CN110743212A - Efficient sludge discharge sedimentation tank - Google Patents
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- 239000010802 sludge Substances 0.000 title claims abstract description 168
- 238000004062 sedimentation Methods 0.000 title claims abstract description 107
- 239000006228 supernatant Substances 0.000 claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 238000007790 scraping Methods 0.000 claims abstract description 12
- 238000007599 discharging Methods 0.000 claims description 15
- 238000005192 partition Methods 0.000 claims description 12
- 238000004891 communication Methods 0.000 claims description 8
- 238000002955 isolation Methods 0.000 claims description 3
- 238000009825 accumulation Methods 0.000 claims description 2
- 230000008878 coupling Effects 0.000 claims 1
- 238000010168 coupling process Methods 0.000 claims 1
- 238000005859 coupling reaction Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 30
- 238000000034 method Methods 0.000 abstract description 22
- 239000013049 sediment Substances 0.000 abstract description 12
- 238000000926 separation method Methods 0.000 abstract description 2
- 238000010276 construction Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003657 drainage water Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000010408 sweeping Methods 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/245—Discharge mechanisms for the sediments
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/003—Sedimentation tanks provided with a plurality of compartments separated by a partition wall
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0087—Settling tanks provided with means for ensuring a special flow pattern, e.g. even inflow or outflow
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/30—Control equipment
- B01D21/32—Density control of clear liquid or sediment, e.g. optical control ; Control of physical properties
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Abstract
本发明公开了一种高效排泥沉淀池,包括位于两侧的多层沉淀池和中央排泥池,每层沉淀池底部均设底部刮泥机,通过底部刮泥机将两侧多层沉淀池底泥刮至中央排泥池,所述中央排泥池液位低于沉淀池,保证水流方向由两侧沉淀池流向中央排泥池,排泥池上方设置上清液回流管回流至沉淀池进水,排泥池底部设置浓缩刮泥装置,排泥池下方设置排泥管连接至污泥脱水装置。该发明主要应用在水处理沉淀工艺中,通过横向排泥缩短沉淀池排泥路径和频率,结合排泥区上清液回流系统,可实现自动连续水力排泥,快速实现泥水分离,有利于提高沉淀效率和底泥浓缩效果。
The invention discloses a high-efficiency sludge discharge sedimentation tank, comprising a multi-layer sedimentation tank located on both sides and a central sludge removal tank. A bottom sludge scraper is arranged at the bottom of each layer of sedimentation tank. The bottom sludge is scraped to the central sludge discharge tank. The liquid level of the central sludge discharge tank is lower than that of the sedimentation tank to ensure that the water flow direction flows from the sedimentation tanks on both sides to the central sludge discharge tank. The supernatant liquid return pipe is set above the sludge discharge tank to return to the sedimentation tank. The pool is filled with water, a concentrated sludge scraping device is set at the bottom of the sludge discharge tank, and a sludge discharge pipe is set below the sludge discharge tank to connect to the sludge dewatering device. The invention is mainly used in the water treatment sedimentation process. The sludge discharge path and frequency of the sedimentation tank are shortened by lateral sludge discharge. Combined with the supernatant liquid return system in the sludge discharge area, automatic and continuous hydraulic sludge discharge can be realized, and the separation of mud and water can be quickly realized, which is conducive to improving the Sedimentation efficiency and sediment concentration.
Description
技术领域technical field
本发明涉及一种高效排泥沉淀池。该系统主要应用在水处理沉淀工艺中,通过在多层沉淀池中央设置排泥区,可提高排泥系统效率,同时简化后续污泥处理流程,节约了占地面积和工程建设费用。The invention relates to a high-efficiency sludge discharge sedimentation tank. The system is mainly used in the water treatment sedimentation process. By setting a sludge discharge area in the center of the multi-layer sedimentation tank, the efficiency of the sludge discharge system can be improved, and the subsequent sludge treatment process can be simplified, saving the floor space and engineering construction costs.
