CN207845454U - Multistage filtering microorganism sewage water processing unit - Google Patents
Multistage filtering microorganism sewage water processing unit Download PDFInfo
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- 239000010865 sewage Substances 0.000 title claims abstract description 24
- 238000001914 filtration Methods 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 43
- 244000005700 microbiome Species 0.000 title claims 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 50
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 47
- 238000006243 chemical reaction Methods 0.000 claims abstract description 23
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 18
- 239000000835 fiber Substances 0.000 claims abstract description 15
- 238000005273 aeration Methods 0.000 claims abstract description 11
- 238000005374 membrane filtration Methods 0.000 claims abstract description 11
- 239000004408 titanium dioxide Substances 0.000 claims abstract description 11
- 239000012528 membrane Substances 0.000 claims abstract description 9
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 4
- 239000011248 coating agent Substances 0.000 claims description 3
- 238000000576 coating method Methods 0.000 claims description 3
- 238000005192 partition Methods 0.000 claims description 3
- 241000220317 Rosa Species 0.000 claims 4
- 238000006385 ozonation reaction Methods 0.000 claims 3
- 229910052799 carbon Inorganic materials 0.000 claims 2
- 239000002351 wastewater Substances 0.000 claims 1
- 230000000813 microbial effect Effects 0.000 abstract description 15
- 239000000969 carrier Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 abstract 1
- 239000000126 substance Substances 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000002955 isolation Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000002957 persistent organic pollutant Substances 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- 241000700605 Viruses Species 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
本实用新型提供一种多级过滤微生物污水处理装置,它包括通过抽液泵依次相连通的浮动过滤器、臭氧处理罐和生物过滤罐;所述浮动过滤器包括外筒体和设置在所述外筒体内部的内胆筒体,所述内胆筒体内设置有二氧化钛纤维网层和紫外线灯,所述臭氧处理罐包括臭氧反应箱、活性炭过滤箱及溢流箱;所述臭氧反应箱的底部还设置有臭氧曝气装置,所述活性炭过滤箱内设置有用于物理过滤的活性炭层;所述生物过滤罐包括生物反应箱和膜过滤箱,所述生物反应箱内设置有多个微生物载体层;所述膜过滤箱内设置有多组过滤管,所述过滤管上覆盖有过滤膜层。该装置结构简单、污水处理效果好。
The utility model provides a multi-stage filtration microbial sewage treatment device, which includes a floating filter, an ozone treatment tank and a biological filter tank connected in sequence through a liquid pump; the floating filter includes an outer cylinder and is arranged on the The inner tank cylinder inside the outer cylinder, the titanium dioxide fiber mesh layer and the ultraviolet lamp are arranged in the inner tank cylinder, and the ozone treatment tank includes an ozone reaction box, an activated carbon filter box and an overflow tank; the ozone reaction box The bottom is also provided with an ozone aeration device, and an activated carbon layer for physical filtration is arranged in the activated carbon filter box; the biological filter tank includes a biological reaction box and a membrane filter box, and a plurality of microbial carriers are arranged in the biological reaction box layer; the membrane filtration box is provided with multiple groups of filter tubes, and the filter tubes are covered with filter membrane layers. The device has simple structure and good sewage treatment effect.
Description
技术领域technical field
本实用新型涉及一种污水处理设备,具体的说,涉及了一种多级过滤微生物污水处理装置。The utility model relates to a sewage treatment device, in particular to a multi-stage filtration microbial sewage treatment device.
背景技术Background technique
二氧化钛是一种能进行光能—化学能转换的半导体材料,并且二氧化钛化学性质稳定、高效、无毒、廉价、应用范围广以及不产生二次污染,利用它的光催化氧化性在较短时间里将难降解毒性有机污染物氧化分解为二氧化钛和水,把有毒有害的污染物氧化或还原为无害物。尽管二氧化钛具有以上优点,但也存在一定的局限性。事实上,对于某些有机物,仅仅使用二氧化钛很难将其完全降解,此时单独使用二氧化钛来处理水并不是最佳的方法。另外,现有的生物污水处理设备投资费用过高,从而导致了中国目前的生物污水处理能力尚跟不上用水规模的迅速扩张,配套设施建设严重滞后。Titanium dioxide is a semiconductor material that can convert light energy to chemical energy. Titanium dioxide has stable chemical properties, high efficiency, non-toxicity, low cost, wide application range and no secondary pollution. Its photocatalytic oxidation can be used in a short time It oxidizes and decomposes refractory toxic organic pollutants into titanium dioxide and water, and oxidizes or reduces toxic and harmful pollutants to harmless substances. Although titanium dioxide has the above advantages, it also has certain limitations. In fact, for some organic substances, it is difficult to completely degrade them only by using titanium dioxide. At this time, using titanium dioxide alone to treat water is not the best method. In addition, the investment cost of existing biological sewage treatment equipment is too high, which has led to the fact that China's current biological sewage treatment capacity cannot keep up with the rapid expansion of water consumption, and the construction of supporting facilities is seriously lagging behind.
