CN110171912A - A kind of circulation dredged industrial waste water disposal device - Google Patents
A kind of circulation dredged industrial waste water disposal device Download PDFInfo
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- 239000010842 industrial wastewater Substances 0.000 title claims abstract description 35
- 238000004062 sedimentation Methods 0.000 claims abstract description 52
- 238000006243 chemical reaction Methods 0.000 claims abstract description 34
- 238000001514 detection method Methods 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 claims abstract description 10
- 238000004065 wastewater treatment Methods 0.000 claims description 29
- 239000012752 auxiliary agent Substances 0.000 claims description 9
- 238000004659 sterilization and disinfection Methods 0.000 claims description 6
- 239000005708 Sodium hypochlorite Substances 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 3
- 238000002347 injection Methods 0.000 claims description 3
- 239000007924 injection Substances 0.000 claims description 3
- 238000012545 processing Methods 0.000 claims description 3
- 239000002893 slag Substances 0.000 claims description 3
- 239000010802 sludge Substances 0.000 claims description 3
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims description 3
- 238000012544 monitoring process Methods 0.000 claims description 2
- 238000012216 screening Methods 0.000 claims 1
- 239000002351 wastewater Substances 0.000 abstract description 14
- 239000010865 sewage Substances 0.000 abstract description 8
- 238000001179 sorption measurement Methods 0.000 abstract description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 6
- 239000002245 particle Substances 0.000 abstract description 5
- 230000003340 mental effect Effects 0.000 abstract 1
- 238000012797 qualification Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 238000011001 backwashing Methods 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/58—Treatment of water, waste water, or sewage by removing specified dissolved compounds
- C02F1/62—Heavy metal compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
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- 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
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- 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
- C02F2303/14—Maintenance of water treatment installations
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- 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
- C02F2303/16—Regeneration of sorbents, filters
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
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- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
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- Water Supply & Treatment (AREA)
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- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
技术领域technical field
本发明属于废水处理设备技术领域,尤其涉及循环疏通式工业废水处理装置。The invention belongs to the technical field of waste water treatment equipment, in particular to a circulation dredging type industrial waste water treatment device.
背景技术Background technique
目前,业内常用的现有技术是这样的:近几年我国经济发展迅速,带来大量的工业废水不能很好的处理,如果不经过正确的处理就排入自然环境会对大自然造成污染,进而导致更大的损失。目前的废水处理设备能耗大,处理工业废水的成本太高;目前的废水处理设备不够智能,效率太低,造成大量废水囤积或设备空转。At present, the existing technologies commonly used in the industry are as follows: my country's rapid economic development in recent years has brought a large amount of industrial wastewater that cannot be treated well. If it is discharged into the natural environment without proper treatment, it will cause pollution to nature. resulting in greater losses. The current wastewater treatment equipment consumes a lot of energy, and the cost of treating industrial wastewater is too high; the current wastewater treatment equipment is not smart enough, and the efficiency is too low, resulting in a large amount of wastewater hoarding or equipment idling.
综上所述,现有技术存在的问题是:In summary, the problems in the prior art are:
(1)目前的废水处理设备能耗大,处理工业废水的成本太高。(1) The current wastewater treatment equipment consumes a lot of energy, and the cost of treating industrial wastewater is too high.
(2)目前的废水处理设备不够智能,效率太低,造成大量废水囤积或设备空转。(2) The current wastewater treatment equipment is not smart enough and the efficiency is too low, resulting in a large amount of wastewater hoarding or equipment idling.
发明内容Contents of the invention
针对现有技术存在的问题,本发明提供了一种循环疏通式工业废水处理装置。Aiming at the problems existing in the prior art, the present invention provides a circulating dredging type industrial wastewater treatment device.
