CN210825900U - A filter-pressing system for sludge treatment - Google Patents
A filter-pressing system for sludge treatment Download PDFInfo
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- CN210825900U CN210825900U CN201921376403.0U CN201921376403U CN210825900U CN 210825900 U CN210825900 U CN 210825900U CN 201921376403 U CN201921376403 U CN 201921376403U CN 210825900 U CN210825900 U CN 210825900U
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- 239000010802 sludge Substances 0.000 title claims abstract description 72
- 230000003750 conditioning effect Effects 0.000 claims abstract description 38
- 239000003814 drug Substances 0.000 claims abstract description 15
- 238000003756 stirring Methods 0.000 claims description 40
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 35
- 238000001914 filtration Methods 0.000 claims description 12
- 239000010865 sewage Substances 0.000 claims description 7
- 230000005540 biological transmission Effects 0.000 claims description 6
- 239000004744 fabric Substances 0.000 claims description 6
- 239000007921 spray Substances 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 5
- 230000007423 decrease Effects 0.000 claims description 4
- 239000002002 slurry Substances 0.000 claims description 4
- 230000000694 effects Effects 0.000 abstract description 10
- 230000007613 environmental effect Effects 0.000 abstract description 2
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- 238000006297 dehydration reaction Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
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- 238000010276 construction Methods 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
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- 239000002351 wastewater Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
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Abstract
本实用新型公开了一种用于污泥处理的压滤系统,其特征在于,包括开泥装置、配药罐、调理罐以及板框压滤机,其中所述开泥装置通过输送管与所述调理罐连接,所述配药罐通过输送管与所述调理罐连接,所述调理罐通过输送管与所述板框压滤机连接。本实用新型运行稳定性强,环保节能,有效改善污泥机械压滤的脱水效果,提高生产率。
The utility model discloses a filter press system for sludge treatment, which is characterized in that it comprises a sludge opening device, a medicine dispensing tank, a conditioning tank and a plate and frame filter press, wherein the sludge opening device communicates with the sludge opening device through a conveying pipe. A conditioning tank is connected, the dispensing tank is connected with the conditioning tank through a conveying pipe, and the conditioning tank is connected with the plate and frame filter press through a conveying pipe. The utility model has the advantages of strong running stability, environmental protection and energy saving, effectively improving the dewatering effect of the mechanical pressure filtration of sludge, and increasing the productivity.
Description
技术领域technical field
本实用新型涉及污泥处理技术领域,具体是涉及一种用于污泥处理的压滤系统。The utility model relates to the technical field of sludge treatment, in particular to a filter press system for sludge treatment.
背景技术Background technique
随着造纸产业的发展和污染防治设施的建设,造纸废水经治理设施处理后产生的污泥成为新的污染源,而且该污染源随着造纸行业生产规模的扩大而不断增多。废纸造纸企业的污泥主要来源有两个:一是废纸造纸过程中的筛选净化等工段产生的污泥,该污泥主要为非纤维杂质,成分复杂,主要包括有机物和无机物;二是造纸废水处理过程中产生的生物污泥,主要成分是细小纤维、木质素、氮、磷、钾等物质。目前主要有两种处理方法,第一种是直接填埋,直接填埋不仅需要填埋场地,而且污染环境;第二种是将污泥进行脱水,与煤进行混合,然后送入锅炉燃烧,现有技术中常采用压滤机直接对污泥进行脱水,其中板框压滤机为化工常用设备,过滤推动力大,泥饼含水率较低,进泥、出泥是间歇的,生产率较低。因此有必要加大污泥处理设施建设力度,选择科学合理的污泥脱水方法和处理工艺,提高处理效率。With the development of the papermaking industry and the construction of pollution prevention and control facilities, the sludge produced by the treatment of papermaking wastewater has become a new source of pollution, and this source of pollution has been increasing with the expansion of the production scale of the papermaking industry. There are two main sources of sludge in waste paper and papermaking enterprises: one is the sludge produced in the process of screening and purification of waste paper and papermaking. The sludge is mainly non-fibrous impurities with complex components, mainly including organic and inorganic substances; It is a biological sludge produced in the process of papermaking wastewater treatment. The main components are fine fibers, lignin, nitrogen, phosphorus, potassium and other substances. At present, there are two main treatment methods. The first is direct landfill, which not only requires landfill, but also pollutes the environment; the second is to dehydrate the sludge, mix it with coal, and then send it to the boiler for combustion. In the prior art, a filter press is often used to directly dehydrate the sludge. Among them, the plate and frame filter press is a common equipment in chemical industry. . Therefore, it is necessary to increase the construction of sludge treatment facilities, select scientific and reasonable sludge dewatering methods and treatment processes, and improve treatment efficiency.
