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CN210085228U - A mobile sludge plate and frame filter press dehydration and cleaning integrated device - Google Patents

A mobile sludge plate and frame filter press dehydration and cleaning integrated device Download PDF

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CN210085228U
CN210085228U CN201920265603.2U CN201920265603U CN210085228U CN 210085228 U CN210085228 U CN 210085228U CN 201920265603 U CN201920265603 U CN 201920265603U CN 210085228 U CN210085228 U CN 210085228U
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tank
sludge
plate
reverse osmosis
filter
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王硕
王子文
王燕
李激
杨叙军
杨汉文
李冲
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Wuxi Guolian Environmental Science & Technology Co Ltd
Jiangnan University
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Wuxi Guolian Environmental Science & Technology Co Ltd
Jiangnan University
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Abstract

The utility model discloses a portable mud sheet frame filter-pressing dehydration and washing integrated device belongs to environmental engineering technical field. The device of the utility model mainly comprises a conditioning tank 1, a plate and frame filter press 2, a pH adjusting tank 4, an active coke adsorption tank 5, an aeration tank 6, a coagulation tank 7, a sedimentation tank 8, a first-level reverse osmosis device 9 and a second-level reverse osmosis device 10. The utility model integrates the sludge treatment system, is suitable for the conditions of small sludge yield, emergency sludge treatment and the like, and the treated filter pressing liquid can reach the B-level standard of the wastewater discharge town sewer water quality standard (CJ 343-2010); furthermore, the utility model discloses focus on retrieving phosphorus, embodied the theory of resource recycling.

Description

一种移动式污泥板框压滤脱水与清洗一体化装置A mobile sludge plate and frame filter press dehydration and cleaning integrated device

技术领域technical field

本实用新型涉及一种移动式污泥板框压滤脱水与清洗一体化装置,属于环境工程技术领域。The utility model relates to a mobile sludge plate and frame filter-pressing dehydration and cleaning integrated device, which belongs to the technical field of environmental engineering.

背景技术Background technique

随着我国水处理工程的发展,污水处理厂产生的污泥量日益增加。剩余污泥的含水率较高,有机质易腐败,气味恶臭且含有大量重金属、病菌等有毒有害物质,对污泥的处理处置,国家严格限制了污泥含水率标准,城镇污水处理厂污泥经处理后含水率小于60%,才可与垃圾混合填埋处置。但目前,我国一些小型污水处理厂和农村地区的生活污水处理系统因处理量较小,一般不会专设污泥处理系统;人工湖、景观水体中产生的污泥中也含有大量的有机物,且污泥中的N、P受到搅动很容易释放出来导致水体富营养化;雨水管道及河道底部也会沉积大量的污泥,如不及时清理,雨季可能导致排水不畅,引起水患。这些地方的污泥处理应该定期、及时、快速处理,且处理规模不宜太大。但是目前存在污泥处理设备较大且不易移动,使得其无法灵活应用上述场景。With the development of water treatment projects in China, the amount of sludge produced by sewage treatment plants is increasing. The excess sludge has a high moisture content, the organic matter is easily corrupted, the odor is foul and contains a large amount of heavy metals, bacteria and other toxic and harmful substances. The state strictly limits the sludge moisture content standards for the treatment and disposal of sludge. After treatment, the moisture content is less than 60% before it can be mixed with garbage for landfill disposal. However, at present, some small sewage treatment plants and domestic sewage treatment systems in rural areas in my country generally do not have a special sludge treatment system due to their small treatment capacity; the sludge produced in artificial lakes and landscape water bodies also contains a large amount of organic matter. In addition, the N and P in the sludge are easily released by agitation, resulting in eutrophication of the water body; a large amount of sludge will also be deposited at the bottom of rainwater pipes and river channels. If it is not cleaned in time, the rainy season may lead to poor drainage and cause flooding. The sludge treatment in these places should be regularly, timely and fast, and the treatment scale should not be too large. However, the existing sludge treatment equipment is large and difficult to move, making it impossible to flexibly apply the above scenarios.

实用新型内容Utility model content

针对上述问题,本实用新型提供了一种移动式污泥板框压滤脱水与清洗一体化装置,针对产量较小、需要定期或应急处理的污泥进行处理,避免了其对环境的二次污染,同时运行过程中产生的副产物可以回收二次利用,缓解了环境压力。In view of the above problems, the utility model provides a mobile sludge plate and frame filter press dehydration and cleaning integrated device, which is aimed at treating sludge with small output and requiring regular or emergency treatment, avoiding the secondary pollution to the environment. At the same time, the by-products produced in the operation process can be recycled and reused, which relieves the pressure on the environment.

