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CN205699790U - A kind of swash plate filter-cloth filtering device and control method - Google Patents

A kind of swash plate filter-cloth filtering device and control method Download PDF

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CN205699790U
CN205699790U CN201620298841.XU CN201620298841U CN205699790U CN 205699790 U CN205699790 U CN 205699790U CN 201620298841 U CN201620298841 U CN 201620298841U CN 205699790 U CN205699790 U CN 205699790U
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filter cloth
pipe
swash plate
water
plate filter
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于鹏飞
马兴冠
唐婧
黄殿男
傅金祥
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Shenyang Jianzhu University
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Shenyang Jianzhu University
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Abstract

一种斜板滤布过滤装置及控制方法,属于环境水污染控制领域,包括池体、斜板滤布盘片、集水管、投药混合系统、清洗系统、排泥系统。进水管、安装在池体底部一侧,出水管安装在池体的另一侧,排泥管布置在池底,进水管进口处设置有加药口,进水管与管式混合器相连接,管式混合器上布置分水口,斜板滤布盘片固定于池体中央,吸泥管靴由吸泥泵连接并紧贴滤布布置,集水管与斜板滤布盘片连接,集水横管与集水管相连接,集水管与集水渠相通,池体上方桁架上安有行车。装置运行方式采取异、侧向流过滤沉淀同步方式运行,运行分为药剂混合、过滤、沉淀排泥、反洗程序。本实用新型具有处理效率高、出水水质良好、占地小等优点,是污水厂深度处理工艺合适选择。

A slanting plate filter cloth filtering device and a control method belong to the field of environmental water pollution control, and include a pool body, a slanting plate filter cloth disc, a water collection pipe, a drug feeding and mixing system, a cleaning system, and a mud discharge system. The water inlet pipe is installed on one side of the bottom of the pool body, the water outlet pipe is installed on the other side of the pool body, the mud discharge pipe is arranged at the bottom of the pool, the entrance of the water inlet pipe is provided with a dosing port, and the water inlet pipe is connected to the tubular mixer. The water diversion port is arranged on the tubular mixer, the inclined plate filter cloth disc is fixed in the center of the pool body, the suction pipe shoe is connected by the dredge pump and arranged close to the filter cloth, the water collecting pipe is connected with the inclined plate filter cloth disc, and the water collecting The horizontal pipe is connected with the water collecting pipe, the water collecting pipe is connected with the water collecting canal, and the truss above the pool body is equipped with a driving vehicle. The operation mode of the device adopts the simultaneous operation of different and lateral flow filtration and sedimentation, and the operation is divided into medicament mixing, filtration, sedimentation and sludge discharge, and backwashing procedures. The utility model has the advantages of high treatment efficiency, good effluent quality, small footprint, etc., and is a suitable choice for the advanced treatment process of sewage plants.

Description

一种斜板滤布过滤装置及控制方法An inclined plate filter cloth filter device and control method

技术领域 technical field

本实用新型属于环境水污染控制领域,特别涉及污水深度处理设备及控制技术领域。尤其是一种斜板滤布过滤装置及控制方法。 The utility model belongs to the field of environmental water pollution control, in particular to the field of advanced sewage treatment equipment and control technology. In particular, a slanting plate filter cloth filtering device and a control method.

背景技术 Background technique

过滤,通常分为表面过滤和深层过滤,表面过滤是指污染物颗粒被截留在介质表面,一段时间形成滤渣层,由介质和滤渣层共同起过滤介质作用,如膜过滤、纤维转盘过滤器等;深层过滤是指污染物颗粒被截留于介质内部的孔隙中,如活性砂滤池、V形滤池等。目前世界上滤型先进且应用广泛的表面过滤器应属纤维转盘滤池(滤布滤池),目前在全世界已经有700个污水厂采用该项技术。滤布转盘过滤器的出水水质高,处理效果好,设备运行稳定。 Filtration is usually divided into surface filtration and depth filtration. Surface filtration means that pollutant particles are trapped on the surface of the medium, and a filter residue layer is formed for a period of time. The medium and the filter residue layer work together as a filter medium, such as membrane filtration, fiber rotary disc filter, etc. ; Depth filtration means that pollutant particles are trapped in the pores inside the medium, such as activated sand filters, V-shaped filters, etc. At present, the most advanced and widely used surface filter in the world should be a fiber rotary disc filter (filter cloth filter). At present, 700 sewage plants around the world have adopted this technology. The effluent water quality of the filter cloth rotary disc filter is high, the treatment effect is good, and the equipment operates stably.

