CN108706822A - Biological rotary cage integration pilot-plant - Google Patents
Biological rotary cage integration pilot-plant Download PDFInfo
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
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- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
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- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
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- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
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- C02F3/082—Rotating biological contactors
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Abstract
本发明涉及污水处理系统,具体为一种生物转笼一体化中试装置,包括连通污水水源的污水进水管、抽出污水的污水水泵、储存污水的调节池、净化污水的反应器、二沉池、连通二沉池的加药箱以及连通二沉池的污泥干化池;反应器包括进水泵、反应池、生物转笼、驱动生物转笼的驱动机构以及连通反应池的进水管与出水管,所述进水泵的进水口连通所述调节池的出水口,所述进水泵的出水口连通所述反应池的进水管,所述反应池的出水管连通所述二沉池;本发明提供一种使生物转笼中生物填料与污水接触并反应的一体化生物转笼装置。
The invention relates to a sewage treatment system, in particular to an integrated pilot plant with a biological cage, comprising a sewage inlet pipe connected to a sewage water source, a sewage water pump for pumping out sewage, a regulating tank for storing sewage, a reactor for purifying sewage, and a secondary settling tank , the dosing box connected to the secondary settling tank and the sludge drying tank connected to the secondary settling tank; the reactor includes the water inlet pump, the reaction tank, the biological cage, the driving mechanism for driving the biological cage, and the water inlet and outlet pipes connected to the reaction tank The water pipe, the water inlet of the water inlet pump is connected to the water outlet of the regulating tank, the water outlet of the water inlet pump is connected to the water inlet pipe of the reaction tank, and the water outlet pipe of the reaction tank is connected to the secondary sedimentation tank; the present invention Provided is an integrated biological cage device for contacting and reacting biological fillers in biological cages with sewage.
Description
技术领域technical field
本发明涉及污水处理系统,具体为一种生物转笼一体化中试装置。The invention relates to a sewage treatment system, in particular to an integrated pilot test device for biological cages.
背景技术Background technique
当前国内外处理污水的先进技术主要有生物法、化学法和物理法。在处理大量的工业排放污水或城市污水中,生物法是较多被采纳的方法。生物法的原理是利用微生物对有机物的分解,通过机械充氧来补充微生物呼吸和对有机物分解所需的氧。At present, the advanced technologies for sewage treatment at home and abroad mainly include biological methods, chemical methods and physical methods. In the treatment of a large amount of industrial sewage or urban sewage, the biological method is the most adopted method. The principle of the biological method is to use microorganisms to decompose organic matter, and supplement the oxygen required for microbial respiration and decomposition of organic matter through mechanical oxygenation.
现有技术中采用生物转笼净化污水,生物转笼中装有生物填料,生物填料表面的生物膜上的微生物有处理污水中污染物的作用。现有技术的问题是,生物填料在转动的过程中,逐渐堆叠在一处,导致生物填料没有充分与污水中的污染物接触。In the prior art, a biological tumbler is used to purify sewage. The biological tumbler is equipped with biological fillers, and the microorganisms on the biofilm on the surface of the biological fillers have the effect of treating pollutants in the sewage. The problem with the prior art is that the biological fillers are gradually piled up in one place during the rotation process, resulting in insufficient contact between the biological fillers and the pollutants in the sewage.
发明内容Contents of the invention
本发明提供一种使生物转笼中生物填料充分与污水接触并反应的装置。The invention provides a device for fully contacting and reacting biological filler in a biological rotating cage with sewage.
本发明提供基础方案是:生物转笼一体化中试装置,包括连通污水水源的污水进水管、抽出污水的污水水泵、储存污水的调节池、净化污水的生物转笼反应器、二沉池、连通二沉池的加药箱以及连通二沉池的污泥干化池;The basic solution provided by the present invention is: a biological tumbler integrated pilot test device, including a sewage inlet pipe connected to a sewage water source, a sewage water pump for pumping out sewage, a regulating tank for storing sewage, a biological tumbler reactor for purifying sewage, a secondary sedimentation tank, The dosing box connected to the secondary settling tank and the sludge drying tank connected to the secondary settling tank;
生物转笼反应器包括进水泵、反应池、生物转笼、驱动生物转笼的驱动机构以及连通反应池的进水管与出水管,进水泵的进水口连通调节池的出水口,进水泵的出水口连通反应池的进水管,反应池的出水管连通二沉池;The bio-rotating cage reactor includes a water inlet pump, a reaction tank, a biological rotating cage, a driving mechanism for driving the biological rotating cage, and a water inlet pipe and an outlet pipe connected to the reaction tank. The water port is connected to the water inlet pipe of the reaction tank, and the water outlet pipe of the reaction tank is connected to the secondary sedimentation tank;
反应池上端开口,驱动机构包括电机与传动组件,电机连接传动组件的输入端,传动组件的输出端传动连接生物转笼,生物转笼包括笼体、设置于笼体内的转轴、若干轴向分隔板、若干径向分隔板以及若干球形的生物填料,生物转笼分为弧状的侧壁与板状的两块侧板,侧壁与侧板上均开设有若干透水孔,轴向分隔板为方形板,轴向分隔板的内侧固定于转轴上,轴向分隔板的外侧固定于笼体侧壁的内壁上,轴向分隔板的两端分别与侧壁连接;径向分隔板为环形板,径向分隔板的内端连接于转轴上,径向分隔板的外端连接于侧壁的内壁上,径向分隔板沿着转轴轴向分布;轴向分隔板与径向分隔板将笼体内部分隔为若干个分隔室,生物填料放置于分隔室内;The upper end of the reaction tank is open, and the driving mechanism includes a motor and a transmission assembly. The motor is connected to the input end of the transmission assembly, and the output end of the transmission assembly is connected to the biological rotating cage. Partition boards, some radial partitions and some spherical biological fillers, the biological cage is divided into arc-shaped side walls and two plate-shaped side plates, and a number of permeable holes are opened on the side walls and side plates. The partition is a square plate, the inner side of the axial partition is fixed on the rotating shaft, the outer side of the axial partition is fixed on the inner wall of the side wall of the cage, and the two ends of the axial partition are respectively connected to the side wall; The radial partition is an annular plate, the inner end of the radial partition is connected to the rotating shaft, the outer end of the radial partition is connected to the inner wall of the side wall, and the radial partition is axially distributed along the rotating shaft; The interior of the cage is divided into several compartments by the partition plate and the radial partition plate, and the biological filler is placed in the compartment;
二沉池的底部设有连通污泥干化池的污泥排出管;The bottom of the secondary sedimentation tank is provided with a sludge discharge pipe connected to the sludge drying tank;
污泥干化池设有过滤层,过滤层的底部设有连通调节池的污水管。The sludge drying tank is provided with a filter layer, and the bottom of the filter layer is provided with a sewage pipe connected to the regulating tank.