本实用新型是一种移动式污泥板框压滤脱水与清洗一体化装置,所述装置包括污泥深度脱水系统、清洗系统、资源回收系统和运输装置,The utility model relates to a mobile sludge plate and frame filter press dehydration and cleaning integrated device, the device comprises a sludge deep dewatering system, a cleaning system, a resource recovery system and a transportation device,

所述污泥脱水系统包括调理池(1)、板框压滤机(2)、pH调节池(4)、活性焦吸附池(5)、曝气池(6)、混凝池(7)、沉淀池(8)、一级反渗透装置(9)、二级反渗透装置(10);The sludge dewatering system comprises a conditioning tank (1), a plate and frame filter press (2), a pH adjustment tank (4), an activated coke adsorption tank (5), an aeration tank (6), and a coagulation tank (7) , a sedimentation tank (8), a primary reverse osmosis device (9), and a secondary reverse osmosis device (10);

所述资源回收系统包括污泥收集装置(3)、磷沉淀收集装置(11)和浓缩水收集装置(12);The resource recovery system comprises a sludge collection device (3), a phosphorus precipitation collection device (11) and a concentrated water collection device (12);

所述运输装置为运输车(29);The transport device is a transport vehicle (29);

具体的,调理池(1)的出泥端与板框压滤机(2)通过螺旋泵(16)连接,板框压滤机(2)外接污泥收集装置(3),板框压滤机(2)出水管与pH调节池(4)连接,pH调节池 (4)出水管与活性焦吸附池(5)连接,活性焦吸附池(5)上部出水管通过输送泵(23)与曝气池(6)连接,曝气池(6)、混凝池(7)、沉淀池(8)之间依次由挡板隔开,磷沉淀收集装置(11)与沉淀池(8)底部连接,沉淀池(8)出水口与一级反渗透装置(9)连接,一级反渗透装置(9)与二级反渗透装置(10)连接,一级反渗透装置(9)和二级反渗透装置(10)均与浓缩水收集装置(12)相连,二级反渗透装置(10)的出水口之一连接外部,另一个出水口与板框压滤机(2)连接。Specifically, the sludge discharge end of the conditioning tank (1) is connected to the plate and frame filter press (2) through a screw pump (16), and the plate and frame filter press (2) is connected to a sludge collection device (3), and the plate and frame filter press (2) is connected to a sludge collection device (3). The outlet pipe of the machine (2) is connected with the pH adjustment tank (4), the outlet pipe of the pH adjustment tank (4) is connected with the activated coke adsorption tank (5), and the upper water outlet pipe of the activated coke adsorption tank (5) is connected to the activated coke adsorption tank (5) through a conveying pump (23). The aeration tank (6) is connected, the aeration tank (6), the coagulation tank (7), and the sedimentation tank (8) are separated by baffles in sequence, and the phosphorus precipitation collection device (11) is connected to the bottom of the sedimentation tank (8). connection, the water outlet of the sedimentation tank (8) is connected with the primary reverse osmosis device (9), the primary reverse osmosis device (9) is connected with the secondary reverse osmosis device (10), the primary reverse osmosis device (9) and the secondary reverse osmosis device (10) are connected. The reverse osmosis devices (10) are all connected to the concentrated water collection device (12), one of the water outlets of the secondary reverse osmosis device (10) is connected to the outside, and the other water outlet is connected to the plate and frame filter press (2).

在本实用新型的一种实施方式中,所述清洗系统是:二级反渗透装置10的出水口通过输送泵28与板框压滤机2连接,用于清洗板框压滤机2。In one embodiment of the present invention, the cleaning system is: the water outlet of the secondary reverse osmosis device 10 is connected to the plate and frame filter press 2 through the conveying pump 28 for cleaning the plate and frame filter press 2 .