发明内容SUMMARY OF THE INVENTION
本实用新型的目的就是为了解决现有技术之不足而提供的一种运行稳定性强,环保节能,有效改善污泥机械压滤的脱水效果,提高生产率的用于污泥处理的压滤系统。The purpose of the utility model is to provide a filter press system for sludge treatment which has strong running stability, environmental protection and energy saving, effectively improves the dewatering effect of sludge mechanical filter press, and improves productivity in order to solve the deficiencies of the prior art.
本实用新型是采用如下技术解决方案来实现上述目的:The utility model adopts the following technical solutions to achieve the above purpose:
一种用于污泥处理的压滤系统,其特征在于,包括开泥装置、配药罐、调理罐以及板框压滤机,其中所述开泥装置通过输送管与所述调理罐连接,所述配药罐通过输送管与所述调理罐连接,所述调理罐通过输送管与所述板框压滤机连接;A filter press system for sludge treatment, characterized in that it includes a sludge opening device, a dispensing tank, a conditioning tank and a plate and frame filter press, wherein the sludge opening device is connected to the conditioning tank through a conveying pipe, so that the The dispensing tank is connected with the conditioning tank through a conveying pipe, and the conditioning tank is connected with the plate and frame filter press through a conveying pipe;
所述开泥装置包括倾斜设置的下料池,与所述下料池输出端连接的、互为并联关系的若干开泥池,其中所述下料池输出端设置有格栅,所述开泥池上部设置有进水管,内部设置有搅拌装置;The mud opening device includes a sloping feeding tank, and several mud opening ponds connected to the output end of the feeding pond and in a parallel relationship with each other, wherein the output end of the feeding pond is provided with a grille, and the opening A water inlet pipe is arranged on the upper part of the mud pool, and a stirring device is arranged inside;
所述配药罐包括配药罐主体,所述配药罐主体上部设置有进水管,内部沿竖直方向设置有搅拌装置;The medicine dispensing tank includes a medicine dispensing tank main body, the upper part of the medicine dispensing tank main body is provided with a water inlet pipe, and the interior is provided with a stirring device along the vertical direction;
所述调理罐内部设置有搅拌装置;A stirring device is arranged inside the conditioning tank;
所述板框压滤机输出端连接有排水管,所述排水管设置有分支管路,主管路为回流段与所述开泥池连接,用于原泥稀释,分管路为直排段与外界污水处理系统连接。The output end of the plate and frame filter press is connected with a drain pipe, and the drain pipe is provided with a branch pipeline. External sewage treatment system connection.
作为上述方案的进一步说明,所述格栅包括依次设置的粗格栅、中格栅、细格栅,其中所述粗格栅、中格栅、细格栅之间的栅条间隔依次减小,污泥依次通过粗格栅、中格栅、细格栅实现多级过滤。As a further description of the above solution, the grid includes a coarse grid, a medium grid, and a fine grid arranged in sequence, wherein the grid interval between the coarse grid, the middle grid, and the thin grid decreases in sequence. , the sludge passes through the coarse grid, the medium grid and the fine grid in turn to achieve multi-stage filtration.