原理:调节池均化污水水质与水量,由于流入该污水处理系统的污水并不总是均匀的,比如凌晨时分水量少、晚饭前后、做饭、洗漱等时间段用水量大,且水质参数变化也比较大,这就需要一个池子,把流入的水暂时存入其中,使其水质得到均化,减少对污水处理系统的冲击。生物转笼主要作用是通过生化反应去除污水中的污染物。为了加快生化反应,让培植有微生物的球形的生物填料显与污水接触,通过生物转笼的旋转,生物填料翻滚,使污水、空气和生物充分接触,为生化反应提供条件,利用微生物的生化反应,如硝化、反硝化等生化反应过程将污水中的污染物去除。轴向分隔板使生物填料上下翻滚,能脱离水面,径向分隔板阻止生物填料轴向滑动,使生物填料分布均匀。经过生物转笼处理的污水进入二沉池中,在二沉池中,污水静置使污泥沉降,并通过加药的方式促进污泥沉降。将这些污泥沉淀并去除,最后将达标的水排放。经过二沉池沉降并从底部排出的污泥,还含有大量的水。为了使其得到充分处理,同时减少污泥处置量,就需要污泥干化,将污泥中含有的污水分离出来,回流到调节池进行循环处理,仅留下干化后的污泥。Principle: The water quality and quantity of the homogenized sewage in the adjustment tank, because the sewage flowing into the sewage treatment system is not always uniform, for example, the water volume is small in the early morning, the water consumption is large during the time period before and after dinner, cooking, washing, etc., and the water quality parameters change It is also relatively large, which requires a pool to temporarily store the inflowing water in it to homogenize the water quality and reduce the impact on the sewage treatment system. The main function of the biological cage is to remove pollutants in sewage through biochemical reactions. In order to speed up the biochemical reaction, let the spherical biological filler with microorganisms be in contact with the sewage, through the rotation of the biological cage, the biological filler will roll, so that the sewage, air and organisms can fully contact, provide conditions for the biochemical reaction, and use the biochemical reaction of microorganisms , such as nitrification, denitrification and other biochemical reaction processes to remove pollutants in sewage. The axial partition plate makes the biological filler roll up and down, and can be separated from the water surface, and the radial partition plate prevents the biological filler from sliding in the axial direction, so that the biological filler is evenly distributed. The sewage treated by the biological cage enters the secondary sedimentation tank. In the secondary sedimentation tank, the sewage is allowed to stand still to settle the sludge, and the sedimentation of the sludge is promoted by adding medicine. These sludges are deposited and removed, and finally the qualified water is discharged. The sludge that has been settled in the secondary settling tank and discharged from the bottom also contains a large amount of water. In order to fully treat it and reduce the amount of sludge disposal, sludge drying is required to separate the sewage contained in the sludge and return it to the regulating tank for recycling treatment, leaving only the dried sludge.
与现有技术相比,本方案的优点在于:Compared with the prior art, the advantages of this solution are:
1.高效的处理污水,经过生物转笼、二沉池的处理后,便能有效处理污水中污染物。1. Efficient treatment of sewage. After the treatment of biological cages and secondary sedimentation tanks, pollutants in sewage can be effectively treated.
2.生物转笼内设置有轴向分隔板与径向分隔板,一方面使生物填料分布均匀,增大生物填料与污水的接触面积,另一方面也使得生物填料能脱离污水环境与空气接触,加快生化反应。2. There are axial partitions and radial partitions in the biological cage. On the one hand, the biological filler is evenly distributed, and the contact area between the biological filler and the sewage is increased. On the other hand, the biological filler can be separated from the sewage environment and Exposure to air accelerates biochemical reactions.
进一步,所述反应池内池底倾斜设置,所述反应池的最低处连通有排泥管,所述排泥管连接有电磁阀。有益效果:本设计方案中,考虑到生物转笼的旋转,生物转笼反应器槽体内沉淀性能较差,故将坡度提升到10%。设置底面坡度,一方面可使生物转笼具备基本的沉淀功能,减轻二沉池的负担;另一方面,由于底坡提供了聚集沉降污泥的空间,使得生物转笼反应器排泥周期大大延长,同时可以发挥污泥中厌氧细菌的厌氧消化功能,减少污泥总体的排放量。Further, the bottom of the reaction tank is inclined, and the lowest part of the reaction tank is connected with a sludge discharge pipe, and the sludge discharge pipe is connected with a solenoid valve. Beneficial effects: In this design scheme, considering the rotation of the biological cage, the sedimentation performance in the tank of the biological cage reactor is poor, so the slope is increased to 10%. Setting the bottom slope, on the one hand, can make the biological cage have the basic sedimentation function and reduce the burden on the secondary sedimentation tank; At the same time, it can exert the anaerobic digestion function of anaerobic bacteria in the sludge and reduce the overall discharge of sludge.