滤布滤池适合于雨水处理、冷却循环水处理、废水的深度处理及再生利用。进水水质SS≤30mg/L以下,出水水质SS≤10mg/L。 用于污水的深度处理,设置于常规活性污泥法、SBR系统、氧化沟系统等生化处理之后,主要用于去除总悬浮固体,结合投加药剂后也可去除磷、重金属等。 Cloth filter is suitable for rainwater treatment, cooling circulating water treatment, advanced treatment and recycling of wastewater. Influent water quality SS≤30mg/L, effluent water quality SS≤10mg/L. It is used for the advanced treatment of sewage, after biochemical treatment such as conventional activated sludge method, SBR system, oxidation ditch system, etc. It is mainly used to remove total suspended solids, and it can also remove phosphorus and heavy metals after adding chemicals.

滤布滤池工艺将过滤和沉淀集中在同一滤池内完成,主要由滤布滤盘、清洗装置、集水装置及排泥装置组成,原水进入滤池特殊处理消能后,通过微孔滤布盘片,固体悬浮物被滤布截留在外侧绒毛上,过滤液通过中空集水管收集,通过重力流溢流槽排出滤池。由于悬浮杂质吸附于滤布外侧绒毛,逐渐形成滤渣层,随着滤布上滤渣层的积累,滤布过滤阻力增加,池内液位逐渐升高,当液位上升到设定值时,开启反抽吸泵及传动装置,圆盘转动过程中,固定于滤布外侧的刮板与滤布表面摩擦,刮去滤布表面的污泥,同时圆盘内的水被由内向外抽吸,清洗滤布微孔中的污泥,池底设排泥管,通过时间设定,开启排泥泵将污泥排出。 The filter cloth filter process concentrates filtration and sedimentation in the same filter tank, which is mainly composed of filter cloth filter disc, cleaning device, water collection device and mud discharge device. After the raw water enters the filter tank for special treatment and energy dissipation, it passes through the microporous filter Cloth disk, solid suspended solids are trapped on the outer fluff by the filter cloth, the filtrate is collected through the hollow water collection pipe, and discharged from the filter through the gravity overflow tank. Due to the adsorption of suspended impurities on the outer fluff of the filter cloth, a filter residue layer is gradually formed. With the accumulation of the filter residue layer on the filter cloth, the filter resistance of the filter cloth increases, and the liquid level in the pool gradually rises. Suction pump and transmission device, during the rotation of the disc, the scraper fixed on the outside of the filter cloth rubs against the surface of the filter cloth to scrape off the sludge on the surface of the filter cloth, and at the same time, the water in the disc is sucked from the inside out to clean For the sludge in the micropores of the filter cloth, a sludge discharge pipe is installed at the bottom of the tank. After setting the time, the sludge discharge pump is turned on to discharge the sludge.

滤布滤池有多种形式,包括转盘式、竖片式、钻石型,各中形式盘片竖直布置,由于盘片上滤布绒毛润水后变软,绒毛垂下,之中含有杂质不易被刮板和反抽吸泵清除,而且滤布盘片在转盘滤布运行一段时间后,滤布上的绒毛易板结、粘附,尤其在投加除磷絮凝剂后,絮体粘性大,反冲洗效果差。 There are many types of filter cloth filters, including rotary disc type, vertical plate type, and diamond type. The discs of each form are arranged vertically. Because the fluff of the filter cloth on the disc becomes soft after being moistened, the fluff hangs down, and the impurities contained in it are not easy to be absorbed. Scraper and back suction pump are removed, and after the filter cloth disc runs for a period of time on the turntable filter cloth, the fluff on the filter cloth is easy to harden and adhere, especially after adding phosphorus removal flocculant, the flocs are highly viscous and backwash poor effect.