进一步地,所述下料池的倾斜角度为30°-60°。Further, the inclination angle of the feeding tank is 30°-60°.
进一步地,所述搅拌装置包括驱动电机、搅拌轴和多层搅拌器,所述多层搅拌器沿所述搅拌轴轴向分布且分别固定于所述搅拌轴上。Further, the stirring device includes a driving motor, a stirring shaft and a multi-layer stirrer, and the multi-layer stirrers are axially distributed along the stirring shaft and are respectively fixed on the stirring shaft.
进一步地,优选所述多层搅拌器的层数为3层,包括上层搅拌器、中层搅拌器和下层搅拌器。Further, it is preferred that the number of layers of the multi-layer agitator is 3 layers, including an upper-layer agitator, a middle-layer agitator and a lower-layer agitator.
进一步地,所述多层搅拌器为浆状件,各浆状件相对于水平面的倾斜角度为30°-60°。Further, the multi-layer agitator is a slurry-like piece, and the inclination angle of each slurry-like piece with respect to the horizontal plane is 30°-60°.
进一步地,所述上层搅拌器、中层搅拌器和下层搅拌器距离所述搅拌轴的半径长度不相等,中层搅拌器半径长、上下层搅拌器半径短,呈两头窄中间宽的纺锤形结构,或上中下层搅拌器半径依次递增/递减,呈梯形结构。Further, the radius lengths of the upper-layer agitator, the middle-layer agitator and the lower-layer agitator are unequal from the stirring shaft, the middle-layer agitator has a long radius, and the upper and lower layer agitators have a short radius, which is a spindle-shaped structure with narrow ends and wide middle, Or the radius of the upper, middle and lower agitators increases/decreases in turn, forming a trapezoidal structure.
进一步地,所述板框压滤机包括机架,机架上设有水平方向设置的主梁,主梁上滑动连接有若干块压滤板,压滤板之间连接有滤布,主梁的两端分别设有左挡板、右挡板,所述左挡板上设置有一能够移动靠近并挤压所述压滤板紧贴在一起的液压传动系统,所述右挡板上设置有一清洗压滤板及滤布的喷淋装置,所述喷淋装置包括接入自来水的软管、连接于软管输出端的喷嘴。Further, the plate-and-frame filter press includes a frame on which a main beam arranged in a horizontal direction is arranged, a number of filter press plates are slidably connected on the main beam, filter cloths are connected between the filter press plates, and the main beam is The two ends of the filter are respectively provided with a left baffle and a right baffle, the left baffle is provided with a hydraulic transmission system that can move close to and squeeze the filter press plates to be close together, and the right baffle is provided with a hydraulic transmission system. A spray device for cleaning filter press plates and filter cloths. The spray device includes a hose connected to tap water and a nozzle connected to the output end of the hose.
进一步地,所述输送管与开泥装置、配药罐、调理罐的连接处分别设置有流量控制阀。Further, a flow control valve is respectively provided at the connection between the conveying pipe and the mud opening device, the dispensing tank and the conditioning tank.
进一步地,所述排水管中设置有液压泵组件,为水的流动提供动力,排水管分支处设置有控制阀,控制水流进入回流段或直排段。Further, a hydraulic pump assembly is arranged in the drainage pipe to provide power for the flow of water, and a control valve is arranged at the branch of the drainage pipe to control the water flow into the return section or the straight discharge section.
进一步地,所述流量控制阀、控制阀、液压泵组件均与PLC控制器电性连接,实现系统自动化控制。Further, the flow control valve, the control valve and the hydraulic pump components are all electrically connected with the PLC controller to realize the automatic control of the system.