背景技术Background technique
沉淀池是水处理厂占地较大的构筑物,而多层沉淀池通过提高单位面积的沉淀效率,节约了沉淀池占地面积,应用较为广泛。根据“浅池理论”,沉淀池中的沉淀物一旦沉至池底,就可被沉淀工艺去除。但实际运行中发现,沉至池底的污泥如不能及时清除,底泥会越积越多,最终导致底泥重新上浮,影响沉淀工艺处理效果。The sedimentation tank is a large-scale structure in the water treatment plant, and the multi-layer sedimentation tank saves the area of the sedimentation tank by improving the sedimentation efficiency per unit area, and is widely used. According to the "shallow pond theory", once the sediment in the sedimentation tank has settled to the bottom of the tank, it can be removed by the sedimentation process. However, in actual operation, it is found that if the sludge that settles to the bottom of the tank cannot be removed in time, the sediment will accumulate more and more, which will eventually lead to the re-floating of the sediment and affect the treatment effect of the sedimentation process.
传统多层沉淀池层数无法做多,主要是因为排泥系统的限制。一方面,传统纵向排泥导致排泥距离太长,各区域底泥分配差距过大,排泥速度过慢会导致沉淀池前段积泥量过多,排泥速度过快会导致沉淀池后段底泥扰动上浮。另一方面,传统排泥方向与水流方向相反,底泥需要克服水流运动方向反向运动,易产生旋涡流,增加底泥上浮概率,这也限制了多层沉淀池单层高度一般不小于2m的主要因素。The number of layers in the traditional multi-layer sedimentation tank cannot be increased, mainly because of the limitation of the sludge discharge system. On the one hand, the traditional longitudinal sludge discharge leads to a long sludge discharge distance, and the distribution gap of the sediment in each area is too large. If the sludge discharge speed is too slow, the amount of sludge in the front section of the sedimentation tank will be too much. The sediment is disturbed and floated up. On the other hand, the traditional sediment discharge direction is opposite to the water flow direction, and the sediment needs to overcome the reverse movement of the water flow direction, which is easy to generate vortex flow and increase the probability of sediment floating. main factor.
沉淀池除了自身影响水厂用地之外,沉淀工艺的后续污泥处理工艺也极大的影响了水厂用地。通常情况下,沉淀工艺排泥水需储存在排泥池,部分工艺需考虑回收上清液以节约水资源,排泥池或回收池底泥再提升至浓缩池,浓缩后排至平衡池,最终通过脱水机房脱水。以上污泥处理工艺不仅极大占用土地资源,而且增加了排泥水处理能耗,间接提高了制水成本。In addition to the sedimentation tank itself affecting the water plant land, the subsequent sludge treatment process of the sedimentation process also greatly affects the water plant land. Usually, the sludge drainage water in the sedimentation process needs to be stored in the sludge drainage tank. In some processes, it is necessary to consider recycling the supernatant to save water resources. The sludge in the sludge drainage tank or recovery tank is then lifted to the concentration tank, and then discharged to the balance tank after being concentrated. Dehydration through the dehydration room. The above sludge treatment process not only greatly occupies land resources, but also increases the energy consumption of sludge water treatment and indirectly increases the cost of water production.
为了解决这一问题,有必要研究一种高效排泥工艺,通过将排泥池与多层沉淀池合建,简化了沉淀池排泥系统和后续污泥处理工艺,从而整体上节约了水厂的总体占地面积和建设费用,并降低了制水成本。In order to solve this problem, it is necessary to study a high-efficiency sludge discharge process. By building the sludge discharge tank together with the multi-layer sedimentation tank, the sludge discharge system of the sedimentation tank and the subsequent sludge treatment process are simplified, thereby saving the water plant as a whole. The overall floor space and construction costs are reduced, and the cost of water production is reduced.
发明内容SUMMARY OF THE INVENTION
本发明目的是提供一种高效排泥沉淀池, 通过将排泥池与多层沉淀池合建,简化了沉淀池排泥系统和后续污泥处理工艺,节约了水厂的总体占地面积和建设费用,并降低了制水成本。The purpose of the present invention is to provide a high-efficiency sludge discharge sedimentation tank, which simplifies the sludge discharge system of the sedimentation tank and the subsequent sludge treatment process by building the sludge discharge tank together with the multi-layer sedimentation tank, and saves the overall floor space and cost of the water plant. Construction costs are reduced, and water production costs are reduced.
为了实现上述目的,本发明的技术方案是:一种高效排泥沉淀池,包括位于两侧的多层沉淀池和中央排泥池,每层沉淀池底部均设底部刮泥机,通过底部刮泥机将两侧多层沉淀池底泥刮至中央排泥池,所述中央排泥池液位低于沉淀池,保证水流方向由两侧沉淀池流向中央排泥池,排泥池上方设置上清液回流管回流至沉淀池进水,排泥池底部设置浓缩刮泥装置,排泥池下方设置排泥管连接至污泥脱水装置。In order to achieve the above-mentioned purpose, the technical scheme of the present invention is: a high-efficiency sludge discharge sedimentation tank, including a multi-layer sedimentation tank and a central sludge discharge tank located on both sides, and a bottom sludge scraper is provided at the bottom of each layer of sedimentation tank. The mud machine scrapes the bottom mud of the multi-layer sedimentation tanks on both sides to the central sludge discharge tank. The liquid level of the central sludge discharge tank is lower than that of the sedimentation tank to ensure that the water flow direction flows from the two sides of the sedimentation tanks to the central sludge discharge tank. The supernatant return pipe is returned to the sedimentation tank inlet water, a concentrated sludge scraping device is set at the bottom of the sludge discharge tank, and a sludge discharge pipe is set below the sludge discharge tank to connect to the sludge dewatering device.
进一步地,所述沉淀区和排泥区之间采用隔墙隔离。Further, a partition wall is used to separate the sedimentation zone and the sludge discharge zone.
进一步地,所述刮泥机靠近中央排泥池一侧设置防回流装置,避免排泥区污泥回流至各层沉淀区。Further, a backflow prevention device is provided on the side of the mud scraper close to the central mud discharge tank to prevent the backflow of sludge from the mud discharge area to the sedimentation areas of each layer.
进一步地,所述多层沉淀池内侧设置隔墙,隔墙底部有连通口,高0.3米至0.5米,用于刮泥机刮出的底泥从该连通口跌落至排泥区,防回流装置为设置在隔墙连通口处,且与刮泥机配合设置的橡胶隔离刷,用于彻底清除刮泥机上附着的污泥。Further, the inner side of the multi-layer sedimentation tank is provided with a partition wall, and the bottom of the partition wall is provided with a communication port with a height of 0.3 to 0.5 meters. The device is a rubber isolation brush arranged at the communication port of the partition wall and matched with the mud scraper, which is used to completely remove the sludge attached to the mud scraper.
进一步地,中央排泥池末端设置集泥坑,集泥坑深度应大于2m,主要目的是提高污泥浓度。Further, a mud collecting pit is set at the end of the central sludge discharge tank, and the depth of the mud collecting pit should be greater than 2m, the main purpose is to increase the sludge concentration.
进一步地,所述刮泥机采用并排布置,根据沉淀池积泥情况调整刮泥机运行速度,使得入口处的刮泥机运行速度快,出口处的刮泥机运行速度慢。Further, the scrapers are arranged side by side, and the running speed of the scrapers is adjusted according to the sludge accumulation in the sedimentation tank, so that the scraper at the inlet runs fast and the scraper at the outlet runs slowly.
进一步地,所述各层并联的多层沉淀池,其刮泥机在相同位置可采用统一驱动方式,各层沉淀区在相同位置可采用相同的刮泥速度,便于控制管理。Further, in the multi-layer sedimentation tank with each layer in parallel, the mud scraper can be driven in a unified manner at the same position, and the same mud scraping speed can be adopted for each layer of sedimentation zone at the same position, which is convenient for control and management.