进一步,所述生物转笼内填充生物填料的填充率为68%-72%。有益效果:一方面,高比表面积填料的填充大大增加了生物转笼可供微生物附着的表面积;另一方面,该填充率使得生物转笼内的生物填料不会因为过多而被卡住无法翻动,而是随着生物转笼的运行在其中不断翻滚运动,处于流化状态。生物填料的流化状态不仅提高了空气与生物膜接触的效率,还通过生物填料之间的相互碰撞使老化的、粘附力差的生物膜脱落,从而进行了生物膜状态的“优胜劣汰”,提高生物填料上生物膜的活性。Further, the filling rate of the biological filler in the biological cage is 68%-72%. Beneficial effects: On the one hand, the filling of high specific surface area fillers greatly increases the surface area of the biological cage for microorganisms to attach; on the other hand, the filling rate prevents the biological filler in the biological cage from being stuck due to too much Turning, but with the running of the biological cage, it is constantly rolling in it, and it is in a fluidized state. The fluidized state of the biofiller not only improves the efficiency of the contact between the air and the biofilm, but also makes the aged and poorly adhered biofilm fall off through the collision between the biofillers, thus carrying out the "survival of the fittest" in the state of the biofilm. Increases the activity of biofilms on biomedia.
进一步,进水泵的出水口与反应池之间有调节管,调节管设有电子流量计与电动阀,生物转笼反应器设有回流分压件,回流分压件包括回流管与设置于回流管内的截至阀,回流管连通调节管,回流管连通调节池。有益效果:因为是中试装置,装置的处理能力有限,而进水泵最低的功率也超过了装置处理能力,此时开启截止阀与电动阀,电动阀限制进入调节管的流量,多余的流量通过截止阀进入回流管内,达到及时调整调节管内流量的效果。Further, there is a regulating pipe between the water outlet of the water inlet pump and the reaction tank, the regulating pipe is provided with an electronic flow meter and an electric valve, and the bio-cage reactor is provided with a return pressure divider, which includes a return pipe and a valve arranged in the return pipe. The cut-off valve, the return pipe is connected to the regulating pipe, and the return pipe is connected to the regulating pool. Beneficial effects: because it is a pilot plant, the processing capacity of the device is limited, and the lowest power of the water inlet pump exceeds the processing capacity of the device. At this time, the stop valve and the electric valve are opened, and the electric valve restricts the flow entering the regulating pipe, and the excess flow passes through The shut-off valve enters the return pipe to achieve the effect of adjusting the flow in the pipe in time.
进一步,所述调节池设有遮挡箱,所述进水泵的进水口设置于遮挡箱内,所述遮挡箱的侧壁设有溢流口,遮挡箱设置于调节池内上部。有益效果:使调节池内上层稍微清澈的水通过溢流口进入遮挡箱内,遮挡箱阻挡调节池中的污泥,避免进水泵吸入过多污泥而影响使用寿命。Further, the regulating tank is provided with a shielding box, the water inlet of the water inlet pump is set in the shielding box, the side wall of the shielding box is provided with an overflow port, and the shielding box is set in the upper part of the regulating pool. Beneficial effect: the slightly clear water in the upper layer of the regulating pool enters the shielding box through the overflow port, and the shielding box blocks the sludge in the regulating pond, so as to prevent the water inlet pump from sucking too much sludge and affecting the service life.
进一步,过滤层为石英砂滤层。有益效果:污泥干化池中间铺有石英砂等滤层,将二沉池流出的污泥经过石英砂滤层过滤,污水被过滤下去,污泥被拦截,从而实现泥水分离,污泥干化。Further, the filter layer is a quartz sand filter layer. Beneficial effects: the middle of the sludge drying tank is covered with a filter layer such as quartz sand, and the sludge flowing out of the secondary settling tank is filtered through the filter layer of quartz sand, the sewage is filtered, and the sludge is intercepted, thereby realizing the separation of mud and water, and the sludge is dried change.
进一步,反应池于出水管的上方设有防溢管。有益效果:当出水管不能将处理后的水及时排出时,反应池内过高的水位会影响到笼体内生物填料与空气的接触,因此设置防溢管在出水管出水速度不足时及时提升反应池的出水速度。Further, the reaction tank is provided with an overflow prevention pipe above the water outlet pipe. Beneficial effects: when the outlet pipe cannot discharge the treated water in time, the high water level in the reaction tank will affect the contact between the biological filler in the cage and the air, so the anti-overflow pipe is set to raise the reaction tank in time when the water outlet speed of the outlet pipe is insufficient water outlet speed.
进一步,所述调节池设置有污水取样机构,所述污水取样机构包括固定在调节池上方的基座、卷扬机、连接绳、定滑轮、取样管、滑套、安装于池底的取样阀以及连通取样阀的取样箱,所述连接绳一端连接卷扬机,连接绳的中部绕过定滑轮,所述连接绳的另一端连接取样管,所述取样管的外壁滑动连接于滑套的内壁,所述滑套固定连接于基座上,取样时,所述取样管下端伸入调节池中,所述取样管的下端为左低右高的倾斜状;所述取样阀包括左阀板与右阀板,所述左阀板与右阀板均通过扭簧枢接于调节池的池底,封闭状态时,左阀板设置于右阀板之上,所述左阀板与右阀板均由枢接点分为驱动端与从动端,打开状态时,取样管的下端向下推动驱动端,所述调节池的池底开设有供驱动端转动的转动槽与供取样水通过的连通孔,所述连通孔下端连通所述取样箱。Further, the regulating tank is provided with a sewage sampling mechanism, and the sewage sampling mechanism includes a base fixed above the regulating pond, a hoist, a connecting rope, a fixed pulley, a sampling pipe, a sliding sleeve, a sampling valve installed at the bottom of the pond, and a connecting The sampling box of the sampling valve, one end of the connecting rope is connected to the winch, the middle part of the connecting rope goes around the fixed pulley, the other end of the connecting rope is connected to the sampling tube, and the outer wall of the sampling tube is slidably connected to the inner wall of the sliding sleeve. The sliding sleeve is fixedly connected to the base. When sampling, the lower end of the sampling tube extends into the adjustment tank. The lower end of the sampling tube is inclined with the left lower and the right higher; the sampling valve includes a left valve plate and a right valve plate. , the left valve plate and the right valve plate are both pivotally connected to the bottom of the regulating pool through a torsion spring. The contact is divided into a driving end and a driven end. When it is opened, the lower end of the sampling tube pushes the driving end downward. The bottom of the adjustment pool is provided with a rotating groove for the driving end to rotate and a communication hole for the sampling water to pass through. The lower end of the communication hole communicates with the sampling box.