本实用新型采用上述技术解决方案所能达到的有益效果是:The beneficial effects that the utility model can achieve by adopting the above-mentioned technical solutions are:
1、本实用新型通过在开泥装置的下料池倾斜设置可以减缓污泥下落至开泥池的速度,防止污泥在开泥池中堆积影响搅拌效果,同时下料池中设置多级格栅,能够根据杂质的体积大小,有效筛选污泥中夹杂的树枝、石头等固体垃圾,起到多级过滤作用,防止大块杂质堵塞格栅的同时,方便工作人员对杂质进行分类清理;搅拌装置配合进水管中的流量控制阀,根据每次处理的污泥质量控制进水量,多层搅拌器对污泥进行充分搅拌稀释,有利于提高后续污泥化学调理的效果。1. The utility model can slow down the speed of sludge falling to the sludge opening tank by slanting the lowering tank of the sludge opening device, preventing the sludge from accumulating in the sludge opening tank and affecting the stirring effect. The grid can effectively screen the solid waste such as branches and stones mixed in the sludge according to the volume of the impurities, and play a multi-stage filtration function to prevent large impurities from clogging the grid, and at the same time, it is convenient for the staff to classify and clean the impurities; stirring The device cooperates with the flow control valve in the water inlet pipe to control the water inlet amount according to the quality of the sludge treated each time, and the multi-layer agitator fully stirs and dilutes the sludge, which is beneficial to improve the effect of subsequent chemical conditioning of the sludge.
2、本实用通过设置配药罐,配合进水管中设置的流量控制阀,根据每次下料的药剂质量控制进水量,配合搅拌装置对药剂进行混合、搅拌,保证药剂达到化学调理的最佳浓度条件,能够定量定性进行配药,既能防止人工投料出现用量误差,有效提高药剂投放精度,又能避免药剂出现结块或分布不均匀。2. The utility model can control the water intake according to the quality of the medicine each time by setting the medicine dispensing tank, cooperate with the flow control valve set in the water inlet pipe, and cooperate with the stirring device to mix and stir the medicine, so as to ensure that the medicine reaches the optimal concentration of chemical conditioning. It can quantitatively and qualitatively dispense medicines under certain conditions, which can not only prevent dosage errors in manual feeding, effectively improve the accuracy of drug delivery, but also avoid agglomeration or uneven distribution of drugs.
3、调理罐接收开泥装置的泥水以及配药罐中的药剂,内部的搅拌装置对罐体里面的泥水和药剂进行充分搅拌,使得污泥颗粒絮凝、结构增强,有效改善板框压滤机的脱水效果。3. The conditioning tank receives the muddy water from the mud opening device and the medicine in the dispensing tank. The internal stirring device fully stirs the muddy water and the medicine in the tank, so that the sludge particles are flocculated and the structure is strengthened, which effectively improves the performance of the plate and frame filter press. Dehydration effect.
4、板框压滤机产生的污泥压滤水(含滤布清洗水)通过排水管的分支管路,一部分通过回流段回流至开泥池用于原泥稀释,剩下的部分污水通过直排段输送到外界的污水处理系统处理,不仅节约水资源,达到废水重复利用的目的,而且污水得到科学有效的处理,对环境友好。4. The sludge press filtration water (including filter cloth cleaning water) produced by the plate and frame filter press passes through the branch pipeline of the drain pipe, and part of it is returned to the mud opening tank through the return section for dilution of raw mud, and the remaining part of the sewage passes through The straight discharge section is transported to the external sewage treatment system for treatment, which not only saves water resources and achieves the purpose of reuse of wastewater, but also scientifically and effectively treats sewage, which is environmentally friendly.
附图说明Description of drawings
图1为本实用新型的原理示意图。Fig. 1 is the principle schematic diagram of the utility model.
图2为开泥装置的原理示意图。Figure 2 is a schematic diagram of the principle of the mud opening device.
图3为开泥装置的俯视图。Figure 3 is a top view of the mud breaking device.
图4为配药罐的结构示意图。Figure 4 is a schematic diagram of the structure of the dispensing tank.
图5为调理罐的结构示意图。Figure 5 is a schematic structural diagram of a conditioning tank.
图6为板框压滤机的结构示意图。Figure 6 is a schematic structural diagram of a plate and frame filter press.
