CN111646571A - A Multi-Mode Operational Biochemical Wastewater Treatment for Winery - Google Patents

A Multi-Mode Operational Biochemical Wastewater Treatment for Winery Download PDF

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CN111646571A
CN111646571A CN201911358411.7A CN201911358411A CN111646571A CN 111646571 A CN111646571 A CN 111646571A CN 201911358411 A CN201911358411 A CN 201911358411A CN 111646571 A CN111646571 A CN 111646571A
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mode operation
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tank
sewage treatment
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黄洁文
杨洛
金林
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Xi'an Water And Animal Husbandry Environment Technology Co ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1263Sequencing batch reactors [SBR]
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/32Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters
    • C02F2103/325Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters from processes relating to the production of wine products
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/06Controlling or monitoring parameters in water treatment pH
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/22O2
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    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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Abstract

本发明提供一种针对葡萄酒厂的多模式运行生化污水处理,包括多模式运行生化池,调节导入池结构,上侧导管,下侧导管,底部电磁阀,多功能导流架结构,第一出风管,第一鼓风机,液碱加药装置,提升泵,第一组合弹性填料层,终端处理架结构,COD传感器和风量电磁阀,所述的调节导入池结构设置在多模式运行生化池的左侧;所述的多功能导流架结构安装在多模式运行生化池的内部。本发明纵向导流板插接在侧边插框的内侧,有利于在使用时方便对厌缺区和好氧区进行分隔,以便对厌缺区和好氧区呈半隔离状态,从而能够避免两个区域混合;开孔分别开设在纵向导流板上,有利于在使用时能够将两个区域接通,并保持液位一致。

Figure 201911358411

The invention provides a multi-mode operation biochemical sewage treatment for wineries, including a multi-mode operation biochemical tank, an adjustment introduction tank structure, an upper side duct, a lower side duct, a bottom solenoid valve, a multi-functional guide frame structure, a first outlet The air duct, the first blower, the liquid alkali dosing device, the lifting pump, the first combined elastic packing layer, the terminal processing frame structure, the COD sensor and the air volume solenoid valve, the adjustment introduction tank structure is set in the multi-mode operation biochemical tank. Left side; the multifunctional guide frame structure is installed inside the multi-mode operation biochemical pool. The longitudinal deflector of the present invention is inserted into the inner side of the side insert frame, which is beneficial to facilitate the separation of the anaerobic and aerobic areas during use, so that the anaerobic and aerobic areas are in a semi-isolated state, thereby avoiding The two areas are mixed; the openings are respectively opened on the longitudinal deflector, which is beneficial to connect the two areas during use and keep the liquid level consistent.

Figure 201911358411

Description

一种针对葡萄酒厂的多模式运行生化污水处理A Multi-Mode Operational Biochemical Wastewater Treatment for Winery

技术领域technical field

本发明属于有机物浓度范围的葡萄酒厂生产废水处理技术领域,尤其涉及一种针对葡萄酒厂的多模式运行生化污水处理。The invention belongs to the technical field of winery production wastewater treatment in the range of organic matter concentration, and particularly relates to a multi-mode operation biochemical wastewater treatment for wineries.

背景技术Background technique

葡萄酒厂因原料的原因,每年生产时期短,约为30天,其余时期排水均为生活污水。葡萄酒厂在生产季节,排水COD浓度 3000-25000mg/l,车间清洗时排水呈酸性,PH可低至3。生产期结束后,酒厂排水为生活污水,COD浓度为300-400mg/l。为节省污水处理站投资造价,一般酒厂污水处理站仅设置了生活污水处理站。生产期排放的高浓度有机废水储存在大容积调节池中,利用长达10个月的停产期(水量少,且全部为生活污水)期间,生活污水处理站不满负荷处理的现状,将调节池的高浓度有机废水慢慢处理。Due to the raw materials, the production period of the winery is short every year, about 30 days, and the drainage in the rest of the period is domestic sewage. During the production season of the winery, the COD concentration of the drainage is 3000-25000mg/l, the drainage is acidic when the workshop is cleaned, and the PH can be as low as 3. After the production period, the drainage of the winery is domestic sewage, and the COD concentration is 300-400mg/l. In order to save the investment cost of the sewage treatment station, generally only the domestic sewage treatment station is set up in the sewage treatment station of the winery. The high-concentration organic wastewater discharged during the production period is stored in a large-volume conditioning tank. During the 10-month shutdown period (the amount of water is small, and all of it is domestic sewage), the domestic sewage treatment station is not fully loaded. The high-concentration organic wastewater is slowly treated.