有益效果:检测水质时,需要在调节池中抽取污水并进行污染物的含量检测,但由于污水中物质太多,静置一段时间后污水会自行分层,单纯在一个高度或者一处抽取污水水样无法代表污水整体的情况。常规的思路是将调节池内污水混匀后采集污水水样,便能收集到混合均匀的污水。但由于调节池会收集大量污水静置,采用搅拌装置搅拌污水会消耗太多的能源,成本过高。本方案污水取样的流程,卷扬机转动,连接绳松动,取样管在自重的作用下下滑,取样管在滑套的限制下竖向滑动,取样管下端的左侧更低,首先推动左阀板的驱动端,而后取样管下端的右侧推动右阀板的驱动端,左阀板与右阀板都翘起,污水通过打开的取样阀进入连通孔中,然后通过连通孔进入取样箱中。进入取样箱中污水包含了竖向上各个高度上的污水,因此混合后能很接近池中所有水充分混合后的情况。污水在流入取样箱的过程中会进行一定程度的混合,当混合不充足时,可以在取样箱内设置小型的搅拌设备,因为只是少量搅拌,因此耗能较少。当取样管提起时,左阀板与右阀板各自在扭簧的作用下重新封闭连通孔。Beneficial effects: when testing water quality, it is necessary to extract sewage from the regulating pool and detect the content of pollutants. However, due to too many substances in the sewage, the sewage will stratify itself after standing for a period of time, and the sewage is simply extracted at one height or one place Water samples cannot represent the overall situation of sewage. The conventional idea is to mix the sewage in the regulating tank and then collect the sewage water samples, so that the uniformly mixed sewage can be collected. However, because the regulating tank will collect a large amount of sewage and leave it still, using a stirring device to stir the sewage will consume too much energy and the cost will be too high. In the sewage sampling process of this scheme, the winch rotates, the connecting rope is loose, the sampling pipe slides down under the action of its own weight, the sampling pipe slides vertically under the restriction of the sliding sleeve, the left side of the lower end of the sampling pipe is lower, and the left valve plate is first pushed Drive end, then the right side of the lower end of the sampling tube pushes the drive end of the right valve plate, the left valve plate and the right valve plate are tilted, the sewage enters the communication hole through the opened sampling valve, and then enters the sampling box through the communication hole. The sewage entering the sampling tank contains sewage at all vertical heights, so after mixing it can be very close to the situation after all the water in the pool is fully mixed. When the sewage flows into the sampling box, it will be mixed to a certain extent. When the mixing is not sufficient, a small stirring device can be installed in the sampling box, because it is only a small amount of stirring, so the energy consumption is less. When the sampling tube was lifted, the left valve plate and the right valve plate respectively re-closed the communicating hole under the action of the torsion spring.
附图说明Description of drawings
图1为本发明生物转笼一体化中试装置实施例的结构示意图。Fig. 1 is a structural schematic diagram of an embodiment of an integrated pilot plant for biological cages of the present invention.
图2为图1中生物转笼反应器的结构示意图。Fig. 2 is a schematic structural diagram of the bio-cage reactor in Fig. 1 .
图3为图2中生物转笼的侧视图。Fig. 3 is a side view of the biological cage in Fig. 2 .
图4为调节池中污水取样机构的结构示意图。Fig. 4 is a structural schematic diagram of the sewage sampling mechanism in the regulating tank.
图5为图4中局部放大图。FIG. 5 is a partially enlarged view in FIG. 4 .
图6为图5的状态示意图。FIG. 6 is a schematic diagram of the state of FIG. 5 .
具体实施方式Detailed ways
下面通过具体实施方式进一步详细的说明:Further detailed explanation through specific implementation mode below:
说明书附图中的附图标记包括:污水进水管1、污水水泵2、调节池3、遮挡箱310、溢流口311、进水泵312、电动阀313、电子流量计314、回流管315、截至阀316、生物转笼反应器4、笼体41、转轴412、径向分隔板413、轴向分隔板414、侧壁415、侧板416、分隔室418、池底419、排泥管420、电磁阀421、反应池430、进水管431、出水管432、防溢管433、二沉池5、加药箱6、污泥干化池7、卷扬机91、连接绳92、取样管93、滑套94、取样箱95、左阀板961、右阀板962、连通孔97。The reference signs in the drawings of the specification include: sewage inlet pipe 1, sewage water pump 2, regulating tank 3, shielding box 310, overflow port 311, water inlet pump 312, electric valve 313, electronic flowmeter 314, return pipe 315, stop Valve 316, biological cage reactor 4, cage body 41, rotating shaft 412, radial partition plate 413, axial partition plate 414, side wall 415, side plate 416, compartment 418, pool bottom 419, sludge discharge pipe 420, solenoid valve 421, reaction tank 430, water inlet pipe 431, water outlet pipe 432, overflow prevention pipe 433, secondary settling tank 5, dosing tank 6, sludge drying tank 7, hoist 91, connecting rope 92, sampling pipe 93 , sliding sleeve 94, sampling box 95, left valve plate 961, right valve plate 962, communication hole 97.
实施例基本如附图1所示:Embodiment is shown in Figure 1 basically:
生物转笼一体化中试装置,包括连通污水水源的污水进水管1、抽出污水的污水水泵2、储存污水的调节池3、净化污水的生物转笼反应器4、二沉池5、连通二沉池5的加药箱6以及连通二沉池5的污泥干化池7。Biological cage integrated pilot test device, including sewage inlet pipe 1 connected to sewage water source, sewage water pump 2 for pumping sewage, regulating tank for storing sewage 3, biological cage reactor for purifying sewage 4, secondary settling tank 5, connecting two The dosing box 6 of the sedimentation tank 5 and the sludge drying tank 7 connected to the secondary sedimentation tank 5 .