附图标记说明:1、开泥装置,1-1、下料池,1-2、开泥池,1-3、格栅,2、配药罐,3、调理罐,4、板框压滤机,4-1、机架,4-2、主梁,4-3、压滤板,4-4、左挡板,4-5、右挡板,4-6、液压传动系统,4-7、喷淋装置,5、输送管,6、进水管,7、搅拌装置,7-1、驱动电机,7-2、搅拌轴,7-3、多层搅拌器,8、排水管,8-1、回流段,8-2、直排段。Explanation of reference numerals: 1, mud opening device, 1-1, feeding tank, 1-2, mud opening tank, 1-3, grille, 2, dispensing tank, 3, conditioning tank, 4, plate and frame filter press Machine, 4-1, frame, 4-2, main beam, 4-3, filter plate, 4-4, left baffle, 4-5, right baffle, 4-6, hydraulic transmission system, 4- 7. Spraying device, 5. Conveying pipe, 6. Water inlet pipe, 7. Stirring device, 7-1, Drive motor, 7-2, Stirring shaft, 7-3, Multilayer agitator, 8. Drain pipe, 8 -1, return section, 8-2, straight row section.
具体实施方式Detailed ways
以下结合具体实施例对本技术方案作详细的描述。The technical solution will be described in detail below with reference to specific embodiments.
如图1-图2所示,本实用新型是一种用于污泥处理的压滤系统,其特征在于,包括开泥装置1、配药罐2、调理罐3以及板框压滤机4,其中所述开泥装置1通过输送管5与所述调理罐3连接,所述配药罐2通过输送管5与所述调理罐3连接,所述调理罐3通过输送管5与所述板框压滤机4连接;所述开泥装置1包括倾斜设置的下料池1-1,与所述下料池输出端连接的、互为并联关系的若干开泥池1-2,其中所述下料池输出端设置有格栅1-3,所述开泥池上部设置有进水管6,内部设置有搅拌装置7;所述配药罐2包括配药罐主体,所述配药罐主体上部设置有进水管6,内部沿竖直方向设置有搅拌装置7;所述调理罐3内部设置有搅拌装置7;所述板框压滤机4输出端连接有排水管8,所述排水管8设置有分支管路,主管路为回流段8-1与所述开泥池连接,用于原泥稀释,分管路为直排段8-2与外界污水处理系统连接。As shown in Figures 1 to 2, the present utility model is a filter press system for sludge treatment, which is characterized in that it comprises a
如图3-图5所示,所述下料池1-1的倾斜角度为30°-60°,下料池输出端设置的格栅1-3包括依次设置的粗格栅、中格栅、细格栅,其中所述粗格栅、中格栅、细格栅之间的栅条间隔依次减小,污泥依次通过粗格栅、中格栅、细格栅实现多级过滤;系统中的搅拌装置7均包括驱动电机7-1、搅拌轴7-2和多层搅拌器7-3,所述多层搅拌器沿所述搅拌轴轴向分布且分别固定于所述搅拌轴上,优选所述多层搅拌器的层数为3层,包括上层搅拌器、中层搅拌器和下层搅拌器,所述多层搅拌器为浆状件,各浆状件相对于水平面的倾斜角度为30°-60°,各层搅拌器距离所述搅拌轴的半径长度不相等,可以采用两头窄中间宽的纺锤形结构或梯形结构;As shown in Figures 3-5, the inclination angle of the feeding pool 1-1 is 30°-60°, and the grids 1-3 set at the output end of the feeding pool include coarse grids and middle grids arranged in sequence. , fine grid, wherein the grid interval between the coarse grid, the medium grid and the fine grid is reduced in turn, and the sludge is sequentially filtered through the coarse grid, the medium grid and the fine grid to achieve multi-stage filtration; the system The stirring devices 7 in each include a drive motor 7-1, a stirring shaft 7-2 and a multi-layer stirrer 7-3, which are distributed axially along the stirring shaft and are respectively fixed on the stirring shaft , preferably the number of layers of the multi-layer agitator is 3 layers, including the upper