在本实用新型的一种实施方式中,具体的,调理池1的出泥端与板框压滤机2通过螺旋泵16连接,板框压滤机2外接污泥收集装置3,板框压滤机2出水管与pH调节池4通过输送泵17连接,pH调节池4外部配有2号药剂储存罐19用于调节pH,pH调节池4出水管与活性焦吸附池5通过输送泵20连接,活性焦吸附池5上部出水管通过输送泵23与曝气池6 连接,曝气池6、混凝池7、沉淀池8之间依次由挡板隔开,含磷沉淀收集装置11与沉淀池 8底部连接,沉淀池8出水口通过输送泵27与一级反渗透装置9连接,一级反渗透装置9与二级反渗透装置10连接,一级反渗透装置9和二级反渗透装置10均与浓缩水收集装置12相连,二级反渗透装置10的出水口之一连接外部,另一个出水口通过输送泵28与板框压滤机 2连接。In an embodiment of the present invention, specifically, the mud discharge end of the conditioning tank 1 is connected to the plate and frame filter press 2 through a screw pump 16, and the plate and frame filter press 2 is connected to an external sludge collection device 3. The outlet pipe of the filter 2 is connected with the pH adjustment tank 4 through the delivery pump 17. The pH adjustment tank 4 is equipped with a No. 2 pharmaceutical storage tank 19 for adjusting the pH. The pH adjustment tank 4 outlet pipe and the active coke adsorption tank 5 pass through the delivery pump 20. The upper water outlet pipe of the activated coke adsorption tank 5 is connected to the aeration tank 6 through the conveying pump 23. The aeration tank 6, the coagulation tank 7 and the sedimentation tank 8 are separated by baffles in turn. The phosphorus-containing precipitation collection device 11 and the The bottom of the sedimentation tank 8 is connected, the water outlet of the sedimentation tank 8 is connected with the primary reverse osmosis device 9 through the delivery pump 27, the primary reverse osmosis device 9 is connected with the secondary reverse osmosis device 10, and the primary reverse osmosis device 9 and the secondary reverse osmosis device are connected. The devices 10 are all connected to the concentrated water collection device 12 , one of the water outlets of the secondary reverse osmosis device 10 is connected to the outside, and the other water outlet is connected to the plate and frame filter press 2 through a transfer pump 28 .

在本实用新型的一种实施方式中,所述1号药剂储存罐(13)与调理池(1)之间通过药剂输送控制箱(14)连接。In an embodiment of the present invention, the No. 1 medicine storage tank (13) and the conditioning pool (1) are connected through a medicine delivery control box (14).

在本实用新型的一种实施方式中,所述1号药剂储存罐13通过药剂输送控制箱14控制药剂投加量,用于调理污泥。In an embodiment of the present invention, the No. 1 chemical storage tank 13 controls the dosage of the chemical through the chemical conveying control box 14 for conditioning the sludge.

在本实用新型的一种实施方式中,所述pH调节池4内部设有搅拌器18。In an embodiment of the present invention, a stirrer 18 is provided inside the pH adjustment tank 4 .

在本实用新型的一种实施方式中,所述活性焦吸附池5内置活性焦填料21和石块承托层 22。In an embodiment of the present invention, the activated coke adsorption tank 5 has a built-in activated coke filler 21 and a rock support layer 22.

在本实用新型的一种实施方式中,所述pH调节池4与活性焦吸附池5的底部相连。In an embodiment of the present invention, the pH adjustment tank 4 is connected to the bottom of the activated coke adsorption tank 5 .

在本实用新型的一种实施方式中,所述挡板的高度使得混合液可以依靠重力作用依次通过曝气池6、混凝池7和沉淀池8。In an embodiment of the present invention, the height of the baffle plate enables the mixed liquid to pass through the aeration tank 6 , the coagulation tank 7 and the sedimentation tank 8 in sequence by the action of gravity.

在本实用新型的一种实施方式中,所述曝气池6底部设有曝气系统24,所述混凝池7外部配有3号药剂储存罐26,内置搅拌器25;所述沉淀池8底部外接含磷沉淀收集装置11,用于收集沉淀进行磷资源回收。In an embodiment of the present invention, an aeration system 24 is provided at the bottom of the aeration tank 6, a No. 3 chemical storage tank 26 is provided outside the coagulation tank 7, and a built-in agitator 25; the sedimentation tank 8. A phosphorus-containing precipitation collection device 11 is externally connected to the bottom for collecting precipitation for phosphorus resource recovery.