生物转笼反应器4,生物转笼反应器4包括进水泵312、反应池430、生物转笼、驱动生物转笼的驱动机构以及连通反应池430的进水管431与出水管432,进水泵312的进水口连通调节池3的出水口,进水泵312的出水口连通反应池430的进水管431,反应池430的出水管432连通二沉池5。The bio-rotating cage reactor 4, the bio-rotating cage reactor 4 comprises an inlet pump 312, a reaction tank 430, a biological rotating cage, a driving mechanism for driving the biological rotating cage, and an inlet pipe 431 and an outlet pipe 432 connected to the reaction tank 430, and an inlet pump 312 The water inlet of the pump is connected to the water outlet of the regulating tank 3, the water outlet of the water inlet pump 312 is connected to the water inlet pipe 431 of the reaction tank 430, and the water outlet pipe 432 of the reaction tank 430 is connected to the secondary sedimentation tank 5.
进水泵312的出水口与反应池430之间有调节管,调节管设有电子流量计314与电动阀313,生物转笼反应器4设有回流分压件,回流分压件包括回流管315与设置于回流管315内的截至阀316,回流管315连通调节管,回流管315连通调节池3。调节池3设有遮挡箱310,进水泵312的进水口设置于遮挡箱310内,遮挡箱310的侧壁415设有溢流口311,遮挡箱310设置于调节池3内上部。There is a regulating pipe between the water outlet of the water inlet pump 312 and the reaction tank 430, and the regulating pipe is provided with an electronic flow meter 314 and an electric valve 313. The return pipe 315 communicates with the adjustment pipe with the stop valve 316 arranged in the return pipe 315 , and the return pipe 315 communicates with the adjustment pool 3 . The adjustment pool 3 is provided with a shielding box 310, the water inlet of the water inlet pump 312 is arranged in the shielding box 310, the side wall 415 of the shielding box 310 is provided with an overflow port 311, and the shielding box 310 is arranged on the upper part of the regulating pool 3.
如图2与图3所示,反应池430上端开口,反应池430内池底419倾斜设置,坡度为10%。反应池430的最低处连通有排泥管420,排泥管420连接有电磁阀421。驱动机构包括电机与皮带轮传动组件,电机连接传动组件的输入端,传动组件的输出端传动连接生物转笼,生物转笼包括笼体41、设置于笼体41内的转轴412、8块轴向分隔板414、4块径向分隔板413以及若干球形的生物填料,生物转笼分为弧状的侧壁415与板状的两块侧板416,侧壁415与侧板416上均开设有若干透水孔,轴向分隔板414为方形板,轴向分隔板414的内侧固定于转轴412上,轴向分隔板414的外侧固定于笼体41侧壁415的内壁上,轴向分隔板414的两端分别与侧壁415连接;径向分隔板413为环形板,径向分隔板413的内端连接于转轴412上,径向分隔板413的外端连接于侧壁415的内壁上,径向分隔板413沿着转轴412轴向分布;轴向分隔板414与径向分隔板413将笼体41内部分隔为若干个分隔室418,生物填料放置于分隔室418内;径向分隔板413与轴向分隔板414上均开设有透水孔,生物转笼内填充生物填料的填充率为70%。As shown in FIG. 2 and FIG. 3 , the upper end of the reaction tank 430 is open, and the bottom 419 of the reaction tank 430 is inclined with a slope of 10%. The lowest part of the reaction pool 430 is connected with a mud discharge pipe 420 , and the mud discharge pipe 420 is connected with a solenoid valve 421 . The driving mechanism includes a motor and a pulley transmission assembly, the motor is connected to the input end of the transmission assembly, and the output end of the transmission assembly is connected to the biological rotating cage. The biological rotating cage includes a cage body 41, a rotating shaft 412 arranged in the cage body 41, and 8 axial Partition plate 414, four radial partition plates 413 and some spherical biological fillers, the biological cage is divided into arc-shaped side walls 415 and two plate-shaped side plates 416, and side walls 415 and side plates 416 are provided with There are some permeable holes, the axial partition plate 414 is a square plate, the inner side of the axial partition plate 414 is fixed on the rotating shaft 412, and the outer side of the axial partition plate 414 is fixed on the inner wall of the cage body 41 side wall 415, the shaft The two ends of the partition plate 414 are respectively connected with the side walls 415; the radial partition plate 413 is an annular plate, the inner end of the radial partition plate 413 is connected to the rotating shaft 412, and the outer end of the radial partition plate 413 is connected to On the inner wall of the side wall 415, the radial partition plate 413 is axially distributed along the rotating shaft 412; the axial partition plate 414 and the radial partition plate 413 divide the interior of the cage body 41 into several compartments 418, and the biological filler Placed in the compartment 418; the radial partition plate 413 and the axial partition plate 414 are provided with permeable holes, and the filling rate of the biological filler in the biological cage is 70%.
如图1所示,加药箱6内装有混凝剂,混凝剂为聚丙烯酰胺或聚合氯化铝,加药箱6设有加药计量泵,加药计量泵的出口连通二沉池5的进口;加药箱6中设有隔离计量泵As shown in Figure 1, the dosing box 6 is equipped with a coagulant, the coagulant is polyacrylamide or polyaluminum chloride, the dosing box 6 is provided with a dosing metering pump, and the outlet of the dosing metering pump is connected to the secondary sedimentation tank 5 inlets; the dosing box 6 is provided with an isolated metering pump
二沉池5的底部设有连通污泥干化池7的污泥排出管;The bottom of the secondary settling tank 5 is provided with a sludge discharge pipe connected to the sludge drying tank 7;
污泥干化池7设有过滤层,过滤层的底部设有连通调节池3的污水管。过滤层为石英砂滤层。The sludge drying tank 7 is provided with a filter layer, and the bottom of the filter layer is provided with a sewage pipe connected to the regulating tank 3 . The filter layer is a quartz sand filter layer.