但是现有的生化污水处理还存在着不具备起到隔离功能,去污不方便,耗费电能大和不方便对COD浓度进行检测的问题。However, the existing biochemical sewage treatment still has the problems of not having the isolation function, inconvenient decontamination, large power consumption and inconvenient detection of COD concentration.

因此,发明一种针对葡萄酒厂的多模式运行生化污水处理显得非常必要。Therefore, it is very necessary to invent a multi-mode operation biochemical wastewater treatment for wineries.

发明内容SUMMARY OF THE INVENTION

为了解决上述技术问题,本发明提供一种针对葡萄酒厂的多模式运行生化污水处理,以解决现有的生化污水处理存在着不具备起到隔离功能,去污不方便,耗费电能大和不方便对COD浓度进行检测的问题。一种针对葡萄酒厂的多模式运行生化污水处理,包括多模式运行生化池,调节导入池结构,上侧导管,下侧导管,底部电磁阀,多功能导流架结构,第一出风管,第一鼓风机,液碱加药装置,提升泵,第一组合弹性填料层,终端处理架结构,COD传感器和风量电磁阀,所述的调节导入池结构设置在多模式运行生化池的左侧;所述的多功能导流架结构安装在多模式运行生化池的内部;所述的第一出风管分别螺钉安装在多模式运行生化池的内侧底部;所述的第一鼓风机与第一出风管管道连接;所述的液碱加药装置与多模式运行生化池管道连接;所述的提升泵螺栓安装在多模式运行生化池的右下侧;所述的第一组合弹性填料层分别螺钉安装在多模式运行生化池的内部左右两侧;所述的风量电磁阀分别安装在第一鼓风机与第一出风管连接的管道上;所述的多功能导流架结构包括侧边插框,纵向导流板,密封垫,开孔和顶部护盖,所述的侧边插框嵌入在多模式运行生化池内壁中间位置的左侧;所述的顶部护盖螺钉安装在纵向导流板的上侧。In order to solve the above-mentioned technical problems, the present invention provides a multi-mode operation biochemical sewage treatment for wineries, so as to solve the problem that the existing biochemical sewage treatment does not have the isolation function, is inconvenient for decontamination, consumes a large amount of electricity and is inconvenient to The problem of COD concentration detection. A multi-mode operation biochemical sewage treatment for wineries, including multi-mode operation biochemical tank, adjustment introduction tank structure, upper side duct, lower side duct, bottom solenoid valve, multi-functional guide frame structure, first air outlet pipe, The first blower, the liquid alkali dosing device, the lifting pump, the first combined elastic packing layer, the terminal processing frame structure, the COD sensor and the air volume solenoid valve, and the adjustment and introduction tank structure is arranged on the left side of the multi-mode operation biochemical tank; The multi-functional guide frame structure is installed inside the multi-mode operation biochemical pool; the first air outlet pipes are respectively screwed to the inner bottom of the multi-mode operation biochemical pool; the first blower and the first outlet are respectively screwed. The air pipe and pipeline are connected; the liquid alkali dosing device is connected with the pipeline of the multi-mode operation biochemical tank; the lifting pump bolt is installed on the lower right side of the multi-mode operation biochemical tank; the first combined elastic packing layer is respectively The screws are installed on the left and right sides of the interior of the multi-mode operation biochemical pool; the air volume solenoid valves are respectively installed on the pipes connecting the first blower and the first air outlet; the multifunctional guide frame structure includes side inserts. frame, longitudinal deflector, sealing gasket, opening and top cover, the side insert frame is embedded in the left side of the middle position of the inner wall of the multi-mode operation biochemical tank; the top cover screw is installed on the longitudinal deflector the upper side of the board.

