津大学 | A kind of DC electric field acts on the breaking method of lower oil-in-water emulsion |
-
2020
- 2020-02-28 CN CN202010128456.1A patent/CN111252871B/en active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1980002716A1 (en) * | 1979-05-31 | 1980-12-11 | Sredneaziat Nii Prirod Gaza | Device for rectification of drilling mud |
CN202538432U (en) * | 2012-04-12 | 2012-11-21 | 安徽理工大学 | 'Three in one' alternating electric field accelerated slime water settling tank |
CN102757143A (en) * | 2012-08-14 | 2012-10-31 | 成都凯迈科技有限公司 | Well drilling wastewater flocculation precipitation treatment device and wastewater treating method |
CN103086574A (en) * | 2013-02-27 | 2013-05-08 | 青岛理工大学 | Aquatic product processing wastewater treatment equipment |
CN105609847A (en) * | 2016-03-01 | 2016-05-25 | 大连理工大学 | Apparatus for realizing surplus sludge disposal and membrane filtration through coupled single-chamber inclined-plate multi-positive-electrode microbial fuel cell |
CN205653285U (en) * | 2016-06-01 | 2016-10-19 | 北京中科奥倍超声波技术研究院 | Ultrasonic coupling multipole formula electrocoagulation - electric superficial reaction unit |
CN110183068A (en) * | 2019-07-12 | 2019-08-30 | 天津市政公路设备工程有限公司 | A kind of food and drink waste water integration advanced treatment reactor |
Also Published As
Publication number | Publication date |
---|---|
CN111252871A (en) | 2020-06-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN207645995U (en) | One kind plus magnetic flocculation clarify sewage-treatment plant | |
CN105060434A (en) | Novel sedimentation clarification pool | |
CN102295371A (en) | Integrated-processing process for river bottom-mud dredging residual water and equipment thereof | |
CN108328786B (en) | Water treatment device and water treatment method | |
CN111252871B (en) | Device for removing colloid impurities under action of static field force coupled with multistage partition plates and water power | |
CN216946616U (en) | Magnetic coagulation-flocculation reaction device and high-turbidity wastewater ultrafiltration treatment system | |
CN210133923U (en) | Novel high-efficient sedimentation tank | |
CN110678244A (en) | Integrated high-efficiency sedimentation and flotation system for sedimentation and floating separation process and its driving method | |
CN104692559A (en) | High-density sedimentation and clarifying integrated device with square overall upper and lower cross sections for water treatment | |
CN205061779U (en) | Novel deposit depositing reservoir | |
CN215102771U (en) | Efficient muddy water treatment thickener with coagulation structure | |
CN203540146U (en) | Novel efficient physical-chemical water processing and precipitating device | |
CN211056859U (en) | Construction wastewater treatment system | |
CN219072151U (en) | Integrated pretreatment system for steel wastewater | |
KR100786774B1 (en) | Integrated precipitation device | |
CN204384990U (en) | A kind of recirculated cooling water lime soften for sewage clarification filtration treatment system | |
CN216997800U (en) | A high-efficiency mechanical clarification solid-liquid separation device integrating coagulation and sedimentation | |
CN102145928A (en) | Efficient flocculation method and device for sewage treatment | |
CN212523126U (en) | A high-efficient integrated device that deposits for groundwater is taken out and is handled | |
CN1850663B (en) | Method for realizing sewage deep purification treatment using suspension filtering film | |
CN116036984A (en) | A new type of granulation fluidized bed integrating multiple functions | |
CN116903106A (en) | A clarification system and method for low-temperature and low-turbidity water | |
CN210001703U (en) | electric flocculation-slow decarburization combined water treatment equipment | |
CN103641259B (en) | Desulfurization wastewater treatment device | |
CN203284238U (en) | Micro-vortex efficient clarifying reactor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |