CN111701326A - A mud-water separation device for sewage treatment - Google Patents
A mud-water separation device for sewage treatment Download PDFInfo
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- CN111701326A CN111701326A CN202010486086.9A CN202010486086A CN111701326A CN 111701326 A CN111701326 A CN 111701326A CN 202010486086 A CN202010486086 A CN 202010486086A CN 111701326 A CN111701326 A CN 111701326A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 66
- 238000000926 separation method Methods 0.000 title claims abstract description 45
- 239000010865 sewage Substances 0.000 title claims abstract description 32
- 239000004744 fabric Substances 0.000 claims abstract description 60
- 239000010802 sludge Substances 0.000 claims abstract description 23
- 230000005540 biological transmission Effects 0.000 claims abstract description 11
- 238000003825 pressing Methods 0.000 claims abstract description 5
- 230000003014 reinforcing effect Effects 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 2
- 238000005507 spraying Methods 0.000 claims description 2
- 238000001914 filtration Methods 0.000 abstract description 12
- 238000006243 chemical reaction Methods 0.000 abstract description 11
- 238000000034 method Methods 0.000 description 10
- 238000004140 cleaning Methods 0.000 description 7
- 230000008569 process Effects 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000004062 sedimentation Methods 0.000 description 6
- 238000005345 coagulation Methods 0.000 description 5
- 230000015271 coagulation Effects 0.000 description 5
- 239000007921 spray Substances 0.000 description 5
- 230000005484 gravity Effects 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000005374 membrane filtration Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000011499 joint compound Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000009285 membrane fouling Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
- 239000003403 water pollutant Substances 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/35—Filters with filtering elements which move during the filtering operation with multiple filtering elements characterised by their mutual disposition
- B01D33/37—Filters with filtering elements which move during the filtering operation with multiple filtering elements characterised by their mutual disposition in parallel connection
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/44—Regenerating the filter material in the filter
- B01D33/46—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element
- B01D33/461—Regenerating the filter material in the filter by scrapers, brushes nozzles or the like acting on the cake-side of the filtering element brushes
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- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Sludge (AREA)
Abstract
本发明属于污水处理技术领域,公开了一种用于污水处理的泥水分离装置,包括同心圆均布的多个旋转滤筒,旋转滤筒的筒身设置有透水孔并包裹有滤布;旋转滤筒的底部通过旋转接头连接污水收集管;滤布在旋转滤筒外部通过两根固定的压紧胶辊相互对压而实现滤布对旋转滤筒的包裹;滤筒传动电机驱动中心筒旋转,中心筒通过滤布带动各个旋转滤筒进行旋转;同时滤布由滤布张紧系统提供张紧力。本发明将传统泥水分离装置的竖直过滤变更为水平过滤,能够增加过滤面积、提高过滤速度,从而增大泥水分离表面负荷,减少占地面积,增加回流污泥浓度,提高生物反应池反应速率,减少泥水分离池和生物反应池的池体投资,并且可做成任何形状更利于组合布置。
The invention belongs to the technical field of sewage treatment, and discloses a mud-water separation device for sewage treatment. The bottom of the filter cartridge is connected to the sewage collection pipe through a rotary joint; the filter cloth is pressed against each other by two fixed pressing rubber rollers outside the rotating filter cartridge to realize the wrapping of the filter cloth on the rotating filter cartridge; the filter cartridge transmission motor drives the central cylinder to rotate , the central cylinder drives each rotating filter cylinder to rotate through the filter cloth; at the same time, the filter cloth is provided with tension by the filter cloth tensioning system. The invention changes the vertical filtration of the traditional mud-water separation device to the horizontal filtration, which can increase the filtration area and increase the filtration speed, thereby increasing the surface load of the mud-water separation, reducing the floor space, increasing the concentration of the return sludge, and improving the reaction rate of the biological reaction tank. , reducing the investment of the mud-water separation tank and the biological reaction tank, and it can be made into any shape, which is more conducive to the combination arrangement.
Description
技术领域technical field
本发明属于污水处理技术领域,更具体的说,是涉及一种污水处理厂生物反应池后用于泥水分离的装置。The invention belongs to the technical field of sewage treatment, and more specifically relates to a device for separating mud and water after a biological reaction tank in a sewage treatment plant.
背景技术Background technique
国内污水处理厂的污染物排放标准越来越高,由原来《城镇污水处理厂污染物排放标准》(GB18918-2002)二级排放标准提高到一级B、一级A,甚至北京市、天津市等地的地方排放标准《水污染物综合排放标准》(DB11/307-2013)、《城镇污水处理厂污染物排放标准》(DB12/599-2015)等,各项污染物排放指标均趋于严格,其中SS排放标准由原来的20mg/L升高到10mg/L,甚至到地方排放标准的5mg/L。The pollutant discharge standard of domestic sewage treatment plants is getting higher and higher. The local discharge standards of cities and other places "Comprehensive Discharge Standard of Water Pollutants" (DB11/307-2013), "Pollutant Discharge Standard for Urban Sewage Treatment Plants" (DB12/599-2015), etc. The SS emission standard has been raised from the original 20mg/L to 10mg/L, and even to the local emission standard of 5mg/L.
在排放标准提高的过程中,污水处理工艺也由预处理+二级处理+泥水分离升级到预处理+二级处理+泥水分离+混凝沉淀过滤工艺,进而发展到目前较为普遍的预处理+二级处理+泥水分离+混凝沉淀+高级氧化+(反硝化)过滤的工艺。但生物处理后的泥水分离,至今为止无论在池型、沉淀方式、设计参数等方面都没有任何变化。In the process of improving the discharge standard, the sewage treatment process has also been upgraded from pretreatment + secondary treatment + mud water separation to pretreatment + secondary treatment + mud water separation + coagulation sedimentation filtration process, and then developed to the more common pretreatment + The process of secondary treatment + mud water separation + coagulation sedimentation + advanced oxidation + (denitrification) filtration. However, the sludge-water separation after biological treatment has not changed so far in terms of pool type, sedimentation method, and design parameters.
传统的泥水分离方式在当时的排放标准下,有着处理效果稳定、能耗低、运行管理方便等优点。但是,同时也暴露了现状泥水分离工艺的四个固有缺点:一、固液分离表面负荷低,单池所需占地面积较大,土建投资较大;圆形沉淀池组合更降低了土地利用率,矩形沉淀池虽然在池体组合方面有一定的优势,但也没有从根本上改观表面负荷低导致占地面积大的劣势。二、由于采用重力集泥方式,污泥不用沉降,一般回流污泥浓度仅6000~8000mg/L,回流污泥浓度低,需要大量的外回流,一方面增加回流能耗,一方面降低生物反应池效率。三、容易发生污泥膨胀。四、由于池体内水的流态至关重要,关乎泥水分离成败,所以传统泥水分离需要设置良好的配水渠道、增设水力挡板。The traditional mud-water separation method has the advantages of stable treatment effect, low energy consumption and convenient operation and management under the discharge standards at that time. However, it also exposes four inherent shortcomings of the current mud-water separation process: 1. Low surface load for solid-liquid separation, large area required for a single tank, and large civil construction investment; the combination of circular sedimentation tanks reduces land use. Although the rectangular sedimentation tank has certain advantages in the combination of the tank body, it does not fundamentally improve the disadvantage of low surface load and large floor space. 2. Due to the gravity sludge collection method, the sludge does not need to settle. Generally, the return sludge concentration is only 6000-8000 mg/L. The return sludge concentration is low and requires a large amount of external return flow. On the one hand, it increases the energy consumption of the return flow and reduces the biological reaction on the other hand pool efficiency. Third, sludge bulking is prone to occur. 4. Since the flow state of the water in the pool is very important, it is related to the success or failure of mud-water separation, so the traditional mud-water separation needs to set up good water distribution channels and add hydraulic baffles.