为了解决以上存在的问题,人们一直在寻求一种理想的技术解决方案。In order to solve the above existing problems, people have been seeking an ideal technical solution.
发明内容Contents of the invention
本实用新型的目的是针对现有技术的不足,从而提供一种多级过滤微生物污水处理装置。The purpose of the utility model is to provide a multi-stage filtration microbial sewage treatment device aiming at the deficiencies of the prior art.
为了实现上述目的,本实用新型所采用的技术方案是:一种多级过滤微生物污水处理装置,它包括通过多个液泵依次相连通的浮动过滤器、臭氧处理罐和生物过滤罐;In order to achieve the above object, the technical solution adopted by the utility model is: a multi-stage filter microbial sewage treatment device, which includes a floating filter, an ozone treatment tank and a biological filter tank connected in sequence through a plurality of liquid pumps;
所述浮动过滤器包括外筒体和设置在所述外筒体内部的内胆筒体,所述外筒体的外部侧壁上固定有浮箱;所述内胆筒体的顶部内侧设置有紫外线灯,所述内胆筒体内设置有多层纤维网层,位于最顶层的所述纤维网层涂覆有二氧化钛涂层;The floating filter includes an outer cylinder body and an inner cylinder body arranged inside the outer cylinder body, a buoyancy tank is fixed on the outer side wall of the outer cylinder body; Ultraviolet lamp, the inner tank cylinder is provided with multiple layers of fiber mesh, and the fiber mesh layer on the top layer is coated with a titanium dioxide coating;
所述外筒体和所述内胆筒体之间的型腔通过两个隔板分为进水室和出水室,所述进水室的侧壁上部开设有污水进口,所述进水室通过第一抽液泵连通所述内胆筒体,且所述第一抽液泵的出水口位于最底层所述纤维网层的下方;位于最顶层所述纤维网层上方的所述内胆筒体侧壁上开设有第一溢流孔,所述内胆筒体通过所述第一溢流孔连通所述出水室;所述出水室的底部开设有预处理水出口,所述预处理水出口通过第二抽液泵连通所述臭氧处理罐;The mold cavity between the outer cylinder and the inner tank cylinder is divided into a water inlet chamber and a water outlet chamber through two partitions, the upper part of the side wall of the water inlet chamber is provided with a sewage inlet, and the water inlet chamber The inner tank cylinder is communicated with the first liquid suction pump, and the water outlet of the first liquid suction pump is located below the bottommost fiber mesh layer; the inner container above the topmost fiber mesh layer A first overflow hole is opened on the side wall of the cylinder, and the inner tank cylinder communicates with the water outlet chamber through the first overflow hole; a pretreatment water outlet is opened at the bottom of the water outlet chamber, and the pretreatment The water outlet communicates with the ozone treatment tank through the second pump;
所述臭氧处理罐包括臭氧反应箱、活性炭过滤箱及溢流箱;所述臭氧反应箱朝向于所述活性炭过滤箱的侧壁上方设置有第一溢流槽,所述臭氧反应箱通过所述第一溢流槽连通所述活性炭过滤箱;The ozone treatment tank includes an ozone reaction box, an activated carbon filter box and an overflow box; the ozone reaction box is provided with a first overflow tank towards the side wall above the activated carbon filter box, and the ozone reaction box passes through the The first overflow tank communicates with the activated carbon filter box;
所述活性炭过滤箱的底部与所述溢流箱的底部相连通;所述臭氧反应箱的底部开设有臭氧反应箱入水口,所述溢流箱的顶部开设有溢流箱出水口;所述臭氧反应箱的底部还设置有臭氧曝气装置,所述臭氧曝气装置连接有臭氧瓶,所述活性炭过滤箱内设置有用于物理过滤的活性炭层,所述活性炭层位于所述第一溢流槽的下方;The bottom of the activated carbon filter box is connected with the bottom of the overflow box; the bottom of the ozone reaction box is provided with an ozone reaction box water inlet, and the top of the overflow box is provided with an overflow box water outlet; The bottom of the ozone reaction box is also provided with an ozone aeration device, the ozone aeration device is connected with an ozone bottle, and the activated carbon filter box is provided with an activated carbon layer for physical filtration, and the activated carbon layer is located in the first overflow below the groove;
