CN110217957A - A kind of inactivated sludge degradation equipment of Hydrodynamic Cavitation - Google Patents
A kind of inactivated sludge degradation equipment of Hydrodynamic Cavitation Download PDFInfo
- Publication number
- CN110217957A CN110217957A CN201910641010.6A CN201910641010A CN110217957A CN 110217957 A CN110217957 A CN 110217957A CN 201910641010 A CN201910641010 A CN 201910641010A CN 110217957 A CN110217957 A CN 110217957A
- Authority
- CN
- China
- Prior art keywords
- cavitation
- stator
- sludge
- shaft
- hydrodynamic cavitation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
- C02F11/04—Anaerobic treatment; Production of methane by such processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/06—Treatment of sludge; Devices therefor by oxidation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/18—Treatment of sludge; Devices therefor by thermal conditioning
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Water Supply & Treatment (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种通过水力空化降解失活污泥的环保装置,属于失活污泥降解技术领域。The invention relates to an environmental protection device for degrading inactivated sludge through hydraulic cavitation, and belongs to the technical field of inactivated sludge degradation.
背景技术Background technique
城市污水处理工艺仍在应用的有一级处理、二级处理、深度处理,但是应用最普遍的是以传统活性污泥法为核心的二级处理。活性污泥法主要是利用微生物对污水进行处理。将空气通入污水中,增加污水中氧气的含量,促进污泥中各种微生物的大量繁殖活动,有效的去除污泥中的大分子有机物。此外,还有对该方法的改进,如间歇式活性污泥法,在处理废水中的大量有机物具有很高的针对性,降低了污水中磷硫等元素的含量,因此普遍应用于化学、造纸等废水的处理中。Municipal sewage treatment processes are still being applied, including primary treatment, secondary treatment, and advanced treatment, but the most commonly used secondary treatment is the traditional activated sludge method as the core. The activated sludge process mainly uses microorganisms to treat sewage. The air is introduced into the sewage to increase the oxygen content in the sewage, promote the mass reproduction of various microorganisms in the sludge, and effectively remove the macromolecular organic matter in the sludge. In addition, there are improvements to this method, such as the batch activated sludge method, which is highly targeted in treating a large amount of organic matter in wastewater, and reduces the content of phosphorus, sulfur and other elements in sewage, so it is widely used in chemistry, papermaking, etc. Waiting for waste water treatment.
但是在活性污泥法中,微生物分解有机物对反应器要求较高,要保证微生物有良好的生存环境,保持反应器内较高的污泥浓度和良好的传质效果,需定期投加营养物质,这增加了运行费用。上述的污水处理方法尤其是活性污泥法会产生大量泥状物质,每座污水处理厂每天要排放含水率约99.2%的剩余污泥,其量可达数百乃至上万吨,这些数量巨大的污泥将成为未来急需处理的难题。而目前处理污泥的方法主要是卫生填埋、土地利用、焚烧和投海。但是这些方法在二次污染、大气污染控制、投资及运营成本等方面存在的问题限制了其实际应用。目前我国对城市污泥主要采用临时填埋的处置方式,既占用了大量土地,又对生态环境造成了破坏。污泥中含有大量的高分子有机物可以利用,因此急需一种高效,适应性强,易控制的污泥有机物降解装置。However, in the activated sludge process, microbial decomposition of organic matter has high requirements on the reactor. To ensure a good living environment for microorganisms, maintain a high sludge concentration and good mass transfer effect in the reactor, it is necessary to add nutrients regularly , which increases operating costs. The above-mentioned sewage treatment methods, especially the activated sludge process, will produce a large amount of muddy matter, and each sewage treatment plant will discharge excess sludge with a moisture content of about 99.2% every day, and the amount can reach hundreds or even tens of thousands of tons. These quantities are huge The sludge will become a problem that needs to be dealt with urgently in the future. The current methods of sludge treatment are mainly sanitary landfill, land use, incineration and throwing into the sea. However, the problems of these methods in terms of secondary pollution, air pollution control, investment and operating costs limit their practical application. At present, my country mainly adopts temporary landfill disposal method for urban sludge, which not only occupies a large amount of land, but also causes damage to the ecological environment. Sludge contains a large amount of polymer organic matter that can be used, so there is an urgent need for an efficient, adaptable, and easy-to-control sludge organic matter degradation device.