随着排放标准的提高,泥水分离工艺段后增加了混凝沉淀+高级氧化+(反硝化)过滤等工艺。传统的泥水分离工艺已经不是污水处理厂的把关工艺,如果还采用传统的泥水分离方式,则更加凸显传统泥水分离过分追求沉淀效果反而造成后续混凝沉淀段由于结合物少而造成混凝沉淀效果不好,影响工艺整体处理效果的弊端。With the improvement of emission standards, coagulation sedimentation + advanced oxidation + (denitrification) filtration and other processes have been added after the mud-water separation process section. The traditional mud-water separation process is no longer the gatekeeping process of the sewage treatment plant. If the traditional mud-water separation method is still adopted, it will be more prominent that the traditional mud-water separation pursues the precipitation effect too much, but will cause the coagulation and precipitation effect in the subsequent coagulation and precipitation section due to less binding substances. Not good, the disadvantages that affect the overall treatment effect of the process.
为了改变传统泥水分离工艺的弊端,尤其是为了增加回流污泥浓度,近年来在传统重力分离的基础上,增加了膜过滤分离。其泥水分离率高、出水SS低、占地面积较小,反应池污泥浓度高。但膜分离过程中能耗大大增加,同时为了防止膜污染,需要增加大量鼓风曝气,这样随着污泥回流,将会带大量溶解氧至反应池前端,降低了反硝化脱氮效率。In order to change the disadvantages of the traditional sludge-water separation process, especially to increase the concentration of the return sludge, membrane filtration separation has been added on the basis of traditional gravity separation in recent years. The mud-water separation rate is high, the effluent SS is low, the floor area is small, and the sludge concentration of the reaction tank is high. However, the energy consumption during the membrane separation process is greatly increased. At the same time, in order to prevent membrane fouling, a large amount of blast aeration needs to be added. This will bring a large amount of dissolved oxygen to the front end of the reaction tank with the return of the sludge, reducing the denitrification and denitrification efficiency.
发明内容SUMMARY OF THE INVENTION
本发明着力于解决传统重力泥水分离及膜过滤分离的固有缺点,提供一种用于污水处理的泥水分离装置,将传统重力分离及过滤分离有机结合起来,并与目前国内污水厂新的排放标准相适应,体现了一种新的技术理念。The invention focuses on solving the inherent shortcomings of traditional gravity separation of mud and water and membrane filtration separation, and provides a mud water separation device for sewage treatment, which organically combines traditional gravity separation and filtration separation, and is compatible with the current new discharge standards of domestic sewage plants. Adapted to reflect a new technical concept.
为了解决上述技术问题,本发明具体通过以下的技术方案予以实现:In order to solve the above-mentioned technical problems, the present invention is specifically realized through the following technical solutions:
一种用于污水处理的泥水分离装置,包括池体,所述池体内部设置有同心圆均布的多个旋转滤筒,每个所述旋转滤筒的筒身设置有透水孔,每个所述旋转滤筒外部包裹有覆盖所述透水孔的滤布;每个所述旋转滤筒的底部通过旋转接头连接污水收集管;所述滤布在每个所述旋转滤筒外部通过两根固定的压紧胶辊相互对压而实现所述滤布对所述旋转滤筒的包裹;多个所述旋转滤筒之间设置有中心筒,所述中心筒由滤筒传动电机驱动进行旋转,所述滤布绕设在中心筒外部并依次连续地绕过各个所述旋转滤筒,所述中心筒通过所述滤布带动各个所述旋转滤筒进行旋转;同时,所述滤布由滤布张紧系统提供张紧力。A mud-water separation device for sewage treatment, comprising a pool body, a plurality of rotating filter cartridges uniformly distributed in concentric circles are arranged inside the pool body, and the cylindrical body of each of the rotating filter cartridges is provided with water permeable holes, and each The outside of the rotating filter cartridge is wrapped with a filter cloth covering the permeable holes; the bottom of each rotating filter cartridge is connected to a sewage collection pipe through a rotary joint; the filter cloth passes through two outside the rotating filter cartridge. The fixed pressing rubber rollers are pressed against each other to realize the wrapping of the filter cloth on the rotating filter cylinder; a center cylinder is arranged between the multiple rotating filter cylinders, and the center cylinder is driven by the filter cylinder transmission motor to rotate. , the filter cloth is wound around the outside of the central cylinder and successively bypasses each of the rotating filter cylinders, and the central cylinder drives each of the rotating filter cylinders to rotate through the filter cloth; at the same time, the filter cloth is made of The filter cloth tensioning system provides tension.