本发明是这样实现的,一种循环疏通式工业废水处理装置设置有:The present invention is achieved in that a kind of circulating dredging type industrial wastewater treatment device is provided with:
离心罐、开口、液位监测仪;Centrifuge tanks, openings, level monitors;
离心罐上开设有开口,离心罐内设置有液位监测仪;There is an opening on the centrifuge tank, and a liquid level monitor is installed in the centrifuge tank;
进一步,离心罐通过管道与第一沉淀池连接;Further, the centrifuge tank is connected with the first sedimentation tank through a pipeline;
进一步,第一沉淀池通过管道与反应池连接,将沉淀好的废水通入反应池中进行化学反应将废水中的重金属离子处理掉。Further, the first sedimentation tank is connected with the reaction tank through a pipeline, and the settled waste water is passed into the reaction tank for chemical reaction to remove the heavy metal ions in the waste water.
进一步,反应池通过管道与第二沉淀池双向连接;Further, the reaction tank is bidirectionally connected with the second sedimentation tank through pipelines;
进一步,反应池通过管道与检测池双向连接;Further, the reaction pool is bidirectionally connected to the detection pool through pipelines;
进一步,所述第一沉淀池与离心罐之间的连接管道内嵌装有粗格栅栏,反应池与第一沉淀池之间的连接管道内嵌装有细格栅栏,所述粗格栅栏和细格栅栏外侧设置有栅渣外运模块。Further, the connection pipeline between the first sedimentation tank and the centrifuge tank is embedded with a coarse grid fence, and the connection pipeline between the reaction tank and the first sedimentation tank is embedded with a fine grid fence. A grid slag transport module is arranged on the outside of the grid fence.
进一步,所述第一沉淀池为沉沙池,第二沉淀池内间隔有A2/O池和二沉池,A2/O池通过管道与鼓风机房连通,所述二沉池与A2/O池之间设置有污泥回流模块。Further, the first sedimentation tank is a grit chamber, and the second sedimentation tank is separated by an A2/O tank and a secondary sedimentation tank, and the A2/O tank is connected to the blower room through a pipeline, and there is a gap between the secondary sedimentation tank and the A2/O tank. A sludge return module is provided.
进一步,所述第二沉淀池连通有高效沉淀池,高效沉淀池与第二沉淀池之间设置有中间提升泵房,高效沉淀池上端开设有辅助剂添加口。Further, the second sedimentation tank is connected with a high-efficiency sedimentation tank, an intermediate lifting pump room is set between the high-efficiency sedimentation tank and the second sedimentation tank, and an auxiliary agent addition port is opened at the upper end of the high-efficiency sedimentation tank.
进一步,所述检测池与第二沉淀池之间还连通有反硝化深床滤池和消毒接触池,消毒接触池设置有次氯酸钠添加模块。Further, a denitrification deep bed filter and a disinfection contact tank are connected between the detection tank and the second sedimentation tank, and the disinfection contact tank is provided with a sodium hypochlorite adding module.
进一步,所述反硝化深床滤池连接有反冲洗模块,反冲洗模块用于对反硝化深床滤池进行冲洗清洁,使反硝化深床滤池在短时间内恢复过滤能力。Further, the denitrification deep-bed filter is connected with a backwash module, and the backwash module is used to flush and clean the denitrification deep-bed filter, so that the denitrification deep-bed filter can restore the filtering capacity in a short time.
本发明的另一目的在于提供一种用于循环疏通式工业废水处理装置的循环疏通式工业废水处理装置的控制系统,所述循环疏通式工业废水处理装置的控制系统包括:Another object of the present invention is to provide a control system for a circulating dredging industrial wastewater treatment device, the control system of the circulating dredging industrial wastewater treatment device includes:
中央控制模块,用于通过中央处理器对整体装置的运行进行智能控制;The central control module is used to intelligently control the operation of the overall device through the central processing unit;
检测模块,与中央控制模块连接,用于通过多个传感器对装置的运行参数进行实时监测;The detection module is connected with the central control module, and is used for real-time monitoring of the operating parameters of the device through multiple sensors;
驱动模块,与中央控制模块连接,用于接收控制指令对多个驱动组件进行运行控制;The drive module is connected with the central control module, and is used to receive control instructions to control the operation of multiple drive components;
辅助剂添加模块,与中央控制模块连接,用于通过注入装置向反应池内添加反应用辅助剂;The auxiliary agent adding module is connected with the central control module, and is used to add the auxiliary agent for reaction into the reaction pool through the injection device;
报警模块,与中央控制模块连接,用于在系统出现故障时发出报警提醒。The alarm module is connected with the central control module and is used for sending an alarm reminder when the system fails.