水力空化过程中,空化结构附近产生极高压高温的条件,水中的水分子和溶解的氧分子的原子之间的化学键会断裂,并形成具有强氧化性的羟自由基。所产生的大量高活性羟自由基·OH能够氧化污泥中的化学物质,极高温高压会使分子中的化学键断裂从而达到降解大分子有机物的目的。对空化现象中产生的高压、高温加以利用,以实现对化学、物理等过程的强化,达到降解污泥中大分子有机物的效果。如中国专利文献CN106745489A公开的一种通过由多孔孔板、文丘里管和空化喷嘴组成的空化装置实现高效污水处理功能。CN104556266A公开了一种强化水力空化处理装置,使流体空化后崩溃产生大量自由基,有效提高水力空化降解有机污染物的能力,以达到提高和强化空化处理废水效果的目的。In the process of hydrodynamic cavitation, the conditions of extremely high pressure and high temperature are generated near the cavitation structure, and the chemical bonds between the atoms of the water molecules and the dissolved oxygen molecules in the water are broken, and hydroxyl radicals with strong oxidative properties are formed. The large amount of highly active hydroxyl radicals OH produced can oxidize the chemical substances in the sludge, and the extremely high temperature and high pressure will break the chemical bonds in the molecules to achieve the purpose of degrading macromolecular organic matter. The high pressure and high temperature generated in the cavitation phenomenon are used to strengthen the chemical and physical processes and achieve the effect of degrading the macromolecular organic matter in the sludge. For example, the Chinese patent document CN106745489A discloses a cavitation device composed of a porous orifice plate, a venturi tube and a cavitation nozzle to realize efficient sewage treatment. CN104556266A discloses an enhanced hydraulic cavitation treatment device, which can cause the fluid to collapse after cavitation to generate a large number of free radicals, effectively improving the ability of hydraulic cavitation to degrade organic pollutants, so as to achieve the purpose of improving and strengthening the effect of cavitation treatment of wastewater.
但是目前市面上的水力空化污水处理装置基本采用文丘里管,空化喷嘴的结构实现空化的目的,上述结构均存在空化效率低、污水处理量小、处理效率低的问题,无法应用于实际污泥处理过程中。However, the current hydraulic cavitation sewage treatment devices on the market basically use Venturi tubes, and the structure of the cavitation nozzle achieves the purpose of cavitation. The above structures all have the problems of low cavitation efficiency, small sewage treatment volume, and low treatment efficiency, so they cannot be applied. in the actual sludge treatment process.
因此亟需一种适应性强,易控制,结构简单,效率高的水力空化装置实现失活污泥降解。Therefore, there is an urgent need for a hydraulic cavitation device with strong adaptability, easy control, simple structure and high efficiency to degrade inactivated sludge.
发明内容Contents of the invention
本发明针对失活污泥降解技术存在的不足,提出一种适应性强,易控制,结构简单,效率高的失活污泥降解水力空化装置。Aiming at the shortcomings of the inactivated sludge degradation technology, the invention proposes a hydraulic cavitation device for inactivated sludge degradation with strong adaptability, easy control, simple structure and high efficiency.
本发明的失活污泥降解水力空化装置,采用如下技术方案:The deactivated sludge degradation hydraulic cavitation device of the present invention adopts the following technical scheme:
该装置,包括定子和转轴,定子内部形成空化腔,定子上设置有进水管和出水管;转轴安装在定子中,转轴一端伸出定子,该伸出端与传动装置连接,转轴上设置有通过轴套隔开的两个轮盘,轮盘处于定子的空化腔中,两个轮盘的与空化腔内壁相对的一侧分布有空化孔洞,空化孔洞为盲孔。The device includes a stator and a rotating shaft. A cavitation cavity is formed inside the stator, and a water inlet pipe and a water outlet pipe are arranged on the stator; the rotating shaft is installed in the stator, and one end of the rotating shaft protrudes from the stator. The two discs separated by the shaft sleeve are located in the cavitation cavity of the stator, and cavitation holes are distributed on the side opposite to the inner wall of the cavitation cavity of the two discs, and the cavitation holes are blind holes.
所述定子下部两侧均设置有进水管,定子上部设置有出水管。Both sides of the lower part of the stator are provided with water inlet pipes, and the upper part of the stator is provided with water outlet pipes.
所述空化孔洞的外端面与定子的内壁之间的距离为4-8mm,保证空化现象的形成。The distance between the outer end surface of the cavitation hole and the inner wall of the stator is 4-8mm, which ensures the formation of cavitation phenomenon.
所述空化孔洞的直径与深度之比为2:5。The ratio of diameter to depth of the cavitation holes is 2:5.
所述空化孔洞的直径为20mm,深度为50mm。The cavitation hole has a diameter of 20mm and a depth of 50mm.
所述转轴的转速范围为1600r/min-3600r/min。The rotation speed range of the rotating shaft is 1600r/min-3600r/min.
所述进水管和出水管在定子上对角设置,以防短流。The water inlet pipe and the water outlet pipe are arranged diagonally on the stator to prevent short flow.