在本实用新型的一种实施方式中,所述1号药剂储存罐13中的调理药剂为FeCl3、石灰、聚丙烯酰胺(PAM),三者的质量比为3:15:0.7。其中,FeCl3和石灰可以改变污泥中颗粒与水的结合力,改善污泥脱水性能;PAM能够通过电中和、吸附架桥作用,使悬浮颗粒絮凝。In an embodiment of the present invention, the conditioning agents in the No. 1 agent storage tank 13 are FeCl 3 , lime, and polyacrylamide (PAM), and the mass ratio of the three is 3:15:0.7. Among them, FeCl 3 and lime can change the binding force between particles and water in the sludge and improve the dewatering performance of the sludge; PAM can flocculate suspended particles through electric neutralization and adsorption bridging.

在本实用新型的一种实施方式中,所述pH调节池4内的pH为7.0-8.0。In an embodiment of the present invention, the pH in the pH adjustment tank 4 is 7.0-8.0.

在本实用新型的一种实施方式中,所述混凝池7中投加的药剂是聚合氯化铝(PAC),目的是为了化学除磷。In an embodiment of the present invention, the agent added in the coagulation tank 7 is polyaluminum chloride (PAC), for the purpose of chemical phosphorus removal.

本实用新型取得的有益效果:The beneficial effects obtained by the utility model:

(1)首先在深度脱水系统中的调理池中加入调理药剂FeCl3、石灰、PAM,FeCl3和石灰可以改变污泥中颗粒与水的结合力,改善污泥脱水性能;PAM能够通过电中和、吸附架桥作用,使悬浮颗粒絮凝。(1) First, add conditioning agents FeCl 3 , lime, PAM to the conditioning tank in the deep dewatering system. FeCl 3 and lime can change the binding force between particles and water in the sludge and improve the dewatering performance of the sludge; PAM can pass through the electricity. And, adsorption bridging effect, so that suspended particles flocculation.

(2)活性焦吸附池中的活性焦表面富含羟基、羰基等官能团,可通过范德华力、静电作用、络合反应等吸附水中的难降解有机物和氮磷污染物。经过处理后,压滤液色度降低,难降解COD变为易降解COD,压滤液的可生化性提高。(2) The surface of the activated coke in the activated coke adsorption pool is rich in functional groups such as hydroxyl and carbonyl, which can adsorb refractory organic matter and nitrogen and phosphorus pollutants in water through van der Waals force, electrostatic interaction, complexation reaction, etc. After treatment, the chromaticity of the press filtrate is reduced, the refractory COD becomes easily degradable COD, and the biodegradability of the press filtrate is improved.

(3)通过曝气将滤液中的有机磷转化为无机磷,投加一定量的聚合氯化铝(PAC)进行化学除磷;混合液最终进入沉淀池进行沉淀、分层,形成的沉淀集中处理,用于资源回收,出水输送至下一级处理。(3) The organic phosphorus in the filtrate is converted into inorganic phosphorus by aeration, and a certain amount of polyaluminum chloride (PAC) is added for chemical phosphorus removal; the mixed solution finally enters the sedimentation tank for precipitation and stratification, and the formed precipitation is concentrated Treatment is used for resource recovery, and the effluent is transported to the next level of treatment.

(4)经过除磷后的出水依次经过两级反渗透装置,能够除去水中的杂质,如离子、有机物、细菌、病毒等,产生的浓水进入收集装置,其中含有较高浓度的COD,经厌氧发酵后其产物可以产生资源类气体甲烷或作为污水处理厂的补充碳源;产生的出水可以作为自身和板框压滤机的清洗水。(4) The effluent after phosphorus removal passes through the two-stage reverse osmosis device in turn, which can remove impurities in the water, such as ions, organics, bacteria, viruses, etc., and the concentrated water generated enters the collection device, which contains a higher concentration of COD. After anaerobic fermentation, its products can produce methane as a resource gas or as a supplementary carbon source for sewage treatment plants; the produced effluent can be used as cleaning water for itself and the plate and frame filter press.

(5)本实用新型将污泥处理系统一体化,集合了污泥深度脱水系统、清洗系统和资源回收系统,适用于污泥产量较低的污水处理厂、河道和人工水体等,同时也可作为污水处理厂污泥处理处置设施的必要补充,且上述装置可由运载装置运输,所述运载装置包括平板运输车、半挂车、拖车、或货车,以便于污泥量小、污泥紧急处理等情况,处理后的压滤液可达到《污水排入城镇下水道水质标准》(CJ343-2010)B级标准;此外,本实用新型注重对磷进行回收,体现了资源再利用的理念。(5) The utility model integrates the sludge treatment system, integrates the sludge deep dewatering system, the cleaning system and the resource recovery system, and is suitable for sewage treatment plants, river courses and artificial water bodies with low sludge output. As a necessary supplement to the sludge treatment and disposal facilities of the sewage treatment plant, the above-mentioned device can be transported by a carrier device including a flatbed truck, a semi-trailer, a trailer, or a truck, so as to facilitate small sludge volume, emergency sludge treatment, etc. Under certain circumstances, the treated press filtrate can reach the B-level standard of "Water Quality Standard for Sewage Discharged into Urban Sewers" (CJ343-2010); in addition, the utility model pays attention to the recovery of phosphorus, which reflects the concept of resource reuse.

附图说明Description of drawings

图1为本实用新型一种实施方式的结构示意图;其中,1,调理池;2,板框压滤机;4,pH调节池;5,活性焦吸附池;6,曝气池;7,混凝池;8,沉淀池;9,一级反渗透装置; 10,二级反渗透装置;13,1号药剂储存罐;26,3号药剂储存罐;29,运输车。1 is a schematic structural diagram of an embodiment of the present utility model; wherein, 1, conditioning tank; 2, plate and frame filter press; 4, pH adjustment tank; 5, activated coke adsorption tank; 6, aeration tank; 7, Coagulation tank; 8, sedimentation tank; 9, primary reverse osmosis device; 10, secondary reverse osmosis device; 13, No. 1 chemical storage tank; 26, No. 3 chemical storage tank; 29, transport vehicle.

图2为本实用新型提供的装置的工艺流程意图;其中1,调理池;2,板框压滤机;3,污泥收集装置;4,pH调节池;5,活性焦吸附池;6,曝气池;7,混凝池;8,沉淀池;9,一级反渗透装置;10,二级反渗透装置;11,含磷沉淀收集装置;12,浓缩水收集装置;13, 1号药剂储存罐;14,药剂输送控制箱;15,搅拌器;16,螺旋泵;17,输送泵;18,搅拌器;19,2号药剂储存罐;20,输送泵;21,活性焦填料;22,石块承托层;23,输送泵; 24,曝气系统;25,搅拌器;26,3号药剂储存罐;27,输送泵;28,输送泵。Fig. 2 is the process flow diagram of the device provided by the utility model; wherein 1, conditioning tank; 2, plate and frame filter press; 3, sludge collection device; 4, pH adjustment tank; 5, activated coke adsorption tank; 6, Aeration tank; 7, coagulation tank; 8, sedimentation tank; 9, primary reverse osmosis device; 10, secondary reverse osmosis device; 11, phosphorus-containing sedimentation collection device; 12, concentrated water collection device; 13, No. 1 Medicine storage tank; 14, medicine delivery control box; 15, agitator; 16, screw pump; 17, delivery pump; 18, agitator; 19, No. 2 medicine storage tank; 20, delivery pump; 21, activated coke filler; 22, stone supporting layer; 23, delivery pump; 24, aeration system; 25, agitator; 26, No. 3 pharmaceutical storage tank; 27, delivery pump; 28, delivery pump.

具体实施方式Detailed ways

为使本实用新型实现上述目的、特征和优点且能够更加明显易懂,下面结合具体实施方式对本实用新型作进一步详细的说明。In order to make the present utility model achieve the above-mentioned objects, features and advantages and make it more obvious and easy to understand, the present utility model will be described in further detail below with reference to the specific embodiments.