优选的,所述的终端处理架结构包括第二生化池,支架,第二组合弹性填料层,出水管,第二出风管和第二鼓风机,所述的支架螺栓安装在第二生化池的下部四角处;所述的第二组合弹性填料层螺钉安装在第二生化池的内侧;所述的出水管插接在第二组合弹性填料层的上侧;所述的第二出风管螺钉安装在第二生化池的底部左右两侧;所述的第二鼓风机螺栓安装在第二生化池的上部左侧,同时与第二出风管管道连接;所述的第二生化池与提升泵的输出管管道连接。Preferably, the terminal treatment rack structure includes a second biochemical tank, a bracket, a second combined elastic packing layer, a water outlet, a second air outlet and a second blower, and the bracket bolts are installed on the second biochemical tank. The lower four corners; the second combined elastic packing layer screw is installed on the inner side of the second biochemical tank; the water outlet pipe is inserted on the upper side of the second combined elastic packing layer; the second air outlet pipe screw Installed on the left and right sides of the bottom of the second biochemical pool; the second blower bolt is installed on the upper left side of the second biochemical pool, and is connected with the second air outlet pipe at the same time; the second biochemical pool and the lift pump The output pipe is connected to the pipe.

优选的,所述的调节导入池结构包括调节池,酒庄污水导入管,矩形安装框,控制器和控制按钮,所述的调节池设置在多模式运行生化池的左侧;所述的酒庄污水导入管插接在调节池的左侧上部;所述的矩形安装框螺钉安装在调节池的前侧中间位置;所述的控制器嵌入在矩形安装框的内侧中间位置;所述的控制按钮嵌入在矩形安装框的前侧下部;所述的调节池上侧通过上侧导管与多模式运行生化池的左上侧接通;所述的调节池的下侧通过下侧导管与多模式运行生化池的左下侧接通。Preferably, the structure of the adjustment and introduction tank includes an adjustment tank, a winery sewage introduction pipe, a rectangular installation frame, a controller and a control button, and the adjustment tank is arranged on the left side of the multi-mode operation biochemical tank; the wine The sewage inlet pipe is inserted into the upper left side of the adjustment tank; the screws of the rectangular installation frame are installed in the middle position of the front side of the adjustment tank; the controller is embedded in the middle position of the inner side of the rectangular installation frame; the control The button is embedded in the lower part of the front side of the rectangular installation frame; the upper side of the adjustment tank is connected to the upper left side of the multi-mode operation biochemical tank through the upper side conduit; the lower side of the adjustment tank is connected to the multi-mode operation biochemical tank through the lower side catheter The lower left side of the pool is turned on.

优选的,所述的纵向导流板插接在侧边插框的内侧。Preferably, the longitudinal deflector is inserted into the inner side of the side frame.

优选的,所述的开孔分别开设在纵向导流板上。Preferably, the openings are respectively opened on the longitudinal guide plates.

优选的,所述的底部电磁阀螺纹连接在下侧导管的中间位置。Preferably, the bottom solenoid valve is threadedly connected to the middle position of the lower conduit.

优选的,所述的COD传感器螺钉安装在多模式运行生化池的内壁右下侧。Preferably, the COD sensor screw is installed on the lower right side of the inner wall of the multi-mode operation biochemical tank.

优选的,所述的密封垫胶接在纵向导流板的下部外侧。Preferably, the sealing gasket is glued on the outer side of the lower part of the longitudinal deflector.

优选的,所述的多模式运行生化池内设置有两个区域,所述的两个区域分别设置为厌缺区和好氧区。Preferably, the multi-mode operation biochemical tank is provided with two zones, and the two zones are respectively set as an anaerobic zone and an aerobic zone.

优选的,所述的控制器采用型号为FX2N-48系列的PLC,所述的 COD传感器采用型号为RMD-ISCOD的COD传感器,所述的底部电磁阀采用2W-160-15电磁阀,所述的房梁电磁阀采用VT307电磁阀,所述的提升泵采用型号为WQ15-20-2.2的水泵,所述的第一鼓风机和第二鼓风机分别采用罗茨鼓风机,所述的COD传感器和控制按钮分别与控制器的输入端电性连接,所述的底部电磁阀、第一鼓风机、提升泵、风量电磁阀和第二鼓风机与控制器的输出端电性连接。Preferably, the controller adopts a PLC with a model of FX2N-48 series, the COD sensor adopts a COD sensor with a model RMD-ISCOD, and the bottom solenoid valve adopts a 2W-160-15 solenoid valve. The house beam solenoid valve adopts VT307 solenoid valve, the lift pump adopts the water pump of model WQ15-20-2.2, the first blower and the second blower respectively adopt Roots blower, the COD sensor and control button They are respectively electrically connected with the input end of the controller, and the bottom solenoid valve, the first blower, the lift pump, the air volume solenoid valve and the second blower are electrically connected with the output end of the controller.