上述装置,用于处理含水率在99.2%左右的污泥,处理污泥与处理污水原理基本一致,可以实现水力空化。由电机带动转轴高速旋转,使转子上的空化孔洞与失活污泥作相对运动,从而引发空化现象。空化现象是指液体内部局部压力降低时,液体中形成气泡并溃灭的过程,当液体流经水力结构时,由于水力结构的限流作用(污泥含水量较高,约99.2%),流速急剧上升,压力下降,当压力降低到工作温度下液体饱和蒸气压时产生空化现象,在空化气泡破灭的瞬间其周围极小范围会产生高压高温,在高温高压条件下污泥中的水分子和溶解的氧分子的原子之间的化学键会断裂,并形成具有强氧化性的羟自由基,产生的大量高活性羟自由基·OH能够氧化污泥中的化学物质,极高温高压会使分子中的化学键断裂从而达到降解大分子有机物的目的,同时产生的热效应可以降低污泥的粘度,使之更加容易处理。The above-mentioned device is used for treating sludge with a water content of about 99.2%. The principle of treating sludge is basically the same as that of treating sewage, and can realize hydraulic cavitation. The motor drives the rotating shaft to rotate at a high speed, so that the cavitation holes on the rotor and the inactivated sludge move relative to each other, thereby causing cavitation. Cavitation phenomenon refers to the process of forming and collapsing bubbles in the liquid when the local pressure inside the liquid decreases. When the liquid flows through the hydraulic structure, due to the flow limiting effect of the hydraulic structure (the water content of the sludge is high, about 99.2%), The flow rate rises sharply and the pressure drops. When the pressure drops to the saturated vapor pressure of the liquid at the working temperature, cavitation occurs. When the cavitation bubbles burst, a very small area around it will generate high pressure and high temperature. Under high temperature and high pressure conditions, the sludge in the sludge The chemical bonds between the water molecules and the atoms of the dissolved oxygen molecules will break and form hydroxyl radicals with strong oxidative properties. The chemical bonds in the molecules are broken to achieve the purpose of degrading macromolecular organic matter, and the thermal effect generated can reduce the viscosity of the sludge and make it easier to handle.
一种污泥处理系统,包括上述水力空化装置,还包括格栅池、调水池、中和池、初沉池、IC反应器、水解酸化池、高温失活处理池、泥浆泵和处理水收集池;格栅池、调节池、中和池、初沉池、IC反应器(厌氧反应器)、水解酸化池、高温失活处理池、泥浆泵、所述水力空化装置和处理水收集池依次连接。污水自流进入格栅集水池,除去大颗粒固体物质并调节水量水质,自流进入调节池,均衡水质和水量,然后由污泥泵提升至中和池。在中和池中通过加入氢氧化钙对污水进行pH调节。调节后的污水进入初沉池通过添加絮凝剂去除悬浮物。污水经物化反应后由泥浆泵提升至IC反应器进行大量有机物的去除。之后废水进入水解酸化池进行反应去除大分子有机物和改善可生化性等,经高温灭活后由泥浆泵将污泥送入水力空化装置,对失活污泥进行降解,将大分子有机物进行分解,获得处理水,输送至处理水收集池。污泥含水量达99%,污泥颗粒为大粒径固体,空化装置对固体有机物处理,降解为小分子物质,获得较为浑浊的处理水。A sludge treatment system, including the above-mentioned hydraulic cavitation device, and also includes a grid tank, a water transfer tank, a neutralization tank, a primary sedimentation tank, an IC reactor, a hydrolytic acidification tank, a high-temperature inactivation treatment tank, a mud pump and treated water Collection tank; grid tank, regulating tank, neutralization tank, primary sedimentation tank, IC reactor (anaerobic reactor), hydrolytic acidification tank, high temperature inactivation treatment tank, mud pump, the hydraulic cavitation device and treated water The collection pools are connected sequentially. Sewage flows into the grid sump by itself, removes large particles of solid matter and adjusts the water quality and water quality, then flows into the adjustment tank by itself, balances the water quality and quantity, and then is lifted to the neutralization tank by the sludge pump. The pH of the sewage is adjusted by adding calcium hydroxide in the neutralization tank. The adjusted sewage enters the primary sedimentation tank to remove suspended solids by adding flocculants. After the physical and chemical reaction, the sewage is lifted by the mud pump to the IC reactor for the removal of a large amount of organic matter. After that, the wastewater enters the hydrolysis acidification tank to react to remove macromolecular organic matter and improve biodegradability. Decompose to obtain treated water, which is sent to the treated water collection tank. The water content of the sludge is up to 99%, and the sludge particles are large-size solids. The cavitation device treats solid organic matter and degrades it into small molecular substances to obtain relatively turbid treated water.