实施例1Example 1

如图2所示,本实用新型的装置包括所述装置包括污泥深度脱水系统、清洗系统、资源回收系统和运输装置,所述污泥脱水系统包括调理池1、板框压滤机2、pH调节池4、活性焦吸附池5、曝气池6、混凝池7、沉淀池8、一级反渗透装置9、二级反渗透装置10;所述资源回收系统包括污泥收集装置3、磷沉淀收集装置11和浓缩水收集装置12;所述运输装置为运输车29(见图1)。具体的,调理池1、板框压滤机2、pH调节池4、活性焦吸附池5、曝气池6、混凝池7、沉淀池8、一级反渗透装置9、二级反渗透装置10,依次通过管道和/ 或泵连接:其中调理池1内部设有搅拌器15,外部配有的1号药剂储存罐13通过药剂输送控制箱14控制药剂投加量,用于调理污泥,出泥端与板框压滤机2通过螺旋泵16连接,板框压滤机2外接污泥收集装置3,出水管与pH调节池4通过输送泵17连接,pH调节池4内部设有搅拌器18,外部配有2号药剂储存罐19用于调节pH,出水管与活性焦吸附池5通过输送泵20连接,活性焦吸附池5内置活性焦填料21和石块承托层22,出水管通过输送泵23 与曝气池6连接,曝气池6底部设有曝气系统24,混合液流入混凝池7与药剂混合,混凝池 7外部配有3号药剂储存罐26,内置搅拌器25,上层混合液流入沉淀池8进行沉淀,出水通过输送泵27进入一级反渗透装置9,底部外接含磷沉淀收集装置11,用于收集沉淀进行磷资源回收,一级反渗透装置9的出水流入二级反渗透装置10,一级反渗透装置9和二级反渗透装置10形成的浓缩水流入外接的浓缩水收集装置12,二级反渗透装置10的出水一部分直接排出,一部分通过输送泵28进入板框压滤机2,用于清洗板框压滤机2。As shown in Figure 2, the device of the present invention includes the device including a sludge deep dewatering system, a cleaning system, a resource recovery system and a transportation device, and the sludge dewatering system includes a conditioning tank 1, a plate and frame filter press 2, pH adjustment tank 4, activated coke adsorption tank 5, aeration tank 6, coagulation tank 7, sedimentation tank 8, primary reverse osmosis device 9, secondary reverse osmosis device 10; the resource recovery system includes a sludge collection device 3 , a phosphorus precipitation collection device 11 and a concentrated water collection device 12; the transportation device is a transportation vehicle 29 (see Figure 1). Specifically, conditioning tank 1, plate and frame filter press 2, pH adjustment tank 4, activated coke adsorption tank 5, aeration tank 6, coagulation tank 7, sedimentation tank 8, primary reverse osmosis device 9, secondary reverse osmosis The device 10 is connected by pipelines and/or pumps in sequence: the conditioning tank 1 is provided with a stirrer 15 inside, and the externally equipped No. 1 pharmaceutical storage tank 13 controls the dosage of the pharmaceutical through the pharmaceutical delivery control box 14 for conditioning the sludge. , the mud discharge end is connected with the plate and frame filter press 2 through the screw pump 16, the plate and frame filter press 2 is connected to the external sludge collection device 3, the water outlet pipe is connected with the pH adjustment tank 4 through the conveying pump 17, and the pH adjustment tank 4 is provided with The stirrer 18 is equipped with a No. 2 pharmaceutical storage tank 19 on the outside for adjusting pH. The water outlet pipe is connected to the activated coke adsorption tank 5 through a transfer pump 20. The activated coke adsorption tank 5 has a built-in activated coke filler 21 and a stone support layer 22. The water outlet pipe is connected with the aeration tank 6 through the conveying pump 23. The aeration system 24 is provided at the bottom of the aeration tank 6, and the mixed liquid flows into the coagulation tank 7 to be mixed with the chemical. The outside of the coagulation tank 7 is equipped with a No. 3 chemical storage tank 26. The built-in agitator 25, the upper layer mixed liquid flows into the sedimentation tank 8 for precipitation, the effluent enters the primary reverse osmosis device 9 through the transfer pump 27, and the phosphorus-containing precipitation collection device 11 is externally connected to the bottom to collect the sediment for phosphorus resource recovery. The primary reverse osmosis The effluent of the device 9 flows into the secondary reverse osmosis device 10, the concentrated water formed by the primary reverse osmosis device 9 and the secondary reverse osmosis device 10 flows into the external concentrated water collection device 12, and part of the effluent of the secondary reverse osmosis device 10 is directly discharged, A part enters the plate and frame filter press 2 through the transfer pump 28 for cleaning the plate and frame filter press 2 .