与现有技术相比,本发明的有益效果为:Compared with the prior art, the beneficial effects of the present invention are:

1.本发明中,所述的纵向导流板插接在侧边插框的内侧,有利于在使用时方便对厌缺区和好氧区进行分隔,以便对厌缺区和好氧区呈半隔离状态,从而能够避免两个区域混合。1. In the present invention, the longitudinal deflector is inserted into the inner side of the side frame, which is beneficial to facilitate the separation of the anaerobic zone and the aerobic zone during use, so that the anaerobic zone and the aerobic zone are separated. semi-isolated state, thus avoiding mixing of the two regions.

2.本发明中,所述的开孔分别开设在纵向导流板上,有利于在使用时能够将两个区域接通,并保持液位一致。2. In the present invention, the openings are respectively opened on the longitudinal guide plate, which is beneficial to connect the two areas during use and keep the liquid level consistent.

3.本发明中,所述的底部电磁阀螺纹连接在下侧导管的中间位置,有利于在酒厂停产时期,打开底部电磁阀调节池内的存水可自动流入到多模式运行生化池内对污水进行处理,以便省去提升污水时的电耗。3. In the present invention, the bottom solenoid valve is threadedly connected to the middle position of the lower conduit, which is beneficial to open the bottom solenoid valve to adjust the stored water in the pool during the shutdown period of the winery and automatically flow into the multi-mode operation biochemical pool for sewage treatment. treatment in order to save electricity consumption when lifting sewage.

4.本发明中,所述的COD传感器螺钉安装在多模式运行生化池的内壁右下侧,有利于在使用时方便对多模式运行生化池内的浓度进行检测。4. In the present invention, the COD sensor screw is installed on the lower right side of the inner wall of the multi-mode operation biochemical tank, which is conducive to convenient detection of the concentration in the multi-mode operation biochemical tank during use.

5.本发明中,所述的密封垫胶接在纵向导流板的下部外侧,有利于在使用时能够增加与侧边插框接触时的密封效果。5. In the present invention, the sealing gasket is glued on the outer side of the lower part of the longitudinal deflector, which is beneficial to increase the sealing effect when it is in contact with the side insert frame during use.

附图说明Description of drawings

图1是本发明的结构示意图。Figure 1 is a schematic structural diagram of the present invention.

图2是本发明的调节导入池结构的结构示意图。FIG. 2 is a schematic structural diagram of the structure of the regulation introduction pool of the present invention.

图3是本发明的多功能导流架结构的结构示意图。FIG. 3 is a schematic structural diagram of the multifunctional deflector structure of the present invention.

图4是本发明的终端处理架结构的结构示意图。FIG. 4 is a schematic structural diagram of a terminal processing rack structure of the present invention.

图5是本发明的电气接线的结构示意图。FIG. 5 is a schematic structural diagram of the electrical wiring of the present invention.

图中:In the picture:

1、多模式运行生化池;2、调节导入池结构;21、调节池;22、酒庄污水导入管;23、矩形安装框;24、控制器;25、控制按钮;3、上侧导管;4、下侧导管;5、底部电磁阀;6、多功能导流架结构; 61、侧边插框;62、纵向导流板;63、密封垫;64、开孔;65、顶部护盖;7、第一出风管;8、第一鼓风机;9、液碱加药装置;10、提升泵;11、第一组合弹性填料层;12、终端处理架结构;121、第二生化池;122、支架;123、第二组合弹性填料层;124、出水管;125、第二出风管;126、第二鼓风机;13、COD传感器;14、风量电磁阀。1. Multi-mode operation of the biochemical tank; 2. Adjust the structure of the introduction tank; 21. Adjust the tank; 22. The winery sewage introduction pipe; 23. Rectangular installation frame; 24. The controller; 4. Lower conduit; 5. Bottom solenoid valve; 6. Multifunctional guide frame structure; 61. Side insert frame; 62. Longitudinal guide plate; 63. Gasket; 64. Opening; 65. Top cover 7. The first air outlet pipe; 8. The first blower; 9. The liquid alkali dosing device; 10. The lifting pump; 11. The first combined elastic packing layer; 122, the bracket; 123, the second combined elastic packing layer; 124, the water outlet pipe; 125, the second air outlet pipe; 126, the second blower; 13, the COD sensor; 14, the air volume solenoid valve.