本发明具有以下特点:The present invention has the following characteristics:
1.采用水力空化装置降解失活污泥,处理量大,可连续作业,具有高效性。1. The hydraulic cavitation device is used to degrade the inactivated sludge, which has a large processing capacity, continuous operation and high efficiency.
2.采用双轮盘式空化的对称结构,运转时可以有效的平衡轴向力,使设备运行更加平稳,有效的增加了设备使用寿命。2. The symmetrical structure of double disc cavitation can effectively balance the axial force during operation, making the equipment run more smoothly and effectively increasing the service life of the equipment.
3.采用电能为能源,零排放,无污染,具有良好的环保性。3. Using electric energy as energy, zero emission, no pollution, and good environmental protection.
4.采用电机作为污泥处理系统的动力来源,不受环境因素的影响,可根据需求随用随开,具有很高的灵活性。4. The motor is used as the power source of the sludge treatment system, which is not affected by environmental factors and can be opened as needed, with high flexibility.
5.本发明工作状态为常压,污水处理系统可以安全稳定运行;本发明结构较为简单,清理及检修拆卸方便。5. The working state of the present invention is normal pressure, and the sewage treatment system can run safely and stably; the structure of the present invention is relatively simple, and it is convenient for cleaning, maintenance and disassembly.
7.本发明可大型化,只需改变转子、定子尺寸,保证定子与转子之间的间距,更换大功率变频电机便可以满足更大污泥处理量的需求。7. The present invention can be enlarged. It only needs to change the size of the rotor and stator, ensure the distance between the stator and the rotor, and replace the high-power frequency conversion motor to meet the demand for greater sludge treatment capacity.
附图说明Description of drawings
图1是本发明的水力空化装置结构示意图。Fig. 1 is a schematic structural view of the hydraulic cavitation device of the present invention.
图2是本发明的水力空化器中转盘结构图。Fig. 2 is a structural diagram of the rotating disk in the hydraulic cavitator of the present invention.
图3是本发明的失活污泥处理流程图。Fig. 3 is a flow chart of inactivated sludge treatment in the present invention.
图中:1.第一进水管,2.密封盖,3.密封装置,4.角接触球轴承,5.端盖,6.轴,7.出水管,8.定子,9.空化孔洞(盲孔),10.轮盘,11.轴套,12.螺栓,13.密封圈,14.楔键,15.端盖,16.密封圈,17.第二进水管,18.联轴器,19.变频电机。In the figure: 1. The first water inlet pipe, 2. Sealing cover, 3. Sealing device, 4. Angular contact ball bearing, 5. End cover, 6. Shaft, 7. Water outlet pipe, 8. Stator, 9. Cavitation hole (Blind hole), 10. Wheel disc, 11. Shaft sleeve, 12. Bolt, 13. Seal ring, 14. Wedge key, 15. End cover, 16. Seal ring, 17. Second water inlet pipe, 18. Coupling 19. Frequency conversion motor.
具体实施方式Detailed ways
如图1所示,本发明的失活污泥降解水力空化装置,包括定子8、轮盘10和转轴6。As shown in FIG. 1 , the deactivated sludge degradation hydraulic cavitation device of the present invention includes a stator 8 , a disc 10 and a rotating shaft 6 .
定子8内部为密闭的空化腔。为便于加工,至少定子6的一端为通过螺栓12连接的端盖15,连接处设置有密封垫圈13。定子8的两端分别设置有轴承壳2,轴承壳2内安装有角接触球轴承4,轴承壳2上连接密封盖5,连接处设置有密封圈16,实现密封。定子8的下端两侧分别连接第一进水管1和第二进水管17,定子8的上端连接出水管7。为防止短流现象,进水管和出水管在定子8上最好对角设置,所以也可不用第二进水管17。Inside the stator 8 is a closed cavitation cavity. To facilitate processing, at least one end of the stator 6 is an end cover 15 connected by bolts 12, and a sealing washer 13 is provided at the connection. The two ends of the stator 8 are respectively provided with bearing shells 2, and angular contact ball bearings 4 are installed in the bearing shells 2. The bearing shell 2 is connected with a sealing cover 5, and a sealing ring 16 is arranged at the connection to realize sealing. Both sides of the lower end of the stator 8 are respectively connected to the first water inlet pipe 1 and the second water inlet pipe 17 , and the upper end of the stator 8 is connected to the water outlet pipe 7 . For preventing short flow phenomenon, water inlet pipe and water outlet pipe are preferably diagonally arranged on stator 8, so also can not need second water inlet pipe 17.