根据浅池理论讲普通沉淀池改进成斜板沉淀池,提高了沉淀效率。利用平行管道分割成一系列浅层沉淀层,沉降的沉泥在各沉淀浅层中相互运动并分离。根据其相互运动方向分为逆(异)向流、同向流和侧向流三种不同分离方式。每两块平行斜板间相当于一个很浅的沉淀池。 According to the shallow pool theory, the ordinary sedimentation tank is improved into an inclined plate sedimentation tank, which improves the sedimentation efficiency. It is divided into a series of shallow sedimentation layers by using parallel pipelines, and the settled sediment moves and separates in each shallow sedimentation layer. According to their mutual movement direction, it can be divided into three different separation methods: reverse (different) flow, co-current flow and lateral flow. Between every two parallel inclined plates is equivalent to a very shallow sedimentation tank.

本实用新型结合滤布滤池和斜板沉淀池的各自优点,进行改进设计,解决了滤布滤池反冲洗效果差问题,增强出水效果,延长滤布使用寿命。 The utility model combines the respective advantages of the filter cloth filter and the inclined plate sedimentation tank to improve the design, solve the problem of poor backwashing effect of the filter cloth filter, enhance the water outlet effect, and prolong the service life of the filter cloth.

发明内容 Contents of the invention

本实用新型目的是提供一种斜板滤布过滤装置及控制技术,用以解决滤布滤池反冲洗效果差问题,增强出水效果,提高出水水质,延长滤布使用寿命。 The purpose of the utility model is to provide a slanted plate filter cloth filter device and control technology, which is used to solve the problem of poor backwashing effect of the filter cloth filter, enhance the water outlet effect, improve the water quality of the outlet water, and prolong the service life of the filter cloth.

本实用新型的技术方案,一种斜板滤布过滤装置,包括池体、斜板滤布盘片、集水管、投药混合系统、清洗系统、排泥系统。进水管、安装在池体底部一侧, 出水管安装在池体的另一侧,排泥管布置在池底,进水管进口处设置有加药口,进水管与管式混合器相连接,管式混合器上布置分水口,斜板滤布盘片固定于池体中央,吸泥管靴由吸泥泵连接并紧贴滤布布置, 集水管与斜板滤布盘片连接,集水横管与集水管相连接,集水管与集水渠相通,池体上方桁架上安有行车。 The technical solution of the utility model is a slanted plate filter cloth filter device, which includes a pool body, a slanted plate filter cloth disk, a water collection pipe, a drug feeding and mixing system, a cleaning system, and a mud discharge system. The water inlet pipe is installed on one side of the bottom of the pool body, the water outlet pipe is installed on the other side of the pool body, the mud discharge pipe is arranged at the bottom of the pool, the entrance of the water inlet pipe is provided with a dosing port, and the water inlet pipe is connected to the tube mixer. The water diversion port is arranged on the tubular mixer, the sloping plate filter cloth disc is fixed in the center of the tank body, the suction pipe shoe is connected by the dredge pump and arranged close to the filter cloth, the water collecting pipe is connected with the slanting plate filter cloth disc, and the water collecting The horizontal pipe is connected with the water collecting pipe, the water collecting pipe is connected with the water collecting canal, and the truss above the pool body is equipped with a driving vehicle.

池体:可根据条件和要求设计成不锈钢或钢混结构,过滤过程的主体结构。 Pool body: It can be designed as a stainless steel or steel-concrete structure according to conditions and requirements, and is the main structure of the filtration process.