具体实施方式Detailed ways

以下结合附图对本发明做进一步描述:The present invention will be further described below in conjunction with the accompanying drawings:

实施例:Example:

如附图1和附图3所示As shown in Figure 1 and Figure 3

本发明提供一种针对葡萄酒厂的多模式运行生化污水处理,包括多模式运行生化池1,调节导入池结构2,上侧导管3,下侧导管4,底部电磁阀5,多功能导流架结构6,第一出风管7,第一鼓风机8,液碱加药装置9,提升泵10,第一组合弹性填料层11,终端处理架结构12,COD传感器13和风量电磁阀14,所述的调节导入池结构2 设置在多模式运行生化池1的左侧;所述的多功能导流架结构6安装在多模式运行生化池1的内部;所述的第一出风管7分别螺钉安装在多模式运行生化池1的内侧底部;所述的第一鼓风机8与第一出风管7管道连接;所述的液碱加药装置9与多模式运行生化池1管道连接;所述的提升泵10螺栓安装在多模式运行生化池1的右下侧;所述的第一组合弹性填料层11分别螺钉安装在多模式运行生化池1的内部左右两侧;所述的风量电磁阀14分别安装在第一鼓风机8与第一出风管7连接的管道上;所述的底部电磁阀5螺纹连接在下侧导管4的中间位置,在酒厂停产时期,打开底部电磁阀5调节池21内的存水可自动流入到多模式运行生化池1内对污水进行处理,以便省去提升污水时的电耗,所述的COD传感器13螺钉安装在多模式运行生化池 1的内壁右下侧,在使用时方便对多模式运行生化池1内的浓度进行检测;所述的多功能导流架结构6包括侧边插框61,纵向导流板62,密封垫63,开孔64和顶部护盖65,所述的侧边插框61嵌入在多模式运行生化池1内壁中间位置的左侧;所述的顶部护盖65螺钉安装在纵向导流板62的上侧;所述的纵向导流板62插接在侧边插框61 的内侧,在使用时方便对厌缺区和好氧区进行分隔,以便对厌缺区和好氧区呈半隔离状态,从而能够避免两个区域混合,所述的开孔64 分别开设在纵向导流板62上,在使用时能够将两个区域接通,并保持液位一致,所述的密封垫63胶接在纵向导流板62的下部外侧,在使用时能够增加与侧边插框61接触时的密封效果。The present invention provides a multi-mode operation biochemical sewage treatment for wineries, including a multi-mode operation biochemical tank 1, an adjustment introduction tank structure 2, an upper side conduit 3, a lower side conduit 4, a bottom solenoid valve 5, and a multifunctional guide frame Structure 6, first air outlet 7, first blower 8, liquid alkali dosing device 9, lift pump 10, first combined elastic packing layer 11, terminal processing rack structure 12, COD sensor 13 and air volume solenoid valve 14, all The described adjustment and introduction pool structure 2 is arranged on the left side of the multi-mode operation biochemical pool 1; the described multifunctional guide frame structure 6 is installed inside the multi-mode operation biochemical pool 1; the described first air outlet pipes 7 are respectively The screw is installed on the inner bottom of the multi-mode operation biochemical tank 1; the first blower 8 is connected with the first air outlet pipe 7; the liquid alkali dosing device 9 is connected with the multi-mode operation biochemical tank 1 pipeline; all The lift pump 10 is bolted to the lower right side of the multi-mode operation biochemical tank 1; the first combined elastic packing layer 11 is screwed to the left and right sides of the multi-mode operation biochemical tank 1; the air volume electromagnetic The valve 14 is installed on the pipeline that the first blower 8 is connected with the first air outlet pipe 7 respectively; the bottom solenoid valve 5 is threadedly connected to the middle position of the lower side conduit 4, and during the shutdown period of the winery, the bottom solenoid valve 5 is opened to adjust The stored water in the pool 21 can automatically flow into the multi-mode operation biochemical tank 1 for sewage treatment, so as to save the power consumption when lifting the sewage. The COD sensor 13 is screwed on the inner wall of the multi-mode operation biochemical tank 1. Right On the lower side, it is convenient to detect the concentration in the multi-mode operation biochemical tank 1 during use; the multi-functional guide frame structure 6 includes a side insert frame 61, a longitudinal guide plate 62, a sealing gasket 63, and an opening 64. and the top cover 65, the side insert frame 61 is embedded in the left side of the middle position of the inner wall of the multi-mode operation biochemical tank 1; the top cover 65 is screwed on the upper side of the longitudinal deflector 62; the The longitudinal deflector 62 is inserted into the inner side of the side insert frame 61, and it is convenient to separate the anaerobic area and the aerobic area during use, so as to semi-isolate the anaerobic area and the aerobic area, so as to avoid the two. The two regions are mixed, and the openings 64 are respectively opened on the longitudinal deflector 62, which can connect the two regions during use and keep the liquid level consistent, and the sealing gasket 63 is glued on the longitudinal deflector. The outer side of the lower part of the 62 can increase the sealing effect when it is in contact with the side insert frame 61 during use.