转轴6通过定子8两端的角接触球轴承4安装在定子8中,转轴6的一端伸出定子8上的端盖15,该伸出端通过联轴器18与电机19连接,电机19采用变频电机。电动机19带动转轴6转动。转轴6上在定子8两端的轴承壳2内均设置有密封装置3,可采用机械密封,以将污水隔离开,防止渗漏。The rotating shaft 6 is installed in the stator 8 through the angular contact ball bearings 4 at both ends of the stator 8. One end of the rotating shaft 6 protrudes from the end cover 15 on the stator 8. The extended end is connected with the motor 19 through the coupling 18. The motor 19 adopts frequency conversion motor. The motor 19 drives the rotating shaft 6 to rotate. The rotating shaft 6 is provided with a sealing device 3 in the bearing housing 2 at both ends of the stator 8, and a mechanical seal can be used to isolate the sewage and prevent leakage.
转轴6上设置有两个轮盘10,两个轮盘10之间通过设置轴套11固定。两个轮盘10均处于定子8的空化腔内,通过楔键14连接在转轴6上,使轮盘10与转轴6一起旋转。轮盘10的外侧面分布有空化孔洞9,空化孔洞9为盲孔,空化孔洞9的外端面与定子8的内壁之间的距离为4-8mm,保证空化现象的形成。轮盘10的转速为1600r/min-3600r/min,空化孔洞9的深度为50mm,直径为20mm,直径与深度比例为2:5。这些参数是根据失活污泥降解的特点经过大量实验获得的,达到了降解效率、效果和成本的最佳匹配。Two wheel discs 10 are arranged on the rotating shaft 6 , and the two wheel discs 10 are fixed by setting a shaft sleeve 11 . Both discs 10 are located in the cavitation cavity of the stator 8 and are connected to the rotating shaft 6 through wedge keys 14 so that the discs 10 and the rotating shaft 6 rotate together. Cavitation holes 9 are distributed on the outer surface of the wheel disc 10, and the cavitation holes 9 are blind holes. The distance between the outer end surface of the cavitation holes 9 and the inner wall of the stator 8 is 4-8mm, so as to ensure the formation of cavitation phenomenon. The rotating speed of the wheel disc 10 is 1600r/min-3600r/min, the depth of the cavitation hole 9 is 50mm, the diameter is 20mm, and the ratio of diameter to depth is 2:5. These parameters are obtained through a large number of experiments according to the characteristics of inactivated sludge degradation, and achieve the best match of degradation efficiency, effect and cost.
轮盘10外侧面上空化孔洞9的分布如图2所示,在转子10的外侧面均设置空化孔洞可以提高空化效率,提高污泥降解速率。The distribution of the cavitation holes 9 on the outer surface of the disc 10 is shown in FIG. 2 . Cavitation holes are provided on the outer surface of the rotor 10 to improve cavitation efficiency and sludge degradation rate.
定子8固定在地基上。轮盘10的材料是双相钢渗氮。将组装完成的轮盘10安装在转轴6上后,再将角接触轴承4安装在转轴6上,随后装配定子端盖15、机械密封3和密封盖。The stator 8 is fixed on the foundation. The material of the disc 10 is duplex steel nitrided. After the assembled wheel disc 10 is installed on the rotating shaft 6, the angular contact bearing 4 is installed on the rotating shaft 6, and then the stator end cover 15, the mechanical seal 3 and the sealing cover are assembled.
失活污泥由第一进水管1和第二进水管17进入定子8的空化腔中,转轴6带动轮盘10旋转,发生空化现象,实现降解失活污泥的作用,最后产生处理水由出水管7输出,进入处理水收集池。The inactivated sludge enters the cavitation cavity of the stator 8 through the first water inlet pipe 1 and the second water inlet pipe 17, and the rotating shaft 6 drives the wheel disc 10 to rotate, causing cavitation to degrade the inactivated sludge, and finally produce Water is output by outlet pipe 7 and enters the treated water collection tank.
如图3所示,应用本发明的失活污泥降解水力空化装置的污水处理系统,除了包括上述水力空化装置以外,还包括格栅池、调节池、中和池、初沉池、IC反应器、水解酸化池、高温失活处理池、泥浆泵、处理水收集池,各部分均为现有常规结构,水力调节、中和、水解酸化、高温失活处理等均为现有技术。格栅池、调水池、中和池、初沉池、IC反应器、水解酸化池、高温失活处理池、泥浆泵、水力空化装置和处理水收集池依次连接。As shown in Figure 3, the sewage treatment system using the deactivated sludge degrading hydraulic cavitation device of the present invention, in addition to including the above-mentioned hydraulic cavitation device, also includes a grid tank, a regulating tank, a neutralization tank, a primary sedimentation tank, IC reactor, hydrolytic acidification tank, high temperature deactivation treatment tank, mud pump, treated water collection tank, all parts are existing conventional structures, hydraulic adjustment, neutralization, hydrolysis acidification, high temperature deactivation treatment, etc. are all existing technologies . Grid pool, water transfer pool, neutralization pool, primary sedimentation tank, IC reactor, hydrolytic acidification pool, high temperature inactivation treatment pool, mud pump, hydraulic cavitation device and treated water collection pool are connected in sequence.