斜板滤布盘片:此部分为本实用新型的核心单元,主要由不锈钢盘片支架、弧形斜板、滤布、集水口组成,斜板滤布盘片45~60°安装,弧形斜板面朝上,滤布面朝下,板长1~1.2m,水平间距3~5mm;由于平板的沉淀易容留沉泥且难以清洗,一旦平面斜板弯曲变形,滑泥通道更趋狭窄不畅,出现斜板严重积泥和出水水质恶化状况,因此本实用新型设置弧形斜板。 Inclined plate filter cloth disc: This part is the core unit of the utility model, mainly composed of stainless steel disc support, arc-shaped inclined plate, filter cloth, and water collection port. The inclined plate filter cloth disc is installed at 45~60°, and the arc-shaped The sloping plate faces upwards, the filter cloth faces downwards, the length of the slab is 1~1.2m, and the horizontal distance is 3~5mm; due to the sedimentation of the flat plate, it is easy to retain sediment and it is difficult to clean, once the flat inclined plate is bent and deformed, the mud passage will become narrow If it is not smooth, there will be serious mud accumulation on the sloping plate and deterioration of effluent quality. Therefore, the utility model is equipped with an arc-shaped sloping plate.

集水管:经过滤的水由中心集水管收集,再由出水堰排出。 Water collection pipe: The filtered water is collected by the central water collection pipe, and then discharged from the outlet weir.

投药混合系统:根据处理要求设计投药和药剂混合系统,在原水进水前端,设置投药口,可选择投加絮凝剂、除磷剂、除重金属等药剂,在进入池体后采用花瓣式管式混合器,药剂与水充分接触,分多点进水口进入池体中。 Dosing mixing system: According to the treatment requirements, the dosing and chemical mixing system is designed. A dosing port is set at the front end of the raw water inlet. You can choose to add flocculants, phosphorus removal agents, heavy metals and other chemicals. After entering the pool, the petal-type tubular In the mixer, the medicament is in full contact with the water, and enters the pool body through multiple water inlets.

排泥系统:排泥系统分为两部分,与盘片接触的反冲系统排除滤布中集结的杂质,池底部布置两个排泥管,主要收集有斜板沉淀集下的污泥。 Sludge discharge system: The sludge discharge system is divided into two parts. The recoil system in contact with the disc removes the impurities accumulated in the filter cloth. Two sludge discharge pipes are arranged at the bottom of the pool to mainly collect the sludge under the inclined plate sedimentation set.

清洗系统:反洗抽吸靴,管道、桁架,驱动机,用于滤布日常排渣反洗。 Cleaning system: backwashing suction boots, pipes, trusses, driving machine, used for daily slag discharge and backwashing of filter cloth.

本实用新型运行方式采取异、侧向流过滤沉淀同步方式运行,运行分为药剂混合、过滤、沉淀排泥、反洗过程: The operation mode of the utility model adopts the synchronous operation mode of different and lateral flow filtration and sedimentation, and the operation is divided into the process of medicament mixing, filtration, sedimentation and mud discharge, and backwashing:

药剂混合——原水经投药后由进水管管式混合器混合后,有设置的多点进水口同时进入反应池; Medicament mixing——After the raw water is mixed by the water inlet pipe mixer after being dosed, the multi-point water inlets are set to enter the reaction pool at the same time;

过滤——水流由池体一侧下方进入,由另一侧上方排出,相对于整个盘片而言是由下至上、由一边至另一边流动,沉降颗粒在重力作用下,沿着斜板下降,而澄清液是沿着斜板的地面上升,两个流体逆向流动,进入池体的原水,在压力作用下,从设置在盘片下面的滤布进入盘片内,悬浮杂质颗粒被截留在滤布表面,实现与水分离,随着过滤的进行,滤布表面的杂质聚集,滤布表面过水阻力再增加,进水水位升高,开启反洗系统; Filtration - the water flow enters from the bottom of one side of the pool body and is discharged from the top of the other side. Compared with the entire disc, it flows from bottom to top and from one side to the other side. The settled particles fall along the inclined plate under the action of gravity , while the clarified liquid rises along the ground of the inclined plate, the two fluids flow in reverse, and the raw water entering the pool body enters the disc from the filter cloth under the pressure under pressure, and the suspended impurity particles are trapped in the The surface of the filter cloth is separated from the water. As the filtration progresses, the impurities on the surface of the filter cloth accumulate, the resistance of the filter cloth surface to pass through the water increases again, the water level of the inlet water rises, and the backwash system is turned on;