如附图4所示,上述实施例中,具体的,所述的终端处理架结构 12包括第二生化池121,支架122,第二组合弹性填料层123,出水管124,第二出风管125和第二鼓风机126,所述的支架122螺栓安装在第二生化池121的下部四角处;所述的第二组合弹性填料层123 螺钉安装在第二生化池121的内侧;所述的出水管124插接在第二组合弹性填料层123的上侧;所述的第二出风管125螺钉安装在第二生化池121的底部左右两侧;所述的第二鼓风机126螺栓安装在第二生化池121的上部左侧,同时与第二出风管125管道连接;所述的第二生化池121与提升泵10的输出管管道连接。As shown in FIG. 4 , in the above embodiment, the terminal processing rack structure 12 specifically includes a second biochemical tank 121 , a bracket 122 , a second combined elastic packing layer 123 , a water outlet pipe 124 , and a second air outlet pipe 125 and the second blower 126, the brackets 122 are bolted to the lower four corners of the second biochemical pool 121; the screws of the second combined elastic packing layer 123 are installed on the inner side of the second biochemical pool 121; The water pipe 124 is plugged on the upper side of the second combined elastic packing layer 123; the second air outlet pipe 125 is screwed on the left and right sides of the bottom of the second biochemical pool 121; the second blower 126 is bolted on the first The upper left side of the second biochemical tank 121 is simultaneously connected to the second air outlet pipe 125; the second biochemical tank 121 is connected to the output pipe of the lift pump 10.

如附图2所示,上述实施例中,具体的,所述的调节导入池结构 2包括调节池21,酒庄污水导入管22,矩形安装框23,控制器24和控制按钮25,所述的调节池21设置在多模式运行生化池1的左侧;所述的酒庄污水导入管22插接在调节池21的左侧上部;所述的矩形安装框23螺钉安装在调节池21的前侧中间位置;所述的控制器24 嵌入在矩形安装框23的内侧中间位置;所述的控制按钮25嵌入在矩形安装框23的前侧下部;所述的调节池21上侧通过上侧导管3与多模式运行生化池1的左上侧接通;所述的调节池21的下侧通过下侧导管4与多模式运行生化池1的左下侧接通。As shown in FIG. 2 , in the above-mentioned embodiment, specifically, the adjustment introduction tank structure 2 includes an adjustment tank 21 , a winery sewage introduction pipe 22 , a rectangular installation frame 23 , a controller 24 and a control button 25 . The adjustment tank 21 is arranged on the left side of the multi-mode operation biochemical tank 1; the winery sewage inlet pipe 22 is inserted into the upper left side of the adjustment tank 21; the rectangular mounting frame 23 is screwed on the adjustment tank 21. The middle position of the front side; the controller 24 is embedded in the inner middle position of the rectangular installation frame 23; the control button 25 is embedded in the lower part of the front side of the rectangular installation frame 23; the upper side of the adjustment pool 21 passes through the upper side The conduit 3 is connected to the upper left side of the multi-mode operation biochemical tank 1; the lower side of the regulating tank 21 is connected to the lower left side of the multi-mode operation biochemical tank 1 through the lower side conduit 4.