污泥自流进入格栅集水池,除去大颗粒固体物质并调节水量水质,自流进入调节池,均衡水质和水量,然后由污泥泵提升至中和池。在中和池中加入氢氧化钙对污泥进行pH调节。再进入初沉池,通过添加絮凝剂去除悬浮物。污泥经物化反应后由泵提升至IC反应器,通过厌氧反应进行大量有机物的去除。之后污泥进入水解酸化池进行反应去除大分子有机物和改善可生化性等,在高温失活处理池进行高温灭活,即在121°的高温下保持30分钟,对污泥中的微生物实现灭活处理,得到失活污泥。高温灭活后的失活污泥由泥浆泵将污泥送入水力空化装置,对失活污泥进行降解,将大分子有机物进行分解,获得处理水。处理水由水力空化器中导出,污泥经过水力空化器处理后,其内部的大分子有机物分解为小分子物质,实现失活污泥降解,内部颗粒粒度变小,得到较为浑浊的水-处理水。污泥含水量达99%,污泥颗粒为大粒径固体,空化装置对固体有机物处理,降解为小分子物质,获得较为浑浊的处理水。处理水再输送至处理水收集池。The sludge flows into the grid sump by itself, removes large particles of solid matter and adjusts the water quantity and quality, then flows into the adjustment tank by gravity, balances the water quality and quantity, and then is lifted to the neutralization tank by the sludge pump. Calcium hydroxide is added to the neutralization tank to adjust the pH of the sludge. Then enter the primary sedimentation tank, and remove the suspended solids by adding flocculant. After the sludge undergoes physical and chemical reactions, it is lifted by the pump to the IC reactor, and a large amount of organic matter is removed through anaerobic reaction. Afterwards, the sludge enters the hydrolysis acidification tank to react to remove macromolecular organic matter and improve biodegradability, etc., and perform high-temperature inactivation in the high-temperature inactivation treatment tank, that is, keep it at a high temperature of 121° for 30 minutes to achieve the elimination of microorganisms in the sludge. active treatment to obtain inactivated sludge. The inactivated sludge after high-temperature inactivation is sent to the hydraulic cavitation device by the mud pump to degrade the inactivated sludge, decompose the macromolecular organic matter, and obtain treated water. The treated water is exported from the hydraulic cavitator. After the sludge is treated by the hydraulic cavitator, the macromolecular organic matter inside it is decomposed into small molecular substances, and the deactivated sludge is degraded. The internal particle size becomes smaller, and relatively turbid water is obtained. - Treat water. The water content of the sludge is up to 99%, and the sludge particles are large-size solids. The cavitation device treats solid organic matter and degrades it into small molecular substances to obtain relatively turbid treated water. The treated water is sent to the treated water collection tank.
Claims (8)
- The equipment of Hydrodynamic Cavitation 1. a kind of inactivated sludge is degraded, it is characterized in that: including stator and shaft, stator interior forms cavitation Chamber is provided with water inlet pipe and outlet pipe on stator;Shaft is installed in the stator, and stator, the extension end and biography are stretched out in shaft one end Dynamic device connects, and is provided with two wheel discs that axle sleeve separates in shaft, wheel disc is in the cavitation chamber of stator, two wheel discs The side opposite with cavitation cavity wall be distributed with cavitation hole, cavitation hole is blind hole.
- 2. inactivated sludge degradation equipment of Hydrodynamic Cavitation according to claim 1, it is characterized in that: stator lower part two sides are all provided with It is equipped with water inlet pipe, stator top is provided with outlet pipe.
- 3. inactivated sludge degradation equipment of Hydrodynamic Cavitation according to claim 1, it is characterized in that: the outer end face of the cavitation hole The distance between inner wall of stator is 4-8mm.
- 4. according to claim 1 inactivated sludge degrade equipment of Hydrodynamic Cavitation, it is characterized in that: the diameter of the cavitation hole with The ratio between depth is 2:5.
- 5. inactivated sludge degradation equipment of Hydrodynamic Cavitation according to claim 1, it is characterized in that: the diameter of the cavitation hole is 20mm, depth 50mm.
- 6. inactivated sludge degradation equipment of Hydrodynamic Cavitation according to claim 1, it is characterized in that: the range of speeds of the shaft is 1600r/min-3600r/min。
- 7. inactivated sludge degradation equipment of Hydrodynamic Cavitation according to claim 1, it is characterized in that: the water inlet pipe and outlet pipe exist Diagonally it is arranged on stator.