进一步地,所述池体设置有进水管道和出水总管,所述进水管道与所述池体内部连通,所述出水总管与所述污水收集管连接。Further, the pool body is provided with a water inlet pipe and a water outlet main pipe, the water inlet pipe is communicated with the inside of the pool body, and the water outlet main pipe is connected with the sewage collection pipe.
进一步地,所述池体四周设置有溢流堰。Further, overflow weirs are arranged around the tank body.
进一步地,所述旋转滤筒顶部通过加强筋板连接有连座轴承。Further, the top of the rotating filter cartridge is connected with a seat bearing through a reinforcing rib plate.
进一步地,所述滤布张紧系统由张紧弹簧、张紧摆臂、张紧旋转轴、张紧胶辊构成,所述滤布的张紧力由所述张紧弹簧提供,通过所述张紧摆臂产生力矩,并作用在所述张紧旋转轴上,再通过所述张紧胶辊将作用力传递到所述滤布上,完成对所述滤布的自动张紧。Further, the filter cloth tensioning system is composed of a tensioning spring, a tensioning swing arm, a tensioning rotating shaft, and a tensioning rubber roller, and the tensioning force of the filter cloth is provided by the tensioning spring, through the The tensioning swing arm generates torque and acts on the tensioning rotating shaft, and then transmits the force to the filter cloth through the tensioning rubber roller to complete the automatic tensioning of the filter cloth.
进一步地,所述旋转滤筒之间设置有旋转毛刷,所述旋转毛刷作用于所述滤布表面;所述旋转毛刷入口方位的所述滤布表面设置有喷淋管路和喷嘴。Further, a rotating brush is provided between the rotating filter cartridges, and the rotating brush acts on the surface of the filter cloth; the surface of the filter cloth at the entrance of the rotating brush is provided with a spray pipeline and a nozzle .
进一步地,所述池体底部设置有污泥泵,用于排出污泥。Further, a sludge pump is provided at the bottom of the tank body for discharging sludge.
本发明的有益效果是:The beneficial effects of the present invention are:
本发明通过独特的滤筒滤布布置形式及传动系统、滤布支撑系统、滤布张紧系统、滤布清洗系统,将传统泥水分离装置的竖直过滤变更为水平过滤,能够增加过滤面积、提高过滤速度,从而增大了泥水分离表面负荷,减少了至少一半的占地面积,增加了回流污泥浓度,提高生物反应池反应速率,减少泥水分离池和生物反应池的池体投资,并且不需要布水系统,可做成任何形状更利于组合布置。The invention changes the vertical filtration of the traditional mud-water separation device to the horizontal filtration through the unique arrangement of the filter cartridge and filter cloth and the transmission system, the filter cloth support system, the filter cloth tensioning system and the filter cloth cleaning system, which can increase the filter area, Increase the filtration speed, thereby increasing the surface load of the mud-water separation, reducing the floor space by at least half, increasing the return sludge concentration, increasing the reaction rate of the biological reaction tank, reducing the investment of the mud-water separation tank and the biological reaction tank, and No water distribution system is required, and it can be made into any shape, which is more convenient for combined arrangement.