所述生物过滤罐包括生物反应箱和膜过滤箱,所述生物反应箱内设置有多层微生物载体层;所述生物反应箱朝向于所述膜过滤箱的侧壁设置有第二溢流槽,且所述第二溢流槽位于最顶层所述微生物载体层的上方,所述生物反应箱通过所述第二溢流槽连通所述膜过滤箱;The biofiltration tank includes a bioreactor box and a membrane filtration box, the bioreactor box is provided with a multi-layer microbial carrier layer; the bioreactor box is provided with a second overflow tank towards the side wall of the membrane filtration box , and the second overflow tank is located above the top microbial carrier layer, and the bioreactor tank communicates with the membrane filtration tank through the second overflow tank;
所述生物反应箱底部设置有生物反应箱入口;所述生物反应箱入口通过第三抽液泵连通所述溢流箱出水口;所述膜过滤箱内设置有多组过滤管,所述过滤管上覆盖有过滤膜层,多组所述过滤管通过汇流管连通有第四抽液泵。The bottom of the bioreactor box is provided with a bioreactor inlet; the inlet of the bioreactor is connected to the outlet of the overflow box through a third pump; the membrane filter box is provided with multiple sets of filter tubes, and the filter The tubes are covered with a filter membrane layer, and multiple groups of the filter tubes are connected to a fourth pump through a confluence tube.
基于上述,所述外筒体的顶部设置有防雨罩,所述防雨罩与所述外筒体的顶部之间形成器材固定室,所述器材固定室内设置所述第一抽液泵和移动电源。Based on the above, the top of the outer cylinder is provided with a rainproof cover, and an equipment fixing room is formed between the rainproof cover and the top of the outer cylinder, and the first liquid suction pump and the first suction pump are arranged in the equipment fixing room. mobile power.
基于上述,所述出水室内还设置有电热丝。Based on the above, a heating wire is also arranged in the water outlet chamber.
基于上述,所述臭氧曝气装置为曝气头、溶气泵、水射器、管道混合器、穿孔管或滤头。Based on the above, the ozone aeration device is an aeration head, a dissolved air pump, a water ejector, a pipeline mixer, a perforated pipe or a filter head.
本实用新型相对现有技术具有实质性特点和进步,具体的说,本实用新型所提供的多级过滤微生物污水处理装置,首先采用多层纤维网层过滤掉污水中的大颗粒物质,再经紫外线灯照射的二氧化钛氧化还原,达到杀灭污水中的细菌病毒,并将有机物初步降解,然后再采用臭氧氧化有机物,提高有机污染物的可生化性,最后与生物过滤区联合进行处理,充分利用臭氧分解产生的氧气,提高了附着在过滤膜层上的各种优势细菌所获得的氧气量,可大幅度提高膜过滤箱内细菌的工作活力,增强对污水的有效处理。该装置结构简单、使用方便。Compared with the prior art, the utility model has substantive characteristics and progress. Specifically, the multi-stage filtration microbial sewage treatment device provided by the utility model first adopts multi-layer fiber mesh layers to filter out large particles in the sewage, and then passes through The oxidation and reduction of titanium dioxide irradiated by ultraviolet light can kill the bacteria and viruses in the sewage, and degrade the organic matter initially, and then use ozone to oxidize the organic matter to improve the biodegradability of organic pollutants, and finally combine with the biological filter area for treatment to make full use of The oxygen generated by the decomposition of ozone increases the amount of oxygen obtained by various dominant bacteria attached to the filter membrane layer, which can greatly improve the working activity of bacteria in the membrane filter box and enhance the effective treatment of sewage. The device is simple in structure and convenient to use.
附图说明Description of drawings
图1是本实用新型提供的多级过滤微生物污水处理装置整体结构示意图。Figure 1 is a schematic diagram of the overall structure of the multi-stage filtration microbial sewage treatment device provided by the utility model.
图2是本实用新型提供的多级过滤微生物污水处理装置中的浮动过滤器结构示意图。Fig. 2 is a structural schematic diagram of the floating filter in the multi-stage filtration microbial sewage treatment device provided by the utility model.
图3是本实用新型提供的多级过滤微生物污水处理装置中的过滤管结构示意图。Fig. 3 is a structural schematic diagram of the filter tube in the multi-stage filtration microbial sewage treatment device provided by the utility model.