调节池3内设有污水取样机构,污水取样机构包括固定在调节池3上方的基座、卷扬机91、连接绳92、定滑轮、取样管93、滑套94、安装于池底419的取样阀以及连通取样阀的取样箱95,连接绳92一端连接卷扬机91,连接绳92的中部绕过定滑轮,连接绳92的另一端连接取样管93,取样管93的外壁滑动连接于滑套94的内壁,滑套94固定连接于基座上,取样时,取样管93下端伸入调节池3中,取样管93的下端为左低右高的倾斜状;取样阀包括左阀板961与右阀板962,左阀板961与右阀板962均通过扭簧枢接于调节池3的池底419,封闭状态时,左阀板961设置于右阀板962之上,左阀板961与右阀板962均由枢接点分为驱动端与从动端,打开状态时,取样管93的下端向下推动驱动端,调节池3的池底419开设有供驱动端转动的转动槽与供取样水通过的连通孔97,连通孔97下端连通取样箱95。There is a sewage sampling mechanism in the regulating tank 3, and the sewage sampling mechanism includes a base fixed on the top of the regulating pond 3, a hoist 91, a connecting rope 92, a fixed pulley, a sampling pipe 93, a sliding sleeve 94, and a sampling valve installed at the bottom of the pond 419 And the sampling box 95 that communicates with the sampling valve, one end of the connecting rope 92 is connected to the winch 91, the middle part of the connecting rope 92 is bypassed by the fixed pulley, the other end of the connecting rope 92 is connected to the sampling tube 93, and the outer wall of the sampling tube 93 is slidably connected to the sliding sleeve 94. The inner wall and the sliding sleeve 94 are fixedly connected to the base. When sampling, the lower end of the sampling tube 93 is inserted into the adjustment pool 3. The lower end of the sampling tube 93 is inclined to the left and the right is high; the sampling valve includes a left valve plate 961 and a right valve plate. Plate 962, left valve plate 961 and right valve plate 962 are all pivotally connected to the pool bottom 419 of regulating pool 3 by torsion springs. The valve plate 962 is divided into a driving end and a driven end by a pivot point. When it is opened, the lower end of the sampling pipe 93 pushes the driving end downward, and the bottom 419 of the adjustment pool 3 is provided with a rotation groove for the driving end to rotate and for sampling. The communication hole 97 through which water passes, and the lower end of the communication hole 97 communicates with the sampling box 95 .
实施过程,如图1所示,污水水泵2启动通过污水进水管1从污水河道中抽起污水,将污水注入调节池3中静置一段时间,污水水质均化,调节池3内水位上升,上层的水经过溢流口311流入遮挡箱310内。启动遮挡箱310内的进水泵312,污水经过电动阀313与电子流量计314流入生物转笼反应器4中,因为本方案为中试结构,还需要调节,因此污水处理量有限,当流入生物转笼反应器4中的污水流量太大时,开启截止阀,并调节电动阀313,多余的污水便会经过回流管315回流进入遮挡箱310内。In the implementation process, as shown in Figure 1, the sewage water pump 2 starts to pump sewage from the sewage channel through the sewage water inlet pipe 1, injects the sewage into the regulating tank 3 and stands for a period of time, the sewage water quality is homogenized, and the water level in the regulating pond 3 rises. The water in the upper layer flows into the shielding box 310 through the overflow port 311 . Start the water inlet pump 312 in the shielding box 310, and the sewage flows into the biological cage reactor 4 through the electric valve 313 and the electronic flow meter 314. Because this scheme is a pilot test structure, it needs to be adjusted, so the sewage treatment capacity is limited. When the sewage flow rate in the tumbler reactor 4 is too large, open the shut-off valve and adjust the electric valve 313, and the excess sewage will flow back into the shielding box 310 through the return pipe 315.
如图2所示,当污水进入生物转笼反应器4后,水经过进水管431进入反应池430内。电机启动,电机通过皮带传动组带动转轴412旋转,转轴412旋转带动生物转笼随之转动。与此同时污水从进水管431进入反应池430内,首先通过侧壁415与侧板416上的透水孔进入最左侧的分隔室418内,与分隔室418内球形的生物填料接触,于此同时通过生物转笼的旋转,如图3所示的轴向分隔板414不停带动生物填料旋转,使污水、空气和生物填料充分接触,为生物填料与污水中的污染物生化反应提供条件,利用微生物的生化反应,如硝化、反硝化等生化反应过程将污水中的污染物去除。在污水从左边的进水管431流向右边出水管432的过程中,污水会从侧壁415、侧板416、径向分隔板413以及轴向分隔板414上的透水孔相互流通,并在生物转笼旋转的过程中加速该过程。污水中的淤泥会有一部分沉淀在反应池430中,经过反应过的水大部分通过出水管432流出,当量积累太多,液面到达防溢管433位置时,防溢管433也会为了尽快将水排出,避免影响转轴412以上的隔离室中生物填料与空气的接触。同时在反应池430池底419沉降的淤泥会沿着池底419的坡度下滑至右侧的坡底,积累到一定量时,开启电磁阀421,将淤泥从排泥管420排出。As shown in FIG. 2 , when the sewage enters the bio-cage reactor 4 , the water enters the reaction tank 430 through the water inlet pipe 431 . The motor starts, and the motor drives the rotating shaft 412 to rotate through the belt transmission group, and the rotating shaft 412 rotates to drive the biological cage to rotate thereupon. At the same time, sewage enters the reaction tank 430 from the water inlet pipe 431, first enters the leftmost compartment 418 through the permeable holes on the side wall 415 and the side plate 416, and contacts with the spherical biological filler in the compartment 418. At the same time, through the rotation of the biological cage, the axial partition plate 414 shown in Figure 3 continuously drives the biological filler to rotate, so that the sewage, air and biological filler are fully contacted, providing conditions for the biochemical reaction between the biological filler and the pollutants in the sewage , using microbial biochemical reactions, such as nitrification, denitrification and other biochemical reaction processes to remove pollutants in sewage. During the process of sewage flowing from the left water inlet pipe 431 to the right water outlet pipe 432, the sewage will flow through the permeable holes on the side wall 415, the side plate 416, the radial partition plate 413 and the axial partition plate 414. This process is accelerated during the rotation of the biological tumbler. A part of the sludge in the sewage will be deposited in the reaction tank 430, and most of the reacted water will flow out through the outlet pipe 432. If the equivalent is accumulated too much, when the liquid level reaches the anti-overflow pipe 433, the anti-overflow pipe 433 will also prevent the overflow pipe 433 from overflowing as soon as possible. The water is drained to avoid contacting the biological filler with air in the isolation chamber above the rotating shaft 412 . Simultaneously, the silt settled at the bottom 419 of the reaction tank 430 will slide down to the bottom of the slope on the right side along the slope of the bottom 419 of the pond.