工作原理working principle

本发明在工作过程中,将污水从酒庄污水导入管22内注入到调节池21内,当污水水位较高时经过上侧导管3进入到多模式运行生化池1内,同时经过第一组合弹性填料层11进行处理,接着经过提升泵10将水液经过导管进入到第二生化池121内,同时利用第二组合弹性填料层123对水液进行二次处理,最后从出水管124向外排出,厌缺区和好氧区的需要不同利用纵向导流板62进行分隔,同时可使液体镜柜开通相互流通,保证运行时两个区域不受干扰,在酒厂停产时期,接着利用控制器24控制底部电磁阀5打开,将调节池21内的水液倒入到多模式运行生化池1内进行处理,同时将第一鼓风机8和液碱加药装置9打开,以便利用第一鼓风机8将气体经过管道从第一出风管7内注入到多模式运行生化池1内,同时利用液碱加药装置9 经过管道将料物导入到多模式运行生化池1内,并把提升泵10关闭,控制好溶解氧和PH值,生化池处于闷曝状态,测定出水的COD浓度和PH值,待COD浓度和PH值符合SBR一体化污水处理设备进一种针对葡萄酒厂的多模式运行生化污水处理要求时,方可启动提升泵10。During the working process of the present invention, the sewage is injected into the adjustment tank 21 from the winery sewage introduction pipe 22, and when the sewage water level is high, it enters the multi-mode operation biochemical tank 1 through the upper conduit 3, and at the same time passes through the first combination. The elastic packing layer 11 is processed, and then the water liquid enters the second biochemical tank 121 through the conduit through the lift pump 10, and at the same time, the second combined elastic packing layer 123 is used for secondary treatment of the water liquid, and finally the water is discharged from the water outlet pipe 124. Discharge, the needs of the deficient area and the aerobic area are different, and the longitudinal deflector 62 is used to separate them. At the same time, the liquid mirror cabinet can be opened to communicate with each other, so as to ensure that the two areas are not disturbed during operation. During the shutdown period of the winery, use the control The device 24 controls the bottom solenoid valve 5 to open, pours the water in the adjustment tank 21 into the multi-mode operation biochemical tank 1 for processing, and simultaneously opens the first blower 8 and the liquid alkali dosing device 9, so as to use the first blower 8. The gas is injected into the multi-mode operation biochemical tank 1 from the first air outlet pipe 7 through the pipeline, and the liquid alkali dosing device 9 is used to introduce the material into the multi-mode operation biochemical tank 1 through the pipeline, and the lift pump is used. 10 Turn off, control the dissolved oxygen and PH value, the biochemical tank is in a stuffy aeration state, measure the COD concentration and PH value of the effluent, wait for the COD concentration and PH value to meet the SBR integrated sewage treatment equipment and enter a multi-mode operation for wineries The lift pump 10 can be started only when required for biochemical sewage treatment.

利用本发明所述的技术方案,或本领域的技术人员在本发明技术方案的启发下,设计出类似的技术方案,而达到上述技术效果的,均是落入本发明的保护范围。Using the technical solutions described in the present invention, or those skilled in the art design similar technical solutions under the inspiration of the technical solutions of the present invention, and achieve the above technical effects, all fall within the protection scope of the present invention.

Claims (9)