layer agitator, the middle layer agitator and the lower layer agitator, the multi-layer agitator is a slurry part, and the inclination angle of each slurry part relative to the horizontal plane is 30°-60°, the radius of each layer of stirrer from the stirring shaft is not equal, and a spindle-shaped structure or a trapezoidal structure with narrow width at both ends and wide in the middle can be used;
如图6所示,所述板框压滤机4包括机架4-1,机架上设有水平方向设置的主梁4-2,主梁上滑动连接有若干块压滤板4-3,压滤板之间连接有滤布,主梁的两端分别设有左挡板4-4、右挡板4-5,所述左挡板4-4上设置有一能够移动靠近并挤压所述压滤板紧贴在一起的液压传动系统4-6,所述右挡板4-5上设置有一清洗压滤板及滤布的喷淋装置4-7,所述喷淋装置包括接入自来水的软管、连接于软管输出端的喷嘴;所述输送管与开泥装置、配药罐、调理罐的连接处分别设置有流量控制阀,所述排水管中设置有液压泵组件,为水的流动提供动力,排水管分支处设置有控制阀,控制水流进入回流段或直排段。As shown in FIG. 6 , the plate and frame filter press 4 includes a frame 4-1, the frame is provided with a main beam 4-2 arranged in a horizontal direction, and a number of filter press plates 4-3 are slidably connected to the main beam. , a filter cloth is connected between the filter press plates, and the two ends of the main beam are respectively provided with a left baffle 4-4 and a right baffle 4-5. The hydraulic transmission system 4-6 in which the filter press plates are closely attached together, the right baffle plate 4-5 is provided with a spray device 4-7 for cleaning the filter press plate and the filter cloth. A hose for entering tap water and a nozzle connected to the output end of the hose; a flow control valve is respectively provided at the connection between the conveying pipe and the mud opening device, the dispensing tank and the conditioning tank, and a hydraulic pump assembly is provided in the drain pipe for The flow of water provides power, and a control valve is arranged at the branch of the drain pipe to control the water flow into the return section or the straight discharge section.
实施例一Example 1
以图1配置为例,本实用新型中采用2组开泥池、2组配药罐、3组调理罐、2台板框压滤机,每个工作周期板框压滤时间为1.5~2h,每天可以工作二十四板,每板处理含水率80%泥量为3.5t,即含水率80%的污泥日处理能力为160吨/日。Taking the configuration of FIG. 1 as an example, the utility model adopts 2 groups of mud-opening tanks, 2 groups of dispensing tanks, 3 groups of conditioning tanks, and 2 plate and frame filter presses, and the plate and frame filter press time of each working cycle is 1.5~2h, Twenty-four boards can be worked every day, and each board can handle 3.5t of sludge with a moisture content of 80%, that is, the daily processing capacity of sludge with a moisture content of 80% is 160 tons/day.