综上所述,本发明的优点和积极效果是:In summary, advantages and positive effects of the present invention are:
本发明通过离心罐能将通入的工业废水离心搅拌,通过开口加入活性炭吸附颗粒,通过离心搅拌对工业废水进行初步的吸附处理,液位监测仪能实时监测离心罐内废水的通入量,根据数据调节整套设备的运行做到节能。离心罐中初步吸附处理的废水通入第一沉淀池进行沉淀将吸附颗粒和吸附的杂质进行沉淀并过滤。进行化学处理后的废水理论上已经可以经过沉淀后排放,但是这样不够智能容易有残留,本发明将化学反应这一步骤进行循环处理污水。循环处理后的污水通入检测池中进行指标检测,检测不合格再次进入循环,合格就可排放,智能处理提高了污水处理效率。The invention can centrifugally stir the incoming industrial wastewater through the centrifuge tank, add activated carbon adsorption particles through the opening, and carry out preliminary adsorption treatment on the industrial wastewater through the centrifugal stirring. The liquid level monitor can monitor the amount of wastewater in the centrifuge tank in real time, Adjust the operation of the whole set of equipment according to the data to achieve energy saving. The wastewater from the preliminary adsorption treatment in the centrifuge tank is passed into the first sedimentation tank for sedimentation, and the adsorbed particles and adsorbed impurities are sedimented and filtered. Theoretically, the wastewater after chemical treatment can be discharged after sedimentation, but this is not smart enough and easy to have residues. The present invention will cycle the step of chemical reaction to treat wastewater. Sewage after recycling treatment is passed into the detection pool for index detection. If it fails to pass the test, it will enter the cycle again. If it is qualified, it can be discharged. Intelligent treatment improves the efficiency of sewage treatment.
附图说明Description of drawings
图1是本发明实施例提供的循环疏通式工业废水处理装置结构示意图。Fig. 1 is a schematic structural diagram of a circulating dredging industrial wastewater treatment device provided by an embodiment of the present invention.
图2是本发明实施例提供的开口结构示意图。Fig. 2 is a schematic diagram of an opening structure provided by an embodiment of the present invention.
图中:1、离心罐;2、开口;3、液位监测仪;4、第一沉淀池;5、反应池;6、检测池;7、第二沉淀池。In the figure: 1. Centrifugal tank; 2. Opening; 3. Liquid level monitor; 4. First sedimentation tank; 5. Reaction tank; 6. Detection tank; 7. Second sedimentation tank.
图3是本发明实施例提供的循环疏通式工业废水处理装置原理图。Fig. 3 is a schematic diagram of a circulating dredging industrial wastewater treatment device provided by an embodiment of the present invention.
图4是本发明实施例提供的循环疏通式工业废水处理装置的控制系统结构示意图。Fig. 4 is a schematic structural diagram of a control system of a circulation dredging industrial wastewater treatment device provided by an embodiment of the present invention.
具体实施方式Detailed ways
为能进一步了解本发明的发明内容、特点及功效,兹例举以下实施例,并配合附图详细说明如下。In order to further understand the content, features and effects of the present invention, the following examples are given, and detailed descriptions are given below with reference to the accompanying drawings.
下面结合附图对本发明的结构作详细的描述。The structure of the present invention will be described in detail below in conjunction with the accompanying drawings.
如图1至图3所示,本发明实施例提供的循环疏通式工业废水处理装置包括:离心罐1、开口2、液位监测仪3、第一沉淀池4、反应池5、检测池6、第二沉淀池7。As shown in Figures 1 to 3, the circulating dredging industrial wastewater treatment device provided by the embodiment of the present invention includes: a centrifugal tank 1, an opening 2, a liquid level monitor 3, a first sedimentation tank 4, a reaction tank 5, and a detection tank 6 , the second sedimentation tank 7.