- 8. a kind of sewage disposal system, including the degradation equipment of Hydrodynamic Cavitation of inactivated sludge described in claim 1-8, further include grid Pond, water transfer pond, neutralization pond, primary sedimentation tank, IC reactor, hydrolysis acidification pool, high temperature deactivation processing pond, slush pump and processing water are collected Pond, it is grid pond, water transfer pond, neutralization pond, primary sedimentation tank, IC reactor, hydrolysis acidification pool, high temperature deactivation processing pond, slush pump, described Equipment of Hydrodynamic Cavitation and processing water collecting pit are sequentially connected.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910253863 | 2019-03-30 | ||
CN2019102538632 | 2019-03-30 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN110217957A true CN110217957A (en) | 2019-09-10 |
CN110217957B CN110217957B (en) | 2021-11-02 |
Family
ID=67813677
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910641010.6A Active CN110217957B (en) | 2019-03-30 | 2019-07-16 | A deactivated sludge degradation hydrodynamic cavitation device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN110217957B (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111453958A (en) * | 2020-04-27 | 2020-07-28 | 北京工业大学 | Cavitation-based excess sludge dewatering agent reduction and addition method |
CN111453957A (en) * | 2020-04-27 | 2020-07-28 | 北京工业大学 | A hydraulic cavitation pump device for excess sludge based on the principle of cavitation |
CN111807458A (en) * | 2020-07-31 | 2020-10-23 | 山东大学 | Antibiotic wastewater treatment device coupled with hydraulic cavitation, acoustic cavitation and photocatalysis |
CN111807499A (en) * | 2020-07-31 | 2020-10-23 | 山东大学 | Hydraulic cavitation and electrocatalysis integrated antibiotic wastewater degradation device |
CN113024060A (en) * | 2021-04-20 | 2021-06-25 | 辽宁大学 | Sludge treatment system based on hydrodynamic cavitation |
CN114057367A (en) * | 2021-11-18 | 2022-02-18 | 浙江大学 | A kind of hydraulic cavitation degrading sludge device and degrading sludge system |
CN115403236A (en) * | 2022-10-31 | 2022-11-29 | 湖南博世科环保科技有限公司 | Sludge cavitator and sludge breaking device and sludge reduction system applying same |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62213890A (en) * | 1986-03-14 | 1987-09-19 | Mitsutoshi Matsuoka | Apparatus for purifying and heating waste water |
JPS62213895A (en) * | 1986-03-14 | 1987-09-19 | Mitsutoshi Matsuoka | Apparatus for purifying and heating waste water |
CN101893225A (en) * | 2009-09-09 | 2010-11-24 | 千庸基 | Boiler using rotary force |
KR20120122442A (en) * | 2011-04-29 | 2012-11-07 | 이재형 | a multiplex heating producer which using centrifugal force and friction force |
CN106630372A (en) * | 2015-11-04 | 2017-05-10 | 东莞源控环保科技有限公司 | A system and method for denitrification treatment of urban sewage |
CN107176767A (en) * | 2017-07-20 | 2017-09-19 | 江苏理文造纸有限公司 | A kind of Novel anaerobic system depth handles waster water process |
CN108264186A (en) * | 2017-12-29 | 2018-07-10 | 乐山海天水务有限公司 | A kind of method recycled to nitric wastewater |
CN108264191A (en) * | 2017-12-12 | 2018-07-10 | 玖龙纸业(东莞)有限公司 | A kind of sewage water treatment method of chemical flocculation precipitation |
-
2019
- 2019-07-16 CN CN201910641010.6A patent/CN110217957B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62213890A (en) * | 1986-03-14 | 1987-09-19 | Mitsutoshi Matsuoka | Apparatus for purifying and heating waste water |
JPS62213895A (en) * | 1986-03-14 | 1987-09-19 | Mitsutoshi Matsuoka | Apparatus for purifying and heating waste water |
CN101893225A (en) * | 2009-09-09 | 2010-11-24 | 千庸基 | Boiler using rotary force |
KR20120122442A (en) * | 2011-04-29 | 2012-11-07 | 이재형 | a multiplex heating producer which using centrifugal force and friction force |
CN106630372A (en) * | 2015-11-04 | 2017-05-10 | 东莞源控环保科技有限公司 | A system and method for denitrification treatment of urban sewage |
CN107176767A (en) * | 2017-07-20 | 2017-09-19 | 江苏理文造纸有限公司 | A kind of Novel anaerobic system depth handles waster water process |
CN108264191A (en) * | 2017-12-12 | 2018-07-10 | 玖龙纸业(东莞)有限公司 | A kind of sewage water treatment method of chemical flocculation precipitation |