图中:1、浮动过滤器;2、浮箱;3、第一抽液泵;4、第二抽液泵;5、臭氧处理罐;6、臭氧曝气装置;7、臭氧供气管;8、活性炭过滤箱;9、隔离板;10、溢流箱;11、第三抽液泵;12、生物反应箱;13、微生物载体层;14、第二溢流槽;15、过滤管;16、第四抽液泵;17、进水室;18、内胆筒体;19、出水室;20、电热丝;21、移动电源;22、紫外线灯;23、污水进口;24、纤维网层;25、过滤膜层;26、第一溢流槽。In the figure: 1. Floating filter; 2. Floating tank; 3. The first liquid suction pump; 4. The second liquid suction pump; 5. Ozone treatment tank; 6. Ozone aeration device; 7. Ozone air supply pipe; 8 , activated carbon filter box; 9, isolation plate; 10, overflow box; 11, the third liquid pump; 12, biological reaction box; 13, microbial carrier layer; 14, the second overflow tank; 15, filter tube; 16 , the fourth suction pump; 17, water inlet chamber; 18, inner tank cylinder; 19, water outlet chamber; 20, heating wire; 21, mobile power supply; 22, ultraviolet lamp; 23, sewage inlet; 24, fiber mesh layer ; 25, filter membrane layer; 26, the first overflow tank.
具体实施方式Detailed ways
下面通过具体实施方式,对本实用新型的技术方案做进一步的详细描述。The technical solutions of the present invention will be further described in detail through specific implementation methods below.
实施例1Example 1
如图1、图2和图3所示,本实施例提供了一种多级过滤微生物污水处理装置,它包括通过多个抽液泵依次相连通的浮动过滤器1、臭氧处理罐5和生物过滤罐。As shown in Fig. 1, Fig. 2 and Fig. 3, the present embodiment provides a kind of multi-stage filtration microbial sewage treatment device, it comprises the floating filter 1 that is connected successively by a plurality of suction pumps, ozone treatment tank 5 and biological canister.
所述浮动过滤器1包括外筒体和设置在所述外筒体内部的内胆筒体18,所述外筒体的外部侧壁上固定有浮箱2;所述内胆筒体18的顶部设置有紫外线灯22。所述内胆筒体18内设置有多层纤维网层24,位于最顶层的纤维网层24涂覆有二氧化钛涂层。The floating filter 1 includes an outer cylinder body and an inner tank cylinder 18 arranged inside the outer cylinder body, and a buoyancy tank 2 is fixed on the outer side wall of the outer cylinder body; The top is provided with an ultraviolet lamp 22 . Multiple layers of fiber mesh layers 24 are arranged inside the inner tank cylinder 18, and the fiber mesh layer 24 on the topmost layer is coated with a titanium dioxide coating.
所述外筒体和所述内胆筒体18之间的型腔通过两个隔板分为进水室17和出水室19,所述进水室17的侧壁上部开设有污水进口23,所述进水室17通过第一抽液泵3连通所述内胆筒体,且所述第一抽液泵3的出水口位于最底层所述纤维网层24的下方。位于最顶层所述纤维网层24上方的所述内胆筒体18侧壁上开设有第一溢流孔,所述内胆筒体18通过所述第一溢流孔连通所述出水室19。所述出水室19的底部开设有预处理水出口,所述预处理水出口通过第二抽液泵4连通所述臭氧处理罐5。The mold cavity between the outer cylinder body and the inner tank cylinder body 18 is divided into a water inlet chamber 17 and a water outlet chamber 19 through two partitions, the upper part of the side wall of the water inlet chamber 17 is provided with a sewage inlet 23, The water inlet chamber 17 communicates with the inner tank cylinder through the first liquid suction pump 3 , and the water outlet of the first liquid suction pump 3 is located below the bottommost fiber mesh layer 24 . A first overflow hole is opened on the side wall of the inner tank cylinder 18 above the fiber mesh layer 24 on the topmost layer, and the inner tank cylinder 18 communicates with the water outlet chamber 19 through the first overflow hole. . The bottom of the outlet chamber 19 is provided with a pre-treated water outlet, and the pre-treated water outlet is connected to the ozone treatment tank 5 through the second liquid suction pump 4 .