离心罐1上开设有开口,离心罐1内设置有液位监测仪3,离心罐1通过管道与第一沉淀池4连接,第一沉淀池4通过管道与反应池5连接,反应池5通过管道与第二沉淀池7双向连接,反应池5通过管道与检测池6双向连接。There is an opening on the centrifuge tank 1, and a liquid level monitor 3 is arranged inside the centrifuge tank 1. The centrifuge tank 1 is connected to the first sedimentation tank 4 through a pipeline, the first sedimentation tank 4 is connected to the reaction tank 5 through a pipeline, and the reaction tank 5 passes through The pipeline is bidirectionally connected with the second sedimentation tank 7, and the reaction pool 5 is bidirectionally connected with the detection pool 6 through the pipeline.
作为优选,开口2上端通过铰轴连接有盖子,盖子另一端通过卡扣与离心罐连接。Preferably, the upper end of the opening 2 is connected with a cover through a hinge, and the other end of the cover is connected with the centrifuge tank through a buckle.
作为优选,第一沉淀池4与离心罐1之间的连接管道内嵌装有粗格栅栏,反应池与第一沉淀池之间的连接管道内嵌装有细格栅栏,所述粗格栅栏和细格栅栏外侧设置有栅渣外运模块。As preferably, the connecting pipeline between the first sedimentation tank 4 and the centrifuge tank 1 is embedded with a coarse grid fence, and the connecting pipeline between the reaction tank and the first sedimentation tank is embedded with a fine grid fence, and the coarse grid fence and A grid slag transport module is arranged on the outside of the fine grid fence.
作为优选,第一沉淀池4为沉沙池,第二沉淀池7内间隔有A2/O池和二沉池,A2/O池通过管道与鼓风机房连通,所述二沉池与A2/O池之间设置有污泥回流模块。As preferably, the first sedimentation tank 4 is a grit chamber, and the second sedimentation tank 7 is separated by an A2/O pond and a secondary sedimentation tank, and the A2/O pond is communicated with the blower room through a pipeline, and the secondary sedimentation tank is connected to the A2/O A sludge return module is arranged between the pools.
作为优选,第二沉淀池7连通有高效沉淀池,高效沉淀池与第二沉淀池之间设置有中间提升泵房,高效沉淀池上端开设有辅助剂添加口。Preferably, the second sedimentation tank 7 is connected with a high-efficiency sedimentation tank, an intermediate lifting pump room is arranged between the high-efficiency sedimentation tank and the second sedimentation tank, and an auxiliary agent addition port is opened at the upper end of the high-efficiency sedimentation tank.
作为优选,检测池6与第二沉淀池7之间还连通有反硝化深床滤池和消毒接触池,消毒接触池设置有次氯酸钠添加模块。Preferably, a denitrification deep bed filter and a disinfection contact tank are connected between the detection tank 6 and the second sedimentation tank 7, and the disinfection contact tank is provided with a sodium hypochlorite adding module.
作为优选,反硝化深床滤池连接有反冲洗模块,反冲洗模块用于对反硝化深床滤池进行冲洗清洁,使反硝化深床滤池在短时间内恢复过滤能力。Preferably, the denitrification deep bed filter is connected with a backwashing module, and the backwashing module is used for flushing and cleaning the denitrification deep bed filter, so that the denitrification deep bed filter can restore the filtering capacity in a short time.