实际应用时,待处理的污泥含水率为80%(原泥)以上,需要先置入开泥装置的下料池,由于下料池输出端设置有多级格栅,若下料池倾斜角度过大则污泥下落过快,影响格栅过滤效果,角度过小则污泥下落太慢,影响格栅过滤效率,因此倾斜角度设置为30°-60°,既保证过滤速率又保证过滤质量;污泥依次经过粗格栅、中格栅、细格栅,其中杂质按照体积大小被过滤,有效避免树枝、石头等固体垃圾进入到开泥池、调理罐中造成相关设备损坏;多级过滤后的污泥落入并联设置的2组开泥池中,若待处理的原泥量较大,可以并联接入多个开泥池组,进水管开始向开泥池中加水,用户输入原泥质量,通过PLC控制器(如施耐德电气生产的Modicon M340可编程控制器)运算得到稀释至一定含水率所需的进水量,控制流量控制阀的进水量,配合搅拌装置,将污泥稀释至含水率为98%以上,达到进行化学调理的最佳条件,由于搅拌装置包括多层搅拌器,搅拌器均呈一定角度且距离所述搅拌轴的半径长度不相等,在转动过程中增加流体系统的不稳定性,形成湍流强化传递和反应过程,有效提高原泥的搅拌、混合效果。In practical application, the moisture content of the sludge to be treated is more than 80% (raw mud), and it needs to be placed in the unloading tank of the sludge opening device. If the angle is too large, the sludge will fall too fast, which will affect the filtering effect of the grid. If the angle is too small, the sludge will fall too slowly, which will affect the filtering efficiency of the grid. Therefore, the inclination angle is set to 30°-60°, which not only ensures the filtration rate but also ensures the filtration efficiency. Quality; the sludge passes through the coarse grid, the medium grid and the fine grid in sequence, and the impurities are filtered according to the size, which effectively prevents the solid waste such as branches and stones from entering the mud opening pool and conditioning tank and causing damage to related equipment; multi-level The filtered sludge falls into the two sets of mud-opening tanks set up in parallel. If the amount of raw mud to be treated is large, multiple mud-opening tank groups can be connected in parallel, and the water inlet pipe starts to add water to the mud-opening tanks. The quality of the raw mud is calculated by the PLC controller (such as the Modicon M340 programmable controller produced by Schneider Electric) to obtain the water intake required for dilution to a certain moisture content, control the water intake of the flow control valve, and cooperate with the stirring device to dilute the sludge. When the water content is above 98%, the best conditions for chemical conditioning are reached. Since the stirring device includes a multi-layer stirrer, the stirrer is at a certain angle and the radius from the stirring shaft is not equal in length. During the rotation process, the fluid increases The instability of the system forms a turbulent flow to strengthen the transfer and reaction process, effectively improving the stirring and mixing effect of the raw mud.
开泥后的污泥经输送管送至调理罐中进行化学调理,以天然硅藻土和聚丙烯酰胺作为化学添加剂为例,由于这两种化学药剂的最佳作用浓度不同,因此需要两组配药罐对单一化学添加剂进行搅拌混合,进水管中的流量控制阀根据添加的化学药剂的质量及目标浓度,分别控制两组配药罐的进水量,搅拌装置的工作过程同上所述,不作赘述。经过配药罐处理后,配置成浓度为70PPM的天然硅藻土及50PPM的聚丙烯酰胺,经输送管送至调理罐中进行污泥化学处理。The sludge after opening the mud is sent to the conditioning tank through the conveying pipe for chemical conditioning. Taking natural diatomite and polyacrylamide as chemical additives as an example, because the optimal concentration of these two chemicals is different, two groups of chemical agents are required. The dispensing tank stirs and mixes a single chemical additive, and the flow control valve in the water inlet pipe controls the water intake of the two groups of dispensing tanks respectively according to the quality and target concentration of the added chemical agent. The working process of the stirring device is the same as the above. After being treated in the dispensing tank, it is configured into natural diatomite with a concentration of 70PPM and polyacrylamide with a concentration of 50PPM, and sent to the conditioning tank through a conveying pipe for chemical sludge treatment.
调理罐中达到各自最佳调理条件的污泥及药剂相接触,搅拌装置促使污泥颗粒絮凝、结构增强,搅拌一段时间后经输送管送至板框压滤机,有利于改善污泥机械压滤的脱水效果。In the conditioning tank, the sludge and the chemicals that have reached their respective optimal conditioning conditions are in contact, and the stirring device promotes the flocculation of the sludge particles and the enhancement of the structure. Dehydration effect of filtration.