1. The utility model provides a biochemical sewage treatment of multi-mode operation to grape wine factory, characterized in that, this biochemical sewage treatment of multi-mode operation to grape wine factory, including multi-mode operation biochemical pond (1), adjust leading-in pond structure (2), upside pipe (3), downside pipe (4), bottom solenoid valve (5), multi-functional water conservancy diversion frame structure (6), first tuber pipe (7), first air-blower (8), liquid caustic soda charge device (9), elevator pump (10), first combination elastic packing layer (11), terminal processing frame structure (12), COD sensor (13) and air volume solenoid valve (14), adjust leading-in pond structure (2) and set up the left side in multi-mode operation biochemical pond (1); the multifunctional flow guide frame structure (6) is arranged inside the multi-mode operation biochemical pool (1); the first air outlet pipes (7) are respectively installed at the bottom of the inner side of the multi-mode operation biochemical pool (1) through screws; the first air blower (8) is connected with the first air outlet pipe (7) through a pipeline; the liquid caustic soda dosing device (9) is connected with the multi-mode operation biochemical pool (1) through a pipeline; the lifting pump (10) is installed on the right lower side of the multi-mode operation biochemical pool (1) through bolts; the first combined elastic packing layer (11) is respectively installed at the left side and the right side inside the multi-mode operation biochemical pool (1) by screws; the air volume electromagnetic valves (14) are respectively arranged on a pipeline connecting the first air blower (8) and the first air outlet pipe (7); the multifunctional flow guide frame structure (6) comprises a side edge inserting frame (61), a longitudinal flow guide plate (62), a sealing gasket (63), an opening (64) and a top protecting cover (65), wherein the side edge inserting frame (61) is embedded in the left side of the middle position of the inner wall of the multi-mode operation biochemical pool (1); the top protecting cover (65) is installed on the upper side of the longitudinal flow guide plate (62) in a screw mode.
2. The biochemical sewage treatment aiming at the winery with multi-mode operation according to claim 1, wherein the terminal processing frame structure (12) comprises a second biochemical pool (121), a bracket (122), a second combined elastic packing layer (123), a water outlet pipe (124), a second air outlet pipe (125) and a second air blower (126), wherein the bracket (122) is installed at the lower four corners of the second biochemical pool (121) by bolts; the second combined elastic filler layer (123) is arranged on the inner side of the second biochemical pool (121) by screws; the water outlet pipe (124) is inserted at the upper side of the second combined elastic packing layer (123); the second air outlet pipe (125) is arranged at the left side and the right side of the bottom of the second biochemical pool (121) by screws; the second air blower (126) is mounted on the left side of the upper part of the second biochemical pool (121) through bolts and is connected with a second air outlet pipe (125) through a pipeline; the second biochemical pool (121) is connected with an output pipe pipeline of the lift pump (10).
3. The multi-mode operation biochemical sewage treatment for wineries of claim 1, wherein the adjusting and introducing tank structure (2) comprises an adjusting tank (21), a winery sewage introducing pipe (22), a rectangular mounting frame (23), a controller (24) and a control button (25), the adjusting tank (21) is arranged at the left side of the multi-mode operation biochemical tank (1); the chateau sewage leading-in pipe (22) is inserted at the upper part of the left side of the adjusting tank (21); the rectangular mounting frame (23) is mounted in the middle of the front side of the regulating tank (21) through screws; the controller (24) is embedded in the middle position of the inner side of the rectangular mounting frame (23); the control button (25) is embedded in the lower part of the front side of the rectangular mounting frame (23); the upper side of the adjusting tank (21) is communicated with the upper left side of the multi-mode operation biochemical tank (1) through an upper side conduit (3); the lower side of the regulating tank (21) is communicated with the left lower side of the multi-mode operation biochemical tank (1) through a lower side conduit (4).
4. The biochemical sewage treatment system for wineries operating in multiple modes according to claim 1, wherein the longitudinal baffles (62) are inserted inside the side insertion frames (61).
5. Biochemical sewage treatment plant with multimode operation according to claim 1, characterized in that said openings (64) are respectively made in a longitudinal deflector (62).
6. Biochemical sewage treatment plant operating in multiple modes for wineries according to claim 1, characterized by the fact that the bottom solenoid valve (5) is screwed in the middle of the lower duct (4).
7. The multi-mode operation biochemical sewage treatment for wineries of claim 1, characterized in that the COD sensor (13) is installed on the right lower side of the inner wall of the multi-mode operation biochemical pool (1) by screws.
8. Biochemical sewage treatment plant directed to the multimode operation of the winery according to claim 1, characterized in that said gasket (63) is glued to the lower outer side of the longitudinal deflector (62).
9. The biochemical sewage treatment aiming at the wine factory with multi-mode operation according to the claim 1, characterized in that two areas are arranged in the biochemical pond (1) with multi-mode operation, and the two areas are respectively arranged as an anaerobic area and an aerobic area.
CN201911358411.7A 2019-12-25 2019-12-25 A Multi-Mode Operational Biochemical Wastewater Treatment for Winery Pending CN111646571A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103992004A (en) * 2014-04-23 2014-08-20 北京城市排水集团有限责任公司 Rural sewage advanced treatment and biochemical filtration integration device and running method thereof
CN206970299U (en) * 2017-07-19 2018-02-06 天津工业大学 A kind of digital control sequencing batch activated sludge reactor of novel visual
CN110563140A (en) * 2019-08-27 2019-12-13 中南大学 Wastewater treatment system based on adjustable A/O reactor and high-load wastewater treatment method
CN212476263U (en) * 2019-12-25 2021-02-05 西安水牧环境科技有限公司 A Multi-Mode Operational Biochemical Wastewater Treatment for Winery

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103992004A (en) * 2014-04-23 2014-08-20 北京城市排水集团有限责任公司 Rural sewage advanced treatment and biochemical filtration integration device and running method thereof
CN206970299U (en) * 2017-07-19 2018-02-06 天津工业大学 A kind of digital control sequencing batch activated sludge reactor of novel visual
CN110563140A (en) * 2019-08-27 2019-12-13 中南大学 Wastewater treatment system based on adjustable A/O reactor and high-load wastewater treatment method
CN212476263U (en) * 2019-12-25 2021-02-05 西安水牧环境科技有限公司 A Multi-Mode Operational Biochemical Wastewater Treatment for Winery

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