所述臭氧处理罐包括臭氧反应箱、活性炭过滤箱8及溢流箱10。所述臭氧反应箱朝向于所述活性炭过滤箱8的侧壁设置有第一溢流槽26,且所述第一溢流槽26位于所述活性炭过滤箱8的上端,所述臭氧反应箱通过所述第一溢流槽26连通所述活性炭过滤箱8。The ozone treatment tank includes an ozone reaction box, an activated carbon filter box 8 and an overflow box 10 . The ozone reaction box is provided with a first overflow tank 26 towards the side wall of the activated carbon filter box 8, and the first overflow tank 26 is positioned at the upper end of the activated carbon filter box 8, and the ozone reaction box passes through The first overflow tank 26 communicates with the activated carbon filter box 8 .
所述活性炭过滤箱8和所述溢流箱10底部连通,且所述活性炭过滤箱8和所述溢流箱10之间通过隔离板9相隔离。所述隔离板9的底部开设有连通孔。所述臭氧反应箱底部开设有臭氧反应箱入水口,所述溢流箱顶部开设有溢流箱出水口;所述臭氧反应箱的底部还设置有臭氧曝气装置6,所述臭氧曝气装置6通过臭氧供气管7连接有臭氧瓶,所述活性炭过滤箱8内设置有用于物理过滤的活性炭层。所述活性炭层位于所述第一溢流槽26的下方。The activated carbon filter box 8 communicates with the bottom of the overflow box 10 , and the activated carbon filter box 8 and the overflow box 10 are separated by a separation plate 9 . The bottom of the isolation plate 9 is provided with communication holes. The bottom of the ozone reaction box is provided with an ozone reaction box water inlet, and the top of the overflow box is provided with an overflow box water outlet; the bottom of the ozone reaction box is also provided with an ozone aeration device 6, and the ozone aeration device 6 is connected with an ozone bottle through an ozone gas supply pipe 7, and an activated carbon layer for physical filtration is arranged in the activated carbon filter box 8. The activated carbon layer is located below the first overflow tank 26 .
所述生物过滤罐包括生物反应箱12和膜过滤箱。所述生物反应箱12内设置有多层微生物载体层13;所述生物反应箱12朝向于所述膜过滤箱的侧壁设置有第二溢流槽14,且所述第二溢流槽14位于所述微生物载体层13的上方,所述生物反应箱12通过所述第二溢流槽14连通所述膜过滤箱。The biofiltration tank includes a bioreactor box 12 and a membrane filtration box. The bioreactor 12 is provided with a multi-layer microbial carrier layer 13; the bioreactor 12 is provided with a second overflow tank 14 towards the side wall of the membrane filtration tank, and the second overflow tank 14 Located above the microbial carrier layer 13 , the bioreactor box 12 communicates with the membrane filtration box through the second overflow tank 14 .
所述生物反应箱12的底部设置有生物反应箱入口;所述生物反应箱入口通过第三抽液泵11连通所述溢流箱出水口。所述膜过滤箱内设置有多组过滤管15,所述过滤管15上覆盖有过滤膜层25,多组所述过滤管15通过汇流管连通有第四抽液泵16。The bottom of the bioreactor 12 is provided with an inlet of the bioreactor; the inlet of the bioreactor is connected to the water outlet of the overflow tank through the third pump 11 . Multiple sets of filter tubes 15 are arranged in the membrane filtration box, and the filter tubes 15 are covered with a filter membrane layer 25 , and multiple sets of the filter tubes 15 are connected to a fourth pump 16 through a confluence tube.
其中,本实施例中,所述外筒体的顶部设置有防雨罩,所述防雨罩与所述外筒体的顶部之间形成器材固定室,所述器材固定室内设置所述第一抽液泵3和移动电源21。所述出水室内19还设置有电热丝20。所述臭氧曝气装置为曝气头。Wherein, in this embodiment, the top of the outer cylinder is provided with a rainproof cover, and an equipment fixing room is formed between the rainproof cover and the top of the outer cylinder, and the first equipment fixing room is provided in the equipment fixing room. Suction pump 3 and mobile power supply 21. The water outlet chamber 19 is also provided with a heating wire 20 . The ozone aeration device is an aeration head.
最后应当说明的是:以上实施例仅用以说明本实用新型的技术方案而非对其限制;尽管参照较佳实施例对本实用新型进行了详细的说明,所属领域的普通技术人员应当理解:依然可以对本实用新型的具体实施方式进行修改或者对部分技术特征进行等同替换;而不脱离本实用新型技术方案的精神,其均应涵盖在本实用新型请求保护的技术方案范围当中。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present utility model and not limit it; although the utility model has been described in detail with reference to the preferred embodiment, those of ordinary skill in the art should understand that: still The specific implementation of the utility model can be modified or some technical features can be equivalently replaced; without departing from the spirit of the technical solution of the utility model, all of them should be included in the scope of the technical solution claimed by the utility model.
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