此时的污水中含有悬浮的污泥(微生物生长产生的污泥),需要将这些污泥沉淀并去除,才能将水达标排放。在二沉池5中,污水静置使污泥沉降,并通过加药的方式促进污泥沉降。二沉池5中沉降后的清水通过清水排水管排入河水之中,完成对污水的整个处理。At this time, the sewage contains suspended sludge (sludge produced by microbial growth), which needs to be precipitated and removed before the water can be discharged up to the standard. In the secondary settling tank 5, the sewage is allowed to stand still to settle the sludge, and the sedimentation of the sludge is promoted by adding medicine. The clear water after settling in the secondary settling tank 5 is discharged into the river water through the clear water drain pipe to complete the whole treatment of the sewage.
同时还需要将二沉池5中的污泥排出,经过二沉池5沉降并从底部排出的污泥,还含有大量的水。为了使其得到充分处理,同时减少污泥处置量,就需要污泥干化,污泥干化池7中间铺有石英砂等滤层,将二沉池5流出的污泥经过石英砂滤层过滤,污泥被拦截,将污泥中含有的污水分离出来,回流到调节池3进行循环处理,仅留下干化后的污泥。从而实现泥水分离,污泥干化。Simultaneously, the sludge in the secondary settling tank 5 needs to be discharged, and the sludge settled in the secondary settling tank 5 and discharged from the bottom also contains a large amount of water. In order to fully treat it and reduce the amount of sludge disposal, sludge drying is required. A filter layer such as quartz sand is laid in the middle of the sludge drying tank 7, and the sludge flowing out of the secondary sedimentation tank 5 is passed through the filter layer of quartz sand. Filtration, the sludge is intercepted, the sewage contained in the sludge is separated, and returned to the regulating tank 3 for circulation treatment, leaving only the dried sludge. Thereby realizing mud-water separation and sludge drying.
本方案污水取样的流程,如图4、图5与图6所示,卷扬机91转动,连接绳92松动,取样管93在自重的作用下下滑,取样管93在滑套94的限制下竖向滑动,取样管93的上端具有透气孔,取样管93下滑的过程中,取样管范围内的污水进入取样管93范围内,取样管93下端的左侧更低,首先推动左阀板961的驱动端,而后取样管93下端的右侧推动右阀板962的驱动端,左阀板961与右阀板962都翘起,污水通过打开的取样阀进入连通孔97中,然后通过连通孔97进入取样箱95中。进入取样箱95中污水包含了竖向上各个高度上的污水,因此混合后能很接近池中所有水充分混合后的情况。污水在流入取样箱95的过程中会进行一定程度的混合,当混合不充足时,可以在取样箱95内设置小型的搅拌设备,因为只是少量搅拌,因此耗能较少。当取样管93提起时,左阀板961与右阀板962各自在扭簧的作用下重新封闭连通孔97。The process of sewage sampling in this scheme, as shown in Fig. 4, Fig. 5 and Fig. 6, the winch 91 rotates, the connecting rope 92 becomes loose, the sampling pipe 93 slides under the action of its own weight, and the sampling pipe 93 is vertically vertical under the restriction of the sliding sleeve 94. Sliding, the upper end of the sampling pipe 93 has air holes. During the sliding process of the sampling pipe 93, the sewage in the scope of the sampling pipe enters the range of the sampling pipe 93, and the left side of the lower end of the sampling pipe 93 is lower. First, the driving of the left valve plate 961 is pushed end, and then the right side of the lower end of the sampling pipe 93 pushes the driving end of the right valve plate 962, the left valve plate 961 and the right valve plate 962 are tilted up, and the sewage enters the communication hole 97 through the opened sampling valve, and then enters through the communication hole 97. In the sampling box 95. The sewage entering the sampling box 95 includes sewage at all heights vertically, so after mixing, it can be very close to the situation after all the water in the pool is fully mixed. Sewage can be mixed to a certain extent when flowing into the sampling box 95. When the mixing is insufficient, a small-scale stirring device can be set in the sampling box 95, because it is only a small amount of stirring, so the energy consumption is less. When the sampling tube 93 is lifted, the left valve plate 961 and the right valve plate 962 respectively re-close the communication hole 97 under the action of the torsion spring.