本发明的高效排泥沉淀池利用了沉淀池和排泥池的液位差,实现全重力排泥,无需任何提升装置,节约了能耗,可节省了排泥池、回收池、浓缩池、平衡池等污泥处理构筑物。各层沉淀池共用排泥区,提高了排泥效率,节约了占地面积。同时,采用上清液排放措施,不仅缩短了上清液回流的距离,而且利用上清液回流实现排泥池底部进泥口的正向水力流态,避免排泥池内污泥再次进入沉淀池。The high-efficiency sludge discharge sedimentation tank of the present invention utilizes the liquid level difference between the sedimentation tank and the sludge discharge tank to realize full gravity sludge discharge without any lifting device, saves energy consumption, and can save the sludge discharge tank, recovery tank, concentration tank, Sludge treatment structures such as balance tanks. The sedimentation tank of each layer shares the sludge discharge area, which improves the sludge discharge efficiency and saves the floor space. At the same time, the use of supernatant discharge measures not only shortens the distance of supernatant backflow, but also uses supernatant backflow to realize the positive hydraulic flow state of the mud inlet at the bottom of the sludge discharge tank, preventing the sludge in the sludge discharge tank from entering the sedimentation tank again. .
附图说明Description of drawings
图1为一种新型高效排泥沉淀池平面图。Figure 1 is a plan view of a new type of high-efficiency sludge sedimentation tank.
图2为一种新型高效排泥沉淀池A-A剖面图。Figure 2 is a cross-sectional view A-A of a new type of high-efficiency sludge sedimentation tank.
图3为一种新型高效排泥沉淀池B-B剖面图。Figure 3 is a B-B sectional view of a new type of high-efficiency sludge sedimentation tank.
图4为一种新型高效排泥沉淀池C-C剖面图。Figure 4 is a C-C sectional view of a new type of high-efficiency sludge discharge sedimentation tank.
具体实施方式Detailed ways
下面结合附图和实施例对本发明做进一步的描述。The present invention will be further described below with reference to the accompanying drawings and embodiments.
本发明此实施例是一种新型高效排泥沉淀池,它主要由多层沉淀池和中央排泥池组成。This embodiment of the present invention is a novel high-efficiency sludge discharge sedimentation tank, which is mainly composed of a multi-layer sedimentation tank and a central sludge removal tank.
多层沉淀池设置在两侧,中央被排泥池分隔。多层沉淀池各沉淀区采用底部刮泥机,刮泥机可采用往复式、链条式或其他类型,但刮泥方向为两侧向中间刮泥,最终将底泥刮至中央排泥池。由于中央排泥区功能为接纳各层底泥,因此各层沉淀池排泥过程中并不影响其他层沉淀池正常运行。The multi-layer sedimentation tanks are arranged on both sides, and the center is separated by a sludge discharge tank. Each sedimentation area of the multi-layer sedimentation tank adopts a bottom scraper. The scraper can be reciprocating, chain or other types, but the scraping direction is to scrape the sludge from both sides to the middle, and finally scrape the bottom sludge to the central sludge discharge tank. Since the function of the central sludge discharge area is to receive the bottom sludge of each layer, the sludge discharge process of each layer of sedimentation tanks does not affect the normal operation of other layers of sedimentation tanks.
如图所示,本发明中央排泥池与两侧多层沉淀池为一座组合池,排泥池位于两格沉淀池中间,与两格沉淀池采用统一底板结构。排泥池宽度2米至6米,排泥池内底标高须低于沉淀池内地标高至少2米至4米。排泥池底部采用刮泥机,刮泥至排泥池终端集泥坑,最终排入后续污泥处理设施。排泥池顶部采用穿孔管或出水堰等,排出上清液或通过提升泵提升上清液回流至沉淀池进水管。As shown in the figure, the central sludge discharge tank and the multi-layer sedimentation tanks on both sides of the present invention are a combined tank, and the sludge discharge tank is located in the middle of the two sedimentation tanks, and adopts a unified floor structure with the two sedimentation tanks. The width of the sludge discharge tank is 2 to 6 meters, and the inner bottom elevation of the sludge removal tank must be at least 2 to 4 meters lower than the inner elevation of the sedimentation tank. A mud scraper is used at the bottom of the sludge discharge tank to scrape the sludge to the sludge collection pit at the terminal of the sludge discharge tank, and finally discharge it into the subsequent sludge treatment facilities. The top of the sludge discharge tank adopts a perforated pipe or an outlet weir, etc., to discharge the supernatant or lift the supernatant through a lift pump and return it to the water inlet pipe of the sedimentation tank.