附图说明Description of drawings
图1是实施例中泥水分离装置的立面图;Fig. 1 is the elevation view of the mud-water separation device in the embodiment;
图2是实施例中泥水分离装置的平面图;Fig. 2 is the plan view of the mud-water separation device in the embodiment;
图3是实施例中泥水分离装置的滤布张紧系统平面图;3 is a plan view of the filter cloth tensioning system of the mud-water separation device in the embodiment;
图4是图3的A-A剖面图;Fig. 4 is the A-A sectional view of Fig. 3;
图5是实施例中泥水分离装置的滤布清洗系统平面图;5 is a plan view of the filter cloth cleaning system of the mud-water separation device in the embodiment;
图6是图5的B-B剖面图。FIG. 6 is a B-B cross-sectional view of FIG. 5 .
上述图中:1-进水管道、2-溢流堰、3-旋转滤筒、4-滤布、5-旋转接头、6-污水收集管、7-出水总管、8-压紧胶辊、9-滤筒传动电机、10-中心筒、11-张紧弹簧、12-张紧摆臂、13-张紧旋转轴、14-张紧胶辊、15-旋转毛刷、16-毛刷传动电机、17-链轮、18-喷嘴、19-喷淋管路、20-污泥泵。In the above picture: 1- water inlet pipe, 2- overflow weir, 3- rotating filter cartridge, 4- filter cloth, 5- rotating joint, 6- sewage collection pipe, 7- water outlet main pipe, 8- pressing rubber roller, 9- Filter cylinder drive motor, 10- Center cylinder, 11- Tension spring, 12- Tension swing arm, 13- Tension rotating shaft, 14- Tension rubber roller, 15- Rotating brush, 16- Brush transmission Motor, 17-sprocket, 18-nozzle, 19-spray pipeline, 20-sludge pump.
具体实施方式Detailed ways
下面通过具体的实施例对本发明作进一步的详细描述,以下实施例可以使本专业技术人员更全面的理解本发明,但不以任何方式限制本发明。The present invention will be further described in detail below through specific examples. The following examples can make those skilled in the art understand the present invention more comprehensively, but do not limit the present invention in any way.
如图1和图2所示,本实施例公开了一种用于污水处理的泥水分离装置,包括池体,池体设置有进水管道1和出水总管7,进水管道1用于将需要进行泥水分离的污水输送至池体内部,出水总管7用于将处理后的污水排出池体。池体四周设置有溢流堰2,用于使进水管道1输送的污水均匀流动至池体内部。As shown in FIG. 1 and FIG. 2 , the present embodiment discloses a mud-water separation device for sewage treatment, including a pool body. The pool body is provided with a water inlet pipe 1 and a water outlet main pipe 7. The water inlet pipe 1 is used to The sewage separated from the mud and water is transported to the inside of the tank body, and the water outlet pipe 7 is used to discharge the treated sewage out of the tank body. An
池体内部设置有多个相同的旋转滤筒3,每个旋转滤筒3以其轴线竖向设置,多个旋转滤筒3在水平方向上同心圆均布。每个旋转滤筒3的筒身满布有透水孔,筒身外部包裹有滤布4,滤布4将透水孔全面覆盖。池体中的污水在穿过滤布4进入到旋转滤筒3内部的过程中完成泥水分离,污泥被隔离在旋转滤筒3外的滤布4上,污水则进入到旋转滤筒3内部。A plurality of identical