如图4所示,一种用于循环疏通式工业废水处理装置的循环疏通式工业废水处理装置的控制系统,所述循环疏通式工业废水处理装置的控制系统包括:As shown in Figure 4, a kind of control system of the circulating dredging type industrial wastewater treatment device for circulating dredging type industrial wastewater treatment device, the control system of described circulating dredging type industrial wastewater treatment device comprises:
中央控制模块401,用于通过中央处理器对整体装置的运行进行智能控制;The central control module 401 is used to intelligently control the operation of the overall device through the central processing unit;
检测模块402,与中央控制模块401连接,用于通过多个传感器对装置的运行参数进行实时监测;The detection module 402 is connected with the central control module 401, and is used to monitor the operating parameters of the device in real time through multiple sensors;
驱动模块403,与中央控制模块401连接,用于接收控制指令对多个驱动组件进行运行控制;The drive module 403 is connected to the central control module 401, and is used to receive control instructions to control the operation of multiple drive components;
辅助剂添加模块404,与中央控制模块401连接,用于通过注入装置向反应池内添加反应用辅助剂;The auxiliary agent adding module 404 is connected with the central control module 401, and is used to add the auxiliary agent for reaction into the reaction pool through the injection device;
报警模块405,与中央控制模块401连接,用于在系统出现故障时发出报警提醒。The alarm module 405 is connected with the central control module 401, and is used for sending out an alarm reminder when the system fails.
本发明针对目前的废水处理设备能耗大,处理工业废水的成本太高的问题,本发明设置了离心罐、开口、液位监测仪,离心罐1上开设有开口2,离心罐1内设置有液位监测仪3,离心罐1能将通入的工业废水离心搅拌,通过开口2加入活性炭吸附颗粒,通过离心搅拌对工业废水进行初步的吸附处理,液位监测仪3能实时监测离心罐1内废水的通入量,根据数据调节整套设备的运行做到节能;离心罐1通过管道与第一沉淀池4连接,离心罐1中初步吸附处理的废水通入第一沉淀池4进行沉淀将吸附颗粒和吸附的杂质进行沉淀并过滤;第一沉淀池4通过管道与反应池5连接,将沉淀好的废水通入反应池5中进行化学反应将废水中的重金属离子处理掉;反应池5通过管道与第二沉淀池7双向连接,进行化学处理后的废水理论上已经可以经过沉淀后排放,但是这样不够智能容易有残留,本发明将化学反应这一步骤进行循环处理污水;反应池5通过管道与检测池6双向连接,循环处理后的污水通入检测池6中进行指标检测,检测不合格再次进入循环。The present invention aims at the problem that the current waste water treatment equipment consumes a lot of energy and the cost of treating industrial waste water is too high. The present invention is provided with a centrifugal tank, an opening, and a liquid level monitor. There is a liquid level monitor 3, the centrifuge tank 1 can centrifugally stir the incoming industrial wastewater, add activated carbon adsorption particles through the opening 2, and carry out preliminary adsorption treatment on the industrial wastewater through centrifugal stirring, and the liquid level monitor 3 can monitor the centrifuge tank in real time 1, adjust the operation of the whole set of equipment according to the data to save energy; the centrifuge tank 1 is connected to the first sedimentation tank 4 through pipelines, and the wastewater in the centrifuge tank 1 is initially adsorbed and treated into the first sedimentation tank 4 for sedimentation Precipitate and filter the adsorbed particles and adsorbed impurities; the first sedimentation tank 4 is connected to the reaction tank 5 through pipelines, and the precipitated wastewater is passed into the reaction tank 5 for chemical reaction to remove the heavy metal ions in the wastewater; the reaction tank 5. The pipeline is bidirectionally connected with the second sedimentation tank 7. The wastewater after chemical treatment can theoretically be discharged after sedimentation, but this is not smart enough and easy to have residues. The present invention circulates the chemical reaction step to treat sewage; the reaction tank 5 is bidirectionally connected to the detection pool 6 through pipelines, and the recycled sewage is passed into the detection pool 6 for index detection, and if the detection is unqualified, it enters the cycle again.
以上所述仅是对本发明的较佳实施例而已,并非对本发明作任何形式上的限制,凡是依据本发明的技术实质对以上实施例所做的任何简单修改,等同变化与修饰,均属于本发明技术方案的范围内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention in any form. Any simple modifications made to the above embodiments according to the technical essence of the present invention, equivalent changes and modifications, all belong to this invention. within the scope of the technical solution of the invention.
Claims (8)
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Application publication date: 20190827 |