沉淀区刮泥机1敷设在各层沉淀池底部,刮泥机长度与沉淀池宽度相同,刮泥机宽度通常可取10米至20米,具体应根据沉淀池总长度以及刮泥机台数确定。刮泥机1可采用链条式或往复式等多种形式,主要功能为刮动两侧沉淀区底部沉积污泥至中央排泥区。The
排泥区刮泥机2主要作用为浓缩并刮动排泥区底部积泥至排泥区集泥区,最终排入污泥脱水系统。The main function of the
上清液排放系统3采用穿孔管,也可采用出水堰等其他出水形式,主要作用是排出排泥区上清液,或回流上清液至沉淀池进水,同时上清液排放系统应保证排泥区水面液位低于沉淀区水面液位,使沉淀池与排泥池之间水流方向一直流向排泥池,避免排泥池污泥回流至沉淀池,造成底泥上浮。The
排泥管4采用电动调流阀门控制排泥速度,并设置污泥浓度计,浓度低于1%时停止排泥。The sludge discharge pipe 4 uses an electric flow regulating valve to control the sludge discharge speed, and a sludge concentration meter is installed. When the concentration is lower than 1%, the sludge discharge is stopped.
集泥坑5为中央排泥池末端,坑深度应大于2m,主要目的是提高污泥浓度。The
所述多层沉淀池内侧设置隔墙,隔墙底部有连通口,高0.3米至0.5米,用于刮泥机刮出的底泥从该连通口跌落至排泥区。The inner side of the multi-layer sedimentation tank is provided with a partition wall, and the bottom of the partition wall has a communication port with a height of 0.3 to 0.5 meters.
防回流装置6为设置在隔墙连通口处,且与刮泥机配合设置的橡胶隔离刷,用于彻底清除刮泥机上附着的污泥,防止已经排出的污泥再次回到沉淀区的装置,影响沉淀效果。防回流装置6也有清理刮泥机1的作用,避免刮泥机1长时间运行造成的污泥吸附情况。The
它区别于现有技术之处在于:It is different from the existing technology in that:
1.相比传统多层沉淀池与排泥池分建的形式,本发明采用多层沉淀池与排泥池合建的形式,缩短了排泥和上清液回流距离,减少了水厂总体构筑物数量,节约了占地面积。1. Compared with the separate construction of the traditional multi-layer sedimentation tank and the sludge discharge tank, the present invention adopts the form of the combined construction of the multi-layer sedimentation tank and the sludge discharge tank, which shortens the distance of sludge discharge and supernatant backflow, and reduces the overall water plant. The number of structures saves floor space.
2.相比传统多层沉淀池排泥方式,本发明采用独立排泥区,避免了各层沉淀池排泥过程中对其他层沉淀池的影响,同时也极大提高了空间利用率,各层沉淀池均可共用排泥区,节约用地的同时,也提高了污泥吸附卷扫效果,提高了排泥区底泥浓缩效果。2. Compared with the traditional multi-layer sedimentation tank discharging method, the present invention adopts an independent sludge discharging area, which avoids the influence on other layers of sedimentation tanks during the sludge discharging process of each layer of sedimentation tanks, and also greatly improves the space utilization rate. Both layers of sedimentation tanks can share the sludge discharge area, which saves land, improves the effect of sludge adsorption and sweeping, and improves the sediment concentration effect in the sludge discharge area.
3.相比传统平流沉淀池纵向刮泥方式,本发明两侧沉淀池采用由两侧向中央刮泥的方式,可极大缩短刮泥行程,减小了底泥停留时间。3. Compared with the vertical scraping method of the traditional advection sedimentation tank, the sedimentation tank on both sides of the present invention adopts the method of scraping the sludge from both sides to the center, which can greatly shorten the scraping stroke and reduce the sediment retention time.