沉淀排泥——截留在滤布表面的杂质颗粒在重力作用下,一部分坠落至相邻盘片上面的弧形斜板上,达到一定积累便会在重力作用下泥渣滑落至池底,由排泥管排出; Sedimentation and mud discharge - under the action of gravity, some of the impurity particles trapped on the surface of the filter cloth fall to the arc-shaped inclined plate on the adjacent disc, and when they reach a certain accumulation, the sludge will slide to the bottom of the pool under the action of gravity mud pipe discharge;

反洗——盘片固定不动,随着池上方桁架上行车的移动,反洗靴对盘片滤布进行刮洗,同时反冲洗靴具有抽吸泵,通过强大的吸力将滤布滤毛松散、展开,使其中隐藏在绒毛缝隙中的杂质颗粒吸出,这样滤布就被清洗干净。 Backwashing——The disc is fixed, and as the truck moves on the truss above the pool, the backwashing boots scrape and wash the disc filter cloth, and at the same time, the backwashing boots have a suction pump to filter the filter cloth through strong suction. Loosen and unfold, so that the impurity particles hidden in the gaps of the fluff are sucked out, so that the filter cloth is cleaned.

过滤滤速4~8m3/(m2·h),反洗强度0.2~0.4m3/ (m2·h),水头损失达到0.35m开始进行抽吸反冲洗。 The filtration rate is 4~8m 3 /(m 2 ·h), the backwash intensity is 0.2~0.4m 3 /(m 2 ·h), and the suction backwash starts when the water head loss reaches 0.35m.

本实用新型的有益技术效果: Beneficial technical effects of the utility model:

1、设备简单、紧凑,易于安装,占地面积小; 1. The equipment is simple, compact, easy to install, and occupies a small area;

2、反洗与过滤、沉淀同时进行,设备闲置率低; 2. Backwashing, filtration and precipitation are carried out at the same time, and the idle rate of equipment is low;

3、可以用于高悬浮物浓度原水净化,也可以除磷、重金属; 3. It can be used to purify raw water with high suspended solids concentration, and can also remove phosphorus and heavy metals;

4、反洗、排泥效果好,提高滤布再生效果,延长滤布使用寿命; 4. The effect of backwashing and mud discharge is good, which improves the regeneration effect of filter cloth and prolongs the service life of filter cloth;

5、过滤水头小,节省能耗。 5. The filter water head is small, saving energy consumption.

附图说明 Description of drawings

图1为本实用新型装置正面示意图。 Fig. 1 is the front schematic view of the utility model device.

图2为本实用新型装置平面示意图。 Fig. 2 is a schematic plan view of the device of the present invention.

图3为本实用新型装置侧面示意图。 Fig. 3 is a schematic side view of the device of the present invention.

图4为本实用新型斜板滤布盘片示意图。 Fig. 4 is a schematic diagram of the inclined plate filter cloth disc of the present invention.

图5为本实用新型斜板滤布盘片剖面示意图。 Fig. 5 is a schematic cross-sectional view of the inclined plate filter cloth disc of the present invention.

1池体、2斜板滤布盘片、3滤布、4集水管、5进水管、6出水管、7排泥管、8加药口、9管式混合器、10分水口、11行车、12吸泥管靴、 13吸泥泵、 14集水堰、 15集水横管、 16弧形斜板。 1 tank body, 2 inclined plate filter cloth disc, 3 filter cloth, 4 water collection pipe, 5 water inlet pipe, 6 water outlet pipe, 7 mud discharge pipe, 8 dosing port, 9 tube mixer, 10 water diversion port, 11 driving , 12 suction dredge pipe boots, 13 suction dredge pumps, 14 water collection weirs, 15 water collection horizontal pipes, 16 curved inclined plates.