本实用新型装置的运行流程为:1号药剂储存罐13内装有FeCl3溶液、PAM溶液和石灰,通过输送管上的药剂输送控制箱14控制药剂进入调理池1;污泥进入调理池1后,在搅拌器 15的作用下与药剂充分混合;药剂调理后的污泥,通过螺旋泵16从板框压滤机2进料口进入,经过板框压榨后的污泥进入污泥收集装置3,用于焚烧,板框压滤机2压滤产生的滤液通过输送泵17进入pH调节池4;通过阀门控制2号药剂储存罐19中的盐酸溶液进入pH调节池4,使用搅拌器18将药剂和压滤液混合均匀;pH调节后的压滤液通过输送泵20从活性焦吸附池5底部进入,经过内置的活性焦填料21吸附后的出水(石块承托层22发挥支撑活性焦填料21的作用),通过输送泵23进入曝气池6;曝气池6底部的曝气系统24开启后,压滤液与污泥混合均匀,出水流入混凝池7;通过阀门控制3号药剂储存罐26中的聚合氯化铝(PAC)进入混凝池7,使用搅拌器25将药剂和压滤液混合均匀,上层混合液流入沉淀池8进行沉淀;上清液通过输送泵27进入一级反渗透装置9,形成的沉淀可进入含磷沉淀收集装置11中进行回收,同步实现资源化的目的;经一级反渗透装置9过滤后的出水流入二级反渗透装置10,一级反渗透装置9和二级反渗透装置10形成的浓缩水流入外接的浓缩水收集装置12,由于浓缩水中COD浓度较高,经厌氧发酵后其产物可以产生资源类气体甲烷或作为污水处理厂的补充碳源等;二级反渗透装置10的出水一部分直接排出,一部分通过输送泵 28进入板框压滤机2,用于清洗板框压滤机2,实现循环利用。The operation process of the device of the utility model is as follows: the No. 1 pharmaceutical storage tank 13 is filled with FeCl 3 solution, PAM solution and lime, and the pharmaceutical is controlled to enter the conditioning tank 1 through the pharmaceutical delivery control box 14 on the conveying pipe; after the sludge enters the conditioning tank 1 Under the action of the agitator 15, it is fully mixed with the agent; the sludge conditioned by the agent enters from the feed port of the plate and frame filter press 2 through the screw pump 16, and the sludge after the plate and frame press enters the sludge collection device 3 For incineration, the filtrate produced by the plate and frame filter press 2 press filtration enters the pH adjustment tank 4 through the delivery pump 17; the hydrochloric acid solution in the No. 2 pharmaceutical storage tank 19 is controlled by the valve into the pH adjustment tank 4, and the mixer The medicament and the press filtrate are mixed evenly; the pH-adjusted press filtrate enters from the bottom of the active coke adsorption tank 5 through the transfer pump 20, and the effluent after being adsorbed by the built-in active coke filler 21 (the stone support layer 22 plays a role in supporting the active coke filler 21). function), enter the aeration tank 6 through the delivery pump 23; after the aeration system 24 at the bottom of the aeration tank 6 is opened, the pressure filtrate and the sludge are mixed evenly, and the effluent flows into the coagulation tank 7; the No. 3 pharmaceutical storage tank is controlled by a valve The polyaluminum chloride (PAC) in 26 enters the coagulation tank 7, and the agitator 25 is used to mix the medicament and the pressure filtrate evenly, and the upper layer mixed liquid flows into the sedimentation tank 8 for precipitation; the supernatant enters the first-stage reverse osmosis through the transfer pump 27 In device 9, the formed precipitate can enter the phosphorus-containing sediment collection device 11 for recovery, and realize the purpose of resource utilization simultaneously; the effluent filtered by the primary reverse osmosis device 9 flows into the secondary reverse osmosis device 10, and the primary reverse osmosis device 9 The concentrated water formed with the secondary reverse osmosis device 10 flows into the external concentrated water collection device 12. Due to the high concentration of COD in the concentrated water, the product of anaerobic fermentation can produce methane as a resource gas or as a supplementary carbon source for the sewage treatment plant. Etc.; part of the effluent of the secondary reverse osmosis device 10 is directly discharged, and a part enters the plate and frame filter press 2 through the transfer pump 28 to clean the plate and frame filter press 2 and realize recycling.

虽然本实用新型已以较佳实施例公开如上,但其并非用以限定本实用新型,任何熟悉此技术的人,在不脱离本实用新型的精神和范围内,都可做各种的改动与修饰,因此本实用新型的保护范围应该以权利要求书所界定的为准。Although the present utility model has been disclosed above with preferred embodiments, it is not intended to limit the present utility model. Anyone who is familiar with this technology can make various changes and modifications without departing from the spirit and scope of the present utility model. Therefore, the protection scope of the present invention should be defined by the claims.