4.相比于平流沉淀池等速刮泥方式,本发明可在沉淀池长度方向设置多台刮泥机,靠近沉淀池入口处的刮泥机运行速度快,靠近沉淀池出口处的刮泥机运行速度慢。这种变速刮泥的方式适应了沉淀池入口污泥多,出口污泥少的特点。一方面通过入口刮泥机的快速运行可及时刮走入口处的大量污泥,另一方面通过出口刮泥机的慢速运行避免刮泥速度过快扰动底部轻小絮体再次上浮。由于本发明采用各层沉淀池并联方式,再确保进水端均匀的情况下,上下各层沉淀池底泥量十分接近,上下各层沉淀池可共用刮泥机,即相同位置的各层沉淀池采用相同的刮泥速度,减小控制难度。4. Compared with the constant-speed mud scraping method of the advection sedimentation tank, the present invention can set up multiple mud scrapers in the length direction of the sedimentation tank. The machine runs slowly. This variable-speed mud scraping method adapts to the characteristics of more sludge at the entrance of the sedimentation tank and less sludge at the exit. On the one hand, a large amount of sludge at the entrance can be scraped off in time by the fast operation of the mud scraper at the entrance, and on the other hand, the slow operation of the mud scraper at the outlet can prevent the mud scraping speed from being too fast and disturbing the light and small flocs at the bottom to float again. Since the present invention adopts the parallel connection mode of each layer of sedimentation tanks, and under the condition that the water inlet end is uniform, the amount of sediment in the upper and lower layers of sedimentation tanks is very close, and the upper and lower layers of sedimentation tanks can share the mud scraper, that is, the sedimentation layers in the same position The pool adopts the same scraping speed to reduce the difficulty of control.
5.相比于传统平流沉淀池排泥方式,本发明充分利用了沉淀池液位差,排泥池内排泥水无需水泵提升,可直接依靠排泥池较高的液位实现重力排泥,节约了能耗。5. Compared with the traditional advection sedimentation tank discharging method, the present invention makes full use of the liquid level difference in the sedimentation tank, and the sludge water in the sludge discharging tank does not need to be lifted by a pump, and can directly rely on the higher liquid level in the sludge discharging tank to realize gravity sludge discharge, saving energy. energy consumption.
6.相比于传统的平流沉淀池,本发明沉淀区和排泥区液位高差很小,上清液回流能耗极低,因此可实现上清液大流量回流。这有利于提高絮体去除效率,一方面使大絮体尽早排入排泥区进行浓缩,另一方面使小絮体通过上清液回流重新絮凝形成大絮体。6. Compared with the traditional advection sedimentation tank, the liquid level difference between the sedimentation area and the sludge discharge area of the present invention is very small, and the energy consumption of the supernatant liquid backflow is extremely low, so the supernatant liquid backflow can be realized with a large flow. This is beneficial to improve the floc removal efficiency. On the one hand, the large flocs are discharged into the sludge discharge area for concentration as soon as possible, and on the other hand, the small flocs are re-flocculated through the backflow of the supernatant to form large flocs.
7.相比于传统的平流沉淀池,本发明实现了底泥和沉淀原水的快速分离,同时上清液回流。排泥水的排放等措施也保证了沉淀池至排泥池的连通口一直是水流正流入状态,消除了排泥池底泥回流至沉淀池,造成底泥上浮等不利现象。这种特性也避免了上层沉淀池排泥可能回流至下层沉淀池的情况。7. Compared with the traditional advection sedimentation tank, the present invention realizes the rapid separation of the bottom sludge and the precipitation raw water, and the supernatant liquid is refluxed at the same time. The measures such as the discharge of sludge water also ensure that the communication port from the sedimentation tank to the sludge discharge tank is always in the state of positive flow of water, which eliminates the unfavorable phenomenon of the bottom sludge from the sludge discharge tank returning to the sedimentation tank and causing the bottom sludge to float. This feature also avoids the situation that the sludge discharged from the upper sedimentation tank may flow back to the lower sedimentation tank.
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