具体实施方式 detailed description

一种斜板滤布过滤装置,进水管5由池体1底部一侧进入,在进水管5进口处设置加药口8,进水管5与管式混合器9相连接,管式混合器9上布置分水口10,斜板滤布盘片2固定于池体中央,吸泥管靴12由吸泥泵13连接并紧贴滤布3布置,反冲洗系统由行车11提供动力进行反洗, 集水管4与斜板滤布盘片2连接,集水横管15与集水管4相连接,由斜板滤布盘片2收集的过滤水经集水管4排出至集水渠14,在由出水管6排出池外。排泥管7布置在池底,定期排泥。 A slanted plate filter cloth filter device, the water inlet pipe 5 enters from the bottom side of the pool body 1, and a drug dosing port 8 is set at the inlet of the water inlet pipe 5, and the water inlet pipe 5 is connected with a tubular mixer 9, and the tubular mixer 9 The water diversion port 10 is arranged on the top, the slanted plate filter cloth disk 2 is fixed in the center of the pool body, the dredging pipe shoe 12 is connected by the dredging pump 13 and arranged close to the filter cloth 3, and the backwashing system is backwashed by the power provided by the crane 11. The water collection pipe 4 is connected to the inclined plate filter cloth disk 2, and the water collection horizontal pipe 15 is connected to the water collection pipe 4. The filtered water collected by the inclined plate filter cloth disk 2 is discharged to the water collection channel 14 through the water collection pipe 4, and is discharged from the outlet Water pipe 6 is discharged outside the pond. The mud discharge pipe 7 is arranged at the bottom of the pool for regular mud discharge.

本实用新型运行方式采取异、侧向流过滤沉淀同步方式运行,运行分为药剂混合、过滤、沉淀排泥、反洗过程。 The operation mode of the utility model adopts the synchronous mode of differential and lateral flow filtration and sedimentation, and the operation is divided into the processes of medicament mixing, filtration, sedimentation and mud discharge, and backwashing.

药剂混合——原水经投药口8投药后由进水管5管式混合器9混合后,由设置的多点分水口10同时进入反应池池体1。 Medicament mixing—the raw water enters the reaction pool body 1 through the multi-point water distribution port 10 after being dosed through the dosing port 8 and then mixed by the water inlet pipe 5 and the tubular mixer 9 .

过滤——水流由池体1一侧下方进入,由另一侧上方排出,沉降颗粒在重力作用下,沿着斜板下降,而澄清液是沿着斜板的板面上升,两个流体逆向流动,进入池体1的原水,在压力作用下,从设置在盘片2下面的滤布3进入盘片②内,过滤滤速4~8m3/(m2·h),悬浮杂质颗粒被截留在滤布3表面,实现与水分离,随着过滤的进行,滤布3表面的杂质聚集,滤布3表面过水阻力再增加,进水水位升高,水头损失达到0.35m开始进行抽吸反冲洗。 Filtration - The water flow enters from the bottom of one side of the pool body 1, and is discharged from the top of the other side. The settled particles descend along the inclined plate under the action of gravity, while the clarified liquid rises along the surface of the inclined plate, and the two fluids are reversed. The raw water flowing into the pool body 1 enters the disc ② from the filter cloth 3 arranged under the disc 2 under pressure, and the filtration rate is 4~8m 3 /(m 2 ·h), and the suspended impurity particles are Trapped on the surface of the filter cloth 3 to realize separation from water. As the filtration proceeds, impurities on the surface of the filter cloth 3 accumulate, and the resistance of the surface of the filter cloth 3 to pass through water increases again. Suction backwash.

沉淀排泥——截留在滤布3表面的杂质颗粒在重力作用下,一部分坠落至相邻盘片2上面的弧形斜板16上,达到一定积累便会在重力作用下泥渣滑落至池底,由排泥管7排出。 Sedimentation and mud discharge - under the action of gravity, some of the impurity particles trapped on the surface of the filter cloth 3 fall to the arc-shaped inclined plate 16 on the adjacent disc 2, and when a certain accumulation is reached, the sludge will slide to the pool under the action of gravity The bottom is discharged from the mud discharge pipe 7.