以上所述的仅是本发明的实施例,方案中公知的具体结构及特性等常识在此未作过多描述,所属领域普通技术人员知晓申请日或者优先权日之前发明所属技术领域所有的普通技术知识,能够获知该领域中所有的现有技术,并且具有应用该日期之前常规实验手段的能力,所属领域普通技术人员可以在本申请给出的启示下,结合自身能力完善并实施本方案,一些典型的公知结构或者公知方法不应当成为所属领域普通技术人员实施本申请的障碍。应当指出,对于本领域的技术人员来说,在不脱离本发明结构的前提下,还可以作出若干变形和改进,这些也应该视为本发明的保护范围,这些都不会影响本发明实施的效果和专利的实用性。本申请要求的保护范围应当以其权利要求的内容为准,说明书中的具体实施方式等记载可以用于解释权利要求的内容。What is described above is only an embodiment of the present invention, and the common knowledge such as the specific structure and characteristics known in the scheme is not described too much here, and those of ordinary skill in the art know all the common knowledge in the technical field to which the invention belongs before the filing date or the priority date Technical knowledge, being able to know all the existing technologies in this field, and having the ability to apply conventional experimental methods before this date, those of ordinary skill in the art can improve and implement this plan based on their own abilities under the inspiration given by this application, Some typical known structures or known methods should not be obstacles for those of ordinary skill in the art to implement the present application. It should be pointed out that for those skilled in the art, under the premise of not departing from the structure of the present invention, several modifications and improvements can also be made, and these should also be regarded as the protection scope of the present invention, and these will not affect the implementation of the present invention. Effects and utility of patents. The scope of protection required by this application shall be based on the content of the claims, and the specific implementation methods and other records in the specification may be used to interpret the content of the claims.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109879475A (en) * | 2019-02-28 | 2019-06-14 | 重庆工商大学 | Dynamic adjustment type sewage working condition treatment method |
| CN110117073A (en) * | 2019-06-19 | 2019-08-13 | 吴万益 | The manufacturing method of rotating biological embedding contact sewage treatment equipment and reaction sphere |
| CN110980933A (en) * | 2019-12-18 | 2020-04-10 | 南京公诚节能新材料研究院有限公司 | Artificial aquatic plant for purifying water quality of river channel |
| CN111908595A (en) * | 2020-08-13 | 2020-11-10 | 重庆大学 | Composite double-rotation moving biological bed sewage treatment device and sewage treatment method |
| CN113731345A (en) * | 2021-08-26 | 2021-12-03 | 深圳市一正科技有限公司 | Supergravity reinforced continuous reaction device |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4562749A (en) * | 1980-04-02 | 1986-01-07 | Exxon Research And Engineering Co. | Sampler |
| CN1272464A (en) * | 1999-05-04 | 2000-11-08 | 武汉长航给排水环境节能设备成套工程公司 | Multifunctional high-effetive biological rotating cage |
| CN1310134A (en) * | 2000-02-25 | 2001-08-29 | 长沙也去欧环保设备成套工程有限公司 | Biological rotary cage complete equipment |
| CA2610599A1 (en) * | 2007-10-15 | 2009-04-15 | Seprotech Systems Incorporated | An integrated water processing technology |
| CN201653752U (en) * | 2010-01-23 | 2010-11-24 | 朱枫 | Sampling device for online measurement of water quality |
| CN103288214A (en) * | 2013-06-26 | 2013-09-11 | 四川大学 | Efficient denitrifying integrated biological drum and operating method thereof |
| CN203820541U (en) * | 2013-12-06 | 2014-09-10 | 湖南清之源环保科技有限公司 | Self-refluxing biological rotating cage equipment |
| CN205222949U (en) * | 2015-11-17 | 2016-05-11 | 林燕彬 | Domestic sewage treatment device |
| CN105967333A (en) * | 2016-07-01 | 2016-09-28 | 中国科学院生态环境研究中心 | Integrated equipment and method for treating town domestic sewage |
| CN207361996U (en) * | 2017-08-28 | 2018-05-15 | 无锡浩润环保科技有限公司 | A kind of combined bio rotating cylinder sewage disposal device |
-
2018
- 2018-05-29 CN CN201810533234.0A patent/CN108706822B/en active Active
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4562749A (en) * | 1980-04-02 | 1986-01-07 | Exxon Research And Engineering Co. | Sampler |
| CN1272464A (en) * | 1999-05-04 | 2000-11-08 | 武汉长航给排水环境节能设备成套工程公司 | Multifunctional high-effetive biological rotating cage |
| CN1310134A (en) * | 2000-02-25 | 2001-08-29 | 长沙也去欧环保设备成套工程有限公司 | Biological rotary cage complete equipment |
| CA2610599A1 (en) * | 2007-10-15 | 2009-04-15 | Seprotech Systems Incorporated | An integrated water processing technology |
| CN201653752U (en) * | 2010-01-23 | 2010-11-24 | 朱枫 | Sampling device for online measurement of water quality |
| CN103288214A (en) * | 2013-06-26 | 2013-09-11 | 四川大学 | Efficient denitrifying integrated biological drum and operating method thereof |
| CN203820541U (en) * | 2013-12-06 | 2014-09-10 | 湖南清之源环保科技有限公司 | Self-refluxing biological rotating cage equipment |
| CN205222949U (en) * | 2015-11-17 | 2016-05-11 | 林燕彬 | Domestic sewage treatment device |
| CN105967333A (en) * | 2016-07-01 | 2016-09-28 | 中国科学院生态环境研究中心 | Integrated equipment and method for treating town domestic sewage |
| CN207361996U (en) * | 2017-08-28 | 2018-05-15 | 无锡浩润环保科技有限公司 | A kind of combined bio rotating cylinder sewage disposal device |
Non-Patent Citations (1)
| Title |
|---|
| 王建辉等: "生物转盘与生物转笼处理榨菜废水效能对比 ", 《水处理技术》 * |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109879475A (en) * | 2019-02-28 | 2019-06-14 | 重庆工商大学 | Dynamic adjustment type sewage working condition treatment method |
| CN109879475B (en) * | 2019-02-28 | 2022-04-22 | 重庆工商大学 | Dynamic adjustment type sewage working condition treatment method |
| CN110117073A (en) * | 2019-06-19 | 2019-08-13 | 吴万益 | The manufacturing method of rotating biological embedding contact sewage treatment equipment and reaction sphere |
| CN110980933A (en) * | 2019-12-18 | 2020-04-10 | 南京公诚节能新材料研究院有限公司 | Artificial aquatic plant for purifying water quality of river channel |
| CN111908595A (en) * | 2020-08-13 | 2020-11-10 | 重庆大学 | Composite double-rotation moving biological bed sewage treatment device and sewage treatment method |
| CN111908595B (en) * | 2020-08-13 | 2021-09-21 | 重庆大学 | Combined type double-rotation mobile biological bed sewage treatment device and sewage treatment method |
| CN113731345A (en) * | 2021-08-26 | 2021-12-03 | 深圳市一正科技有限公司 | Supergravity reinforced continuous reaction device |
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