污泥进入到板框压滤机后,用户启动液压传动系统对压滤板进行挤压,机械挤压后的压滤水流入排水管中,完成压滤工作周期后,用户可以通过喷淋装置对压滤板和滤布进行喷淋清洗,保证下一工作周期开始时压滤机中没有污泥残留。由于排水管设置分支管路,PLC控制器(如施耐德电气生产的Modicon M340可编程控制器)通过控制阀,控制水流进入回流段或直排段,排水管中的液压泵组件为压滤水的流动提供动力,产生的污泥压滤水(含滤布清洗水)一部分回流用于原泥稀释,剩下的通过管道输送到一体化污水处理系统处理;压滤完毕后,开动压滤机输送带,开板,抽检泥样,确保泥样含水率在60%左右后,每天160吨80%水份污泥压滤后转化为80吨60%水份污泥。After the sludge enters the plate and frame filter press, the user starts the hydraulic transmission system to squeeze the filter plate, and the pressure filter water after mechanical extrusion flows into the drainage pipe. After the filter press work cycle is completed, the user can pass the spray device. Spray and clean the filter press plate and filter cloth to ensure that there is no sludge residue in the filter press at the beginning of the next working cycle. Since the drain pipe is set with branch pipes, the PLC controller (such as the Modicon M340 programmable controller produced by Schneider Electric) controls the water flow into the return section or the straight discharge section through the control valve. The flow provides power, and a part of the produced sludge press filtration water (including filter cloth cleaning water) is returned for the dilution of the raw mud, and the rest is transported to the integrated sewage treatment system through the pipeline for treatment; after the filtration is completed, the filter press is started to transport Take, open the board, and randomly check the mud sample to ensure that the moisture content of the mud sample is about 60%, and 160 tons of 80% water sludge per day will be converted into 80 tons of 60% water sludge after pressure filtration.
实施例二Embodiment 2
本实施例提供的一种用于污泥处理的压滤系统,其结构与实施例一基本一致,区别在于,所述开泥池、配药罐、调理罐以及板框压滤机的实际数量根据生产规模进行调整。本实施例具有实施例一的所有技术效果,这里不再赘述。The structure of a filter press system for sludge treatment provided in this embodiment is basically the same as that of the first embodiment, the difference is that the actual number of the mud opening tank, the dispensing tank, the conditioning tank and the plate and frame filter press is based on The scale of production is adjusted. This embodiment has all the technical effects of the first embodiment, which will not be repeated here.
本实用新型与现有技术相比,在进行板框压滤机脱水前通过对污泥以及药剂进行预处理,达到各自最佳调理条件再进行化学调理,使污泥颗粒絮凝、结构增强,以改善污泥机械压滤的脱水效果,同时排水管设置分支管路,实现部分压滤水的回流重复利用,大大节约水资源,对环境友好。Compared with the prior art, the utility model pre-processes the sludge and the chemicals before the dehydration of the plate and frame filter press to achieve the respective optimal conditioning conditions and then carries out chemical conditioning, so as to flocculate the sludge particles and strengthen the structure, so as to improve the performance of the sludge particles. The dewatering effect of the sludge mechanical filter press is improved. At the same time, the drainage pipe is equipped with a branch pipeline to realize the return and reuse of part of the filter press water, which greatly saves water resources and is environmentally friendly.
以上所述的仅是本实用新型的优选实施方式,应当指出,对于本领域的普通技术人员来说,在不脱离本实用新型创造构思的前提下,还可以做出若干变形和改进,这些都属于本实用新型的保护范围。The above are only the preferred embodiments of the present utility model. It should be pointed out that for those of ordinary skill in the art, without departing from the inventive concept of the present utility model, several modifications and improvements can be made. It belongs to the protection scope of the present invention.
Claims (10)
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| CN116272025B (en) * | 2023-03-16 | 2026-03-20 | 广东高瓷科技股份有限公司 | A highly efficient fully automatic slurry preparation, filter press, and washing system |
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Denomination of utility model: A pressure filtration system for sludge treatment Granted publication date: 20200623 Pledgee: Jiangmen Rural Commercial Bank Co.,Ltd. Xinhui Technology Branch Pledgor: Jiangmen Huajie solid waste treatment Co.,Ltd. Registration number: Y2024980043549 |