Claims (10)

1. A movable integrated device for filter-pressing, dewatering and cleaning of a sludge plate frame is characterized by comprising a sludge deep dewatering system, a cleaning system, a resource recovery system and a transportation device,
the sludge deep dehydration system comprises a conditioning tank (1), a plate-and-frame filter press (2), a pH adjusting tank (4), an active coke adsorption tank (5), an aeration tank (6), a coagulation tank (7), a sedimentation tank (8), a primary reverse osmosis device (9) and a secondary reverse osmosis device (10);
the resource recovery system comprises a sludge collection device (3), a phosphorus precipitation collection device (11) and a concentrated water collection device (12);
the transportation device is a transportation vehicle (29);
specifically, the sludge outlet end of a conditioning tank (1) is connected with a plate-and-frame filter press (2) through a screw pump (16), the plate-and-frame filter press (2) is externally connected with a sludge collection device (3), the water outlet pipe of the plate-and-frame filter press (2) is connected with a pH adjusting tank (4), the water outlet pipe of the pH adjusting tank (4) is connected with an active coke adsorption tank (5), the water outlet pipe at the upper part of the active coke adsorption tank (5) is connected with an aeration tank (6) through a delivery pump (23), the aeration tank (6), a coagulation tank (7) and a sedimentation tank (8) are sequentially separated by a baffle plate, a phosphorus precipitation collection device (11) is connected with the bottom of the sedimentation tank (8), the water outlet of the sedimentation tank (8) is connected with a primary reverse osmosis device (9), the primary reverse osmosis device (9) is connected with a secondary reverse osmosis device (10), the primary reverse osmosis device (9) and the secondary, one of the water outlets of the secondary reverse osmosis device (10) is connected with the outside, and the other water outlet is connected with the plate-and-frame filter press (2).
2. The movable integrated filter-pressing, dewatering and cleaning device for sludge plates and frames as claimed in claim 1, wherein the conditioning tank (1) is internally provided with a stirrer (15) and externally provided with a No. 1 medicament storage tank (13).
3. The movable integrated filter-pressing, dewatering and cleaning device for the sludge plate and frame according to claim 2, wherein the No. 1 medicament storage tank (13) is connected with the conditioning tank (1) through a medicament conveying control box (14).
4. The integrated filter-press dewatering and cleaning device for the movable sludge plate frame according to claim 1, wherein the activated coke adsorption tank (5) is internally provided with activated coke fillers (21) and a stone supporting layer (22), and the stone supporting layer (22) is positioned at the bottom layer.
5. The integrated device for filter-pressing, dewatering and cleaning of the movable sludge plate frame according to claim 1, characterized in that a No. 2 medicament storage tank (19) is arranged outside the pH adjusting tank (4) for adjusting pH.
6. The integrated filter-press dewatering and cleaning device for the movable sludge plate and frame according to claim 1, wherein the height of the baffle is such that the mixed liquor can pass through the aeration tank (6), the coagulation tank (7) and the sedimentation tank (8) in sequence by gravity.
7. The integrated device for filter-press dewatering and cleaning of mobile sludge plate and frame according to claim 1, characterized in that an aeration system (24) is arranged at the bottom of the aeration tank (6).
8. The integrated device for filter-pressing, dewatering and cleaning of mobile sludge plate and frame according to claim 1, characterized in that a No. 3 medicament storage tank (26) is arranged outside the coagulation tank (7) and a stirrer (25) is arranged inside.
9. The movable integrated filter-press dewatering and cleaning device for sludge with plate and frame filter-press according to claim 1, wherein the secondary reverse osmosis device (10) is connected with the plate and frame filter-press (2) for cleaning the plate and frame filter-press (2).
10. The movable integrated filter-pressing, dewatering and cleaning device for sludge plates and frames as claimed in claim 1, wherein the bottom of the sedimentation tank (8) is externally connected with a phosphorus-containing sediment collecting device (11) for collecting sediment for phosphorus resource recovery.
CN201920265603.2U 2019-03-01 2019-03-01 A mobile sludge plate and frame filter press dehydration and cleaning integrated device Active CN210085228U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112794618A (en) * 2020-12-18 2021-05-14 中交(天津)生态环保设计研究院有限公司 River, lake and pond polluted sediment modular dehydration method and dehydration system thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112794618A (en) * 2020-12-18 2021-05-14 中交(天津)生态环保设计研究院有限公司 River, lake and pond polluted sediment modular dehydration method and dehydration system thereof

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