旋转滤筒3顶部敞口并位于池体内液面以上,旋转滤筒3顶部设置有加强筋板并通过加强筋板与池体上方的连座轴承连接。旋转滤筒3底部设置有缩口部分并通过旋转接头5与污水收集管6连接,进入旋转滤筒3内部的污水通过旋转接头5汇集到污水收集管6。污水收集管6连通于出水总管7,通过出水总管7将汇集的污水排出池体。The top of the
所有旋转滤筒3均由滤布4带动进行旋转,滤布4在每个旋转滤筒3外部通过两根固定的压紧胶辊8相互对压,实现滤布4对旋转滤筒3的包裹。多个旋转滤筒3之间的中心位置设置有中心筒10,中心筒10连接有滤筒传动电机9,中心筒10由滤筒传动电机9驱动进行连续旋转。整圈滤布4绕设在中心筒10外部并依次连续地绕过每个旋转滤筒3,滤布4通过中心筒10的旋转将动力传递至各个旋转滤筒3。All the
如图3和图4所示,整圈滤布4由滤布张紧系统提供张紧力,从而保证传动和过滤的效果。本实施例中,滤布张紧系统主要由张紧弹簧11、张紧摆臂12、张紧旋转轴13、张紧胶辊14构成。张紧弹簧11的一端固定于池体上方支架,另一端与张紧摆臂12的一端固定连接,张紧摆臂12的另一端通过张紧旋转轴13与张紧胶辊14连接。滤布4的张紧力由张紧弹簧11提供,通过张紧摆臂12产生力矩,并作用在张紧旋转轴13上,再通过张紧胶辊14将作用力传递到滤布4上,完成对滤布4的自动张紧。As shown in Figures 3 and 4, the entire circle of
如图5和图6所示,本发明的泥水分离装置还配置有滤布清洗系统,用于随时对滤布4进行清洗。本实施例中,滤布清洗系统由毛刷清洗装置以及喷淋装置构成,包括旋转毛刷15、毛刷传动电机16、链轮17、喷嘴18、喷淋管路19。若干旋转毛刷15设置在滤布4表面,对滤布4表面的污泥进行清扫,实现将污泥由滤布4剥离。旋转毛刷15顶部通过链轮17连接毛刷传动电机16,由毛刷传动电机16提供旋转动力,并在链轮17的传动作用下,使旋转毛刷15进行旋转,完成对滤布4表面污泥的清扫。一般地,旋转毛刷15设置在旋转滤筒3之间的滤布4路径上,两个旋转毛刷15可通过链轮17由一个毛刷传动电机16进行驱动。在旋转毛刷15的入口方位设置有多个纵向排布在喷淋管路19上的喷嘴18,通过在旋转毛刷15清扫滤布4之前预先喷淋,提高清扫效果。As shown in FIG. 5 and FIG. 6 , the mud-water separation device of the present invention is further equipped with a filter cloth cleaning system, which is used to clean the
通过滤布4分离出来的污泥落入池体底部,由池体底部设置的污泥泵20排出池体,剩余污泥进入污泥处理系统,其余回流污泥回流至生物反应池,至此完成泥水分离。The sludge separated by the
尽管上面结合附图对本发明的优选实施例进行了描述,但是本发明并不局限于上述的具体实施方式,上述的具体实施方式仅仅是示意性的,并不是限制性的,本领域的普通技术人员在本发明的启示下,在不脱离本发明宗旨和权利要求所保护的范围情况下,还可以作出很多形式的具体变换,这些均属于本发明的保护范围之内。Although the preferred embodiments of the present invention have been described above with reference to the accompanying drawings, the present invention is not limited to the above-mentioned specific embodiments. Under the inspiration of the present invention, without departing from the scope of the present invention and the protection scope of the claims, personnel can also make many specific transformations, which all fall within the protection scope of the present invention.
Claims (7)
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Address after: 300051 No. 239, Yingkou Road, Heping District, Tianjin Patentee after: Tianjin municipal engineering design and Research Institute Co.,Ltd. Address before: 300051 No. 239, Yingkou Road, Heping District, Tianjin Patentee before: TIANJIN MUNICIPAL ENGINEERING DESIGN & Research Institute |