反洗——盘片2固定不动,随着池上方桁架上行车11的移动,反洗靴12对盘片滤布3进行刮洗,同时反冲洗靴具有抽吸泵13,反洗强度0.2~0.4m3/ (m2·h),通过强大的吸力将滤布3滤毛松散、展开,使其中隐藏在绒毛缝隙中的杂质颗粒吸出,这样滤布3就被清洗干净。 Backwash——The disc 2 is fixed, and with the movement of the crane 11 on the truss above the pool, the backwash boot 12 scrapes and washes the disc filter cloth 3. At the same time, the backwash boot has a suction pump 13, and the backwash intensity is 0.2 ~0.4m3/ (m2·h), loosen and unfold the filter hairs of the filter cloth 3 through strong suction, so that the impurity particles hidden in the gaps of the fluff are sucked out, so that the filter cloth 3 is cleaned.

Claims (4)

  1. null1. a swash plate filter-cloth filtering device,Including cell body、Swash plate filter cloth disc、Collector pipe、Dispensing hybrid system、Purging system、Sludge drainage system,It is characterized in that: water inlet pipe (5) is arranged on cell body (1) bottom side,Outlet pipe (6) is arranged on the opposite side of cell body (1),Discharge pipeline (7) is arranged at the bottom of pond,Water inlet pipe (5) import department is provided with dosing mouth (8),Water inlet pipe (5) is connected with tube mixer (9),Bleeder (10) is arranged on tube mixer (9),Swash plate filter cloth disc (2) is fixed on cell body (1) central authorities,Dredging tube boots (12) are connected by dredge pump (13) and are close to filter cloth (3) to be arranged,Collector pipe (4) is connected with swash plate filter cloth disc (2),The transverse tube (15) that catchments is connected with collector pipe (4),Collector pipe (4) communicates with braiding channel (14),Driving (11) it is equipped with in cell body (1) upper truss.
  2. A kind of swash plate filter-cloth filtering device the most according to claim 1, it is characterised in that: swash plate filter cloth disc is made up of stainless steel disc plate rack, swash plate, filter cloth, inlet, and wherein swash plate is arc swash plate.
  3. A kind of swash plate filter-cloth filtering device the most according to claim 1, it is characterised in that: swash plate filter cloth disc 45 ~ 60 ° installation, arc swash plate faces up, filter cloth surface down, plate length 1 ~ 1.2m, level interval 3 ~ 5mm.
  4. A kind of swash plate filter-cloth filtering device the most according to claim 1, it is characterised in that: described discharge pipeline (7) number is one, two or more.
CN201620298841.XU 2016-04-12 2016-04-12 A kind of swash plate filter-cloth filtering device and control method Expired - Fee Related CN205699790U (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105749619A (en) * 2016-04-12 2016-07-13 沈阳建筑大学 Inclined plate filter cloth filtering device and control method
CN106669279A (en) * 2017-02-09 2017-05-17 无锡玖和隆工程科技有限公司 Filtering equipment for realizing separation of catalyst in production of polytetramethylene ether glycol
CN111841146A (en) * 2020-08-20 2020-10-30 湖南有色黄沙坪矿业有限公司 Mineral sedimentation tank gate
CN112190982A (en) * 2020-07-20 2021-01-08 上海兴全电力技术有限公司 High-efficient non-maintaining swash plate subsides device

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105749619A (en) * 2016-04-12 2016-07-13 沈阳建筑大学 Inclined plate filter cloth filtering device and control method
CN105749619B (en) * 2016-04-12 2018-07-27 沈阳建筑大学 A kind of inclined plate filter-cloth filtering device and control method
CN106669279A (en) * 2017-02-09 2017-05-17 无锡玖和隆工程科技有限公司 Filtering equipment for realizing separation of catalyst in production of polytetramethylene ether glycol
CN106669279B (en) * 2017-02-09 2022-04-22 无锡玖和隆工程科技有限公司 Filtering equipment for realizing catalyst separation in polytetramethylene glycol production
CN112190982A (en) * 2020-07-20 2021-01-08 上海兴全电力技术有限公司 High-efficient non-maintaining swash plate subsides device
CN112190982B (en) * 2020-07-20 2022-03-22 上海兴全电力技术有限公司 High-efficient non-maintaining swash plate subsides device
CN111841146A (en) * 2020-08-20 2020-10-30 湖南有色黄沙坪矿业有限公司 Mineral sedimentation tank gate

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