CN108264186A (en) * | 2017-12-29 | 2018-07-10 | 乐山海天水务有限公司 | A kind of method recycled to nitric wastewater |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111453958A (en) * | 2020-04-27 | 2020-07-28 | 北京工业大学 | Cavitation-based excess sludge dewatering agent reduction and addition method |
CN111453957A (en) * | 2020-04-27 | 2020-07-28 | 北京工业大学 | A hydraulic cavitation pump device for excess sludge based on the principle of cavitation |
CN111453957B (en) * | 2020-04-27 | 2022-03-08 | 北京工业大学 | Residual sludge hydrodynamic cavitation pump device based on cavitation principle |
CN111453958B (en) * | 2020-04-27 | 2022-03-08 | 北京工业大学 | Cavitation-based excess sludge dewatering agent reduction and addition method |
CN111807458A (en) * | 2020-07-31 | 2020-10-23 | 山东大学 | Antibiotic wastewater treatment device coupled with hydraulic cavitation, acoustic cavitation and photocatalysis |
CN111807499A (en) * | 2020-07-31 | 2020-10-23 | 山东大学 | Hydraulic cavitation and electrocatalysis integrated antibiotic wastewater degradation device |
CN111807458B (en) * | 2020-07-31 | 2022-06-21 | 山东大学 | Antibiotic wastewater treatment device coupled with hydraulic cavitation, acoustic cavitation and photocatalysis |
CN113024060A (en) * | 2021-04-20 | 2021-06-25 | 辽宁大学 | Sludge treatment system based on hydrodynamic cavitation |
CN114057367A (en) * | 2021-11-18 | 2022-02-18 | 浙江大学 | A kind of hydraulic cavitation degrading sludge device and degrading sludge system |
CN115403236A (en) * | 2022-10-31 | 2022-11-29 | 湖南博世科环保科技有限公司 | Sludge cavitator and sludge breaking device and sludge reduction system applying same |
CN115403236B (en) * | 2022-10-31 | 2023-02-03 | 湖南博世科环保科技有限公司 | Sludge cavitator and sludge breaking device and sludge reduction system applying same |
Also Published As
Publication number | Publication date |
---|---|
CN110217957B (en) | 2021-11-02 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110217957B (en) | A deactivated sludge degradation hydrodynamic cavitation device | |
CN104355476B (en) | A kind of technique for the overall process up to standard of oilfield drilling waste and device | |
CN109824175B (en) | Organic waste water supersound and hydrodynamic cavitation joint processing apparatus | |
CN109824176A (en) | A device for hydrodynamic cavitation combined with oxidant to degrade dye wastewater | |
CN109824216A (en) | A hydraulic cavitation treatment system for brewing wastewater | |
CN109824226A (en) | A kind of hydraulic cavitation for degrading oily sludge oil | |
CN102115291A (en) | Refractory high-concentration organic wastewater treatment process | |
CN113024060A (en) | Sludge treatment system based on hydrodynamic cavitation | |
CN109824137A (en) | A kind of hydraulic cavitation for domestic sewage treatment | |
CN113845257B (en) | A device and method for recycling drilling and completion waste liquid using ultrasonic technology | |
CN111807644A (en) | A combined hydraulic cavitation and biological method for the degradation of antibiotic wastewater | |
CN103819034B (en) | The system and method for ultrasonic combined light-Fenton oxidation renovation of organic pollution underground water | |
JP6271787B1 (en) | Sludge treatment system that produces biogas | |
CN111807497A (en) | A deep degradation device for antibiotic wastewater based on hydraulic cavitation | |
CN113045094A (en) | Physicochemical treatment system and treatment process for waste emulsion | |
CN216737989U (en) | Medical sewage treatment and sludge reduction system | |
JP6271691B1 (en) | Pressurized sludge solidification concentrator | |
CN109824217B (en) | Fenton's reagent of pesticide waste water and hydrodynamic cavitation combined treatment system | |
CN204958651U (en) | Oiliness chemical industry sewage treatment plant | |
CN113045160A (en) | Sludge treatment method for improving residual sludge methane yield through reflux of digestive fluid | |
CN103641284A (en) | Sludge breaking and centrifugal filtration integrated machine | |
CN203700075U (en) | Treatment system of restoration sewage of organic polluted soil | |
CN105948301A (en) | Integrated processing system and method for sewage sludge with high dryness | |
CN207811535U (en) | The sludge dehydration device that microwave and ozone are combined | |
CN111807458B (en) | Antibiotic wastewater treatment device coupled with hydraulic cavitation, acoustic cavitation and photocatalysis |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |