CN107473471B - 一种污水净化处理装置 - Google Patents
一种污水净化处理装置 Download PDFInfo
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- CN107473471B CN107473471B CN201710839324.8A CN201710839324A CN107473471B CN 107473471 B CN107473471 B CN 107473471B CN 201710839324 A CN201710839324 A CN 201710839324A CN 107473471 B CN107473471 B CN 107473471B
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- water
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- filtration
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- 238000000746 purification Methods 0.000 title claims abstract description 65
- 239000010865 sewage Substances 0.000 title claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 195
- 238000001914 filtration Methods 0.000 claims abstract description 99
- 239000002351 wastewater Substances 0.000 claims abstract description 49
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 48
- 239000001301 oxygen Substances 0.000 claims abstract description 48
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 46
- 239000000945 filler Substances 0.000 claims abstract description 28
- 238000004062 sedimentation Methods 0.000 claims abstract description 11
- 238000003756 stirring Methods 0.000 claims description 33
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 30
- 239000012528 membrane Substances 0.000 claims description 17
- 238000001223 reverse osmosis Methods 0.000 claims description 17
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titan oxide Chemical compound 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[P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 230000001954 sterilising Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 230000004083 survival Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- 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
-
- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultra-violet light
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/727—Treatment of water, waste water, or sewage by oxidation using pure oxygen or oxygen rich gas
-
- 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
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- 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
Abstract
本发明涉及污水处理设备技术领域，具体涉及一种污水净化处理装置，包括壳体、进水管、制氧机构和精滤机构，所述壳体内并列设置有过滤净化室和储水室，所述过滤净化室自上而下依次设置有净化区、吸附填料区、过滤网和沉降区，所述储水室内设置有水质调节区和蓄水区。本发明的净化装置，利用沉降区对废水进行一级过滤，利用吸附填料区对废水进行二级过滤，在净化区对废水进行三级过滤，在水质调节区对废水进行四级过滤，通过四级过滤，实现废水中充分过滤，使经净化装置净化后的水体达到饮用水标准，同时本发明净化装置一体化设置，占地面积小，制备成本低，便于安装使用，对促进农村水资源保护与循环利用具有重要意义。
Description
技术领域
本发明涉及污水处理设备技术领域，具体涉及一种污水净化处理装置。
背景技术
生活废水指的是居民日常生活中排泄的洗涤水。我国是一个发展中的农业大国，农村人口是城市人口的两倍多，农村生活水平不断的提高，全国农村每年有超过2500万吨的生活污水直接排放，造成河流、水塘污染，影响村民居住环境，严重威胁农民的身体健康。农村生活废水造成的环境污染不仅是农村水源地潜在的安全隐患，还会加剧淡水资源的危机，使耕地灌溉得不到有效保障，危害农民的生存发展。因此，加强农村生活污水收集、处理与资源化设施建设，避免因生活污水直接排放
现有的农村生活废水处理技术中，如中国专利公开号CN205676259U公开的一种农村生活废水回收处理设备，包括过滤网、斜挡板一、连接块一、密封挡板一、电动缸一、电动缸二、污泥泵、排污管、连接块二、斜挡板二以及密封挡板二，电动缸一上端连接密封挡板一，密封挡板一左端设有连接块一，连接块一上端安装斜挡板一，斜挡板一上方设有过滤网，过滤网下方安装斜挡板二，连接块二左端连接密封挡板二，密封挡板二下端设有电动缸二，电动缸二右侧安装污泥泵，污泥泵右端装配排污管，实现对农村生活废水进行过滤处理，降低环境污染。该回收处理设置使用方便，结构简单，便于操作，但是该装置的污水处理效果差。
又如中国专利公开号CN105645683A公开的一种结构填料强化的农村生活与餐饮废水处理装置及其方法，包括依次连接的除油池、厌氧池、缺氧池、好氧池、好氧回流池和沉淀池，所述除油池上设置有进水口，除油池内设有悬浮吸油填料；所述厌氧池、缺氧池、好氧池内分别设有生物填料；在除油池和厌氧池之间以及缺氧池和好氧池之间均设有导流管；其中好氧回流池中的曝气支管上设有曝气头，曝气头上方设置扬水管，扬水管管体侧壁通过回流管与缺氧池相连，通过气提回流方式实现污水回流；该发明在总体布局上采用一体化的处理工艺，可以实现75％以上的总氮，65％以上的总磷去除和90％以上的COD降解，但是该装置的占地面积宽，投资成本大，不利于实际农村推广和应用。
又如中国专利公开号CN205347104U公开的一种农村生活废水处理系统，包括依次连接的化粪池、格栅井、集水池、综合池、土壤渗滤系统。该系统化粪池分为三格：第一格为进粪池，第二格为沉卵灭菌池，第三格为排放池、集水池内安装有污水泵、综合池为长方形池体，在池底部设贮泥斗。该系统结构简单，操作性强，实施费用较低，但是该系统的废水处理量小，处理效率低。
为弥补现有技术中的不足，本发明提供一种结构简单，使用便捷，废水处理效率高，处理效果好的农村生活污水处理装置。
发明内容
本发明的目的在于克服现有技术的不足，提供一种污水净化处理装置，结构简单，使用便捷，利用沉降区对废水进行一级过滤，利用吸附填料区对废水进行二级过滤，在净化区对废水进行三级过滤，在水质调节区对废水进行四级过滤，通过四级过滤，实现废水中充分过滤，使经净化装置净化后的水体达到饮用水标准，同时本发明净化装置一体化设置，占地面积小，制备成本低，便于安装使用，对促进农村水资源保护与循环利用具有重要意义。
本发明的目的是通过以下技术方案来实现的：
一种污水净化处理装置，包括壳体、进水管、制氧机构和精滤机构，所述壳体内设置在第一隔板，第一隔板将壳体分割为并列设置的过滤净化室和储水室，所述过滤净化室自上而下依次设置有净化区、吸附填料区、过滤网和沉降区，所述进水管设置在壳体顶部，且进水管依次穿过壳体、净化区、吸附填料区和过滤网，与沉降区连通，所述沉降区的底部上还设置有排渣管，所述过滤网用于过滤废水中的大颗粒杂质，所述吸附填料区内填充有吸附填料，用于对污水进行进一步的过滤吸附，所述制氧机构包括制氧装置、氧气管和排气管，所述制氧装置设置在壳体的侧壁上，所述氧气管设置在净化区内，氧气管与制氧装置通过连通管连接，所述排气管设置在净化区顶部，所述储水室内设置有第二隔板，第二隔板将储水室分割为水质调节区和蓄水区，所述水质调节区设置在蓄水区的上方，水质调节区的侧壁上设置有加药管，所述精滤机构包括精滤管、精滤水管和水泵，所述精滤管设置在水质调节区内，精滤管内设置有水通道，所述精滤水管设置在壳体外，精滤水管的一端与水通道连通，另一端与蓄水区连通，所述水泵设置在精滤水管上，所述蓄水区的侧壁上还设置有出水管；所述第一隔板上还设置有溢流口，净化区通过溢流口与水质调节区连通。
进一步地，所述精滤管为反渗透膜，所述水通道周围被反渗透膜片包裹。在实际使用过程中，通过加药管向水质调节区加入试剂，调节水的pH值，对水体进行消毒，然后在驱动装置的作用下，带动搅拌叶旋转，使水与试剂充分混合，提高水质调节效率；待水质调节完全后，利用水泵工作，将水质调节区的通过反渗透膜抽入精滤水管中，在水流经反渗透膜的过程中，利用反渗透膜对水进行进一步地过滤，提高净化效果和净化效率；而经过反渗透膜过滤后的水通过精滤水管流入蓄水区储存，留待使用。
进一步地，所述净化装置还包括混合搅拌机构，所述混合搅拌机构包括驱动装置、搅拌轴和搅拌叶，所述驱动装置设置在水质调节区顶部，所述搅拌叶和搅拌轴分别设置在水质调节区内，搅拌轴的一端穿过壳体与驱动装置连接，所述搅拌叶设置在搅拌轴另一端的侧壁上。通过设置搅拌机构，在利用加药管向水质调节区加试剂进行水质调节时，启动搅拌机构，对水质调节区内的水和试剂进行搅拌混合，提高水质调节效率和调节效果。
优选地，所述水质调节区内还设置有检测单元，所述检测单元用于检测水质调节区内水质状态。通过检测单元检测水质调节区内水质状态，然后控制加药管根据水质状态加入相应试剂进行调节，节约试剂用量，提高水质调节效率和水质调节效果。
进一步地，所述搅拌叶设置在溢流口下方，所述精滤管设置在搅拌叶的下方。在使用过程中，将精滤管设置在搅拌叶的下方，避免搅拌叶在工作过程中，对精滤管造成磨损。
优选地，所述搅拌叶为螺旋式搅拌叶。
进一步地，所述氧气管上均匀设置有多个通气孔，氧气管设置在溢流口的下方。在使用过程中，通过制氧装置制得氧气，氧气通过氧气管上通气孔进入并溶解水中，从而提高水体中含氧量，实现对水体含氧量的调节控制。
进一步地，所述净化区内还分别设置有活性炭滤网和紫外光照单元，所述活性炭滤网表面负载二氧化钛，且活性炭滤网与溢流口底部齐平设置，所紫外光灯照单元设置在净化区顶部。在实际工作过程中，通过进水管向沉降区注入农村生活废水，在沉降区内，废水中的固体颗粒杂质受过滤网的阻隔，不能进入吸附填料区，同时受重力作用，落入沉降区底部，实现对废水的一级过滤；而水则在水压作用下不断向上升，依次通过过滤网、吸附填料区和净化区，利用吸附填料区对废水进行进一步的吸附过滤，去除废水中的小颗粒杂质和重金属，实现对废水的二级过滤；然后在净化区中，利用制氧机构对废水进行含氧量调节，同时废水在通过活性炭滤网，从溢流口流入水质调节区的过程中，利用紫外光照单元与负载二氧化钛的活性炭滤网具有光触媒效应，对水质进行深度吸附过滤，分解废水中的有机物，提高净化效率和净化效果，实现对废水的三级过滤；最后在水质调节区中，利用反渗透膜结构的精滤管对废水进行精细过滤，过滤级别达到纳米级别，实现对废水的四级过滤，使经净化装置净化后的水体达到饮用水标准。
进一步地，所述紫外灯照单元为紫外灯管。利用紫外光照单元与负载二氧化钛的活性炭滤网协作，使活性炭滤网具有光触媒功能，能够有效对水体内有机物进行持续吸附分解，提高净化效率和净化效果。
进一步地，所述排渣管上设置有排渣阀，所述出水管上还设置有出水阀。在需要对沉降区内沉积的杂质进行清除时，开启排渣阀，使沉降区内沉积的杂质通过排渣管排出，提高沉降区持续工作能力。
本发明的有益效果是：本发明污水净化处理装置，结构简单，使用便捷，利用沉降区对废水进行一级过滤，利用吸附填料区对废水进行二级过滤，在净化区对废水进行三级过滤，在水质调节区对废水进行四级过滤，通过四级过滤，实现废水中充分过滤，使经净化装置净化后的水体达到饮用水标准，同时本发明净化装置一体化设置，占地面积小，制备成本低，便于安装使用，对促进农村水资源保护与循环利用具有重要意义。
附图说明
图1为本发明农村生活废水净化装置的结构示意图；
图2为本发明精滤管的结构示意图；
图3为本发明精滤管的局部剖视图；
图中，1-壳体，2-进水管，3-沉降区，4-过滤网，5-吸附填料区，6-净化区，7-排渣管，8-水质调节区，9-蓄水区，10-第一隔板，11-第二隔板，12-制氧装置，13-连通管，14-氧气管，15-通气孔，16-排气管，17-溢流口，18-驱动装置，19-搅拌轴，20-搅拌叶，21-加药管，22-检测单元，23-精滤管，24-精滤水管，25-水泵，26-出水管，27-活性炭滤网，28-紫外灯照单元，29-排渣阀，30-出水阀，31-水通道。
具体实施方式
下面结合附图进一步详细描述本发明的技术方案，但本发明的保护范围不局限于以下所述。
如图1、图2和图3所示，一种污水净化处理装置，包括壳体1、进水管2、制氧机构和精滤机构，所述壳体1内设置在第一隔板10，第一隔板10将壳体1分割为并列设置的过滤净化室和储水室，所述过滤净化室自上而下依次设置有净化区6、吸附填料区5、过滤网4和沉降区3，所述进水管2设置在壳体1顶部，且进水管2依次穿过壳体1、净化区6、吸附填料区5和过滤网4，与沉降区3连通，所述沉降区3的底部上还设置有排渣管7，所述过滤网4用于过滤废水中的大颗粒杂质，所述吸附填料区5内填充有吸附填料，用于对污水进行进一步的过滤吸附，所述制氧机构包括制氧装置12、氧气管14和排气管16，所述制氧装置12设置在壳体1的侧壁上，所述氧气管14设置在净化区6内，氧气管14与制氧装置12通过连通管13连接，所述排气管16设置在净化区6顶部，所述储水室内设置有第二隔板11，第二隔板11将储水室分割为水质调节区8和蓄水区9，所述水质调节区8设置在蓄水区9的上方，水质调节区8的侧壁上设置有加药管21，所述精滤机构包括精滤管23、精滤水管24和水泵25，所述精滤管23设置在水质调节区8内，精滤管23内设置有水通道31，所述精滤水管24设置在壳体1外，精滤水管24的一端与水通道31连通，另一端与蓄水区9连通，所述水泵25设置在精滤水管24上，所述蓄水区9的侧壁上还设置有出水管26；所述第一隔板10上还设置有溢流口17，净化区6通过溢流口17与水质调节区8连通。
具体地，所述精滤管23为反渗透膜，所述水通道31周围被反渗透膜片包裹。在实际使用过程中，通过加药管21向水质调节区8加入试剂，调节水的pH值，对水体进行消毒，然后在驱动装置18的作用下，带动搅拌叶20旋转，使水与试剂充分混合，提高水质调节效率；待水质调节完全后，利用水泵25工作，将水质调节区8的通过反渗透膜抽入精滤水管24中，在水流经反渗透膜的过程中，利用反渗透膜对水进行进一步地过滤，提高净化效果和净化效率；而经过反渗透膜过滤后的水通过精滤水管24流入蓄水区9储存，留待使用。优选地，所述水质调节区8内均匀设置有多条精滤管23。
具体地，所述净化装置还包括混合搅拌机构，所述混合搅拌机构包括驱动装置18、搅拌轴19和搅拌叶20，所述驱动装置18设置在水质调节区8顶部，所述搅拌叶20和搅拌轴19分别设置在水质调节区8内，搅拌轴19的一端穿过壳体1与驱动装置18连接，所述搅拌叶20设置在搅拌轴19另一端的侧壁上。通过设置搅拌机构，在利用加药管21向水质调节区8加试剂进行水质调节时，启动搅拌机构，对水质调节区内的水和试剂进行搅拌混合，提高水质调节效率和调节效果。
优选地，所述水质调节区8内还设置有检测单元22，所述检测单元22用于检测水质调节区内水质状态。通过检测单元22检测水质调节区内水质状态，然后控制加药管21根据水质状态加入相应试剂进行调节，节约试剂用量，提高水质调节效率和水质调节效果。
具体地，所述搅拌叶20设置在溢流口17下方，所述精滤管23设置在搅拌叶20的下方。在使用过程中，将精滤管23设置在搅拌叶20的下方，避免搅拌叶20在工作过程中，对精滤管23造成磨损。
优选地，所述搅拌叶20为螺旋式搅拌叶。
具体地，所述氧气管14上均匀设置有多个通气孔15，氧气管14设置在溢流口17的下方。在使用过程中，通过制氧装置12制得氧气，氧气通过氧气管14上通气孔15进入并溶解水中，从而提高水体中含氧量，实现对水体含氧量的调节控制。
具体地，所述净化区6内还分别设置有活性炭滤网27和紫外光照单元28，所述活性炭滤网27表面负载二氧化钛，且活性炭滤网27与溢流口17底部齐平设置，所紫外光灯照单元28设置在净化区6顶部。在实际工作过程中，通过进水管2向沉降区3注入农村生活废水，在沉降区3内，废水中的固体颗粒杂质受过滤网4的阻隔，不能进入吸附填料区5，同时受重力作用，落入沉降区3底部，实现对废水的一级过滤；而水则在水压作用下不断向上升，依次通过过滤网4、吸附填料区5和净化区6，利用吸附填料区5对废水进行进一步的吸附过滤，去除废水中的小颗粒杂质和重金属，实现对废水的二级过滤；然后在净化区6中，利用制氧机构对废水进行含氧量调节，同时废水在通过活性炭滤网27，从溢流口17流入水质调节区8的过程中，利用紫外光照单元28与负载二氧化钛的活性炭滤网27具有光触媒效应，对水质进行深度吸附过滤，分解废水中的有机物，提高净化效率和净化效果，实现对废水的三级过滤；最后在水质调节区8中，利用反渗透膜结构的精滤管23对废水进行精细过滤，过滤级别达到纳米级别，实现对废水的四级过滤，使经净化装置净化后的水体达到饮用水标准。
具体地，所述紫外灯照单元28为紫外灯管。利用紫外光照单元28与负载二氧化钛的活性炭滤网27协作，使活性炭滤网27具有光触媒功能，能够有效对水体内有机物进行持续吸附分解，提高净化效率和净化效果。
具体地，所述排渣管7上设置有排渣阀29，所述出水管26上还设置有出水阀30。在需要对沉降区3内沉积的杂质进行清除时，开启排渣阀29，使沉降区3内沉积的杂质通过排渣管7排出，提高沉降区持续工作能力。而需要利用蓄水区9内净化水时，开启出水阀30，即可实现净化水的导出。
使用时，将农村生活废水通过进水管2注入沉降区3，在沉降区3内，废水中的固体颗粒杂质受过滤网4的阻隔，不能进入吸附填料区5，同时固体颗粒杂质受重力作用，落入沉降区3底部，实现对废水的一级过滤；而水则在水压作用下不断向上升，依次通过过滤网4、吸附填料区5和净化区6，利用吸附填料区5对废水进行进一步的吸附过滤，去除废水中的小颗粒杂质和重金属，实现对废水的二级过滤；然后在净化区6中，利用制氧机构对废水进行含氧量调节，同时废水在通过活性炭滤网27，从溢流口17流入水质调节区8的过程中，利用紫外光照单元28与负载二氧化钛的活性炭滤网27具有光触媒效应，对水质进行深度吸附过滤，分解废水中的有机物，提高净化效率和净化效果，实现对废水的三级过滤；最后在水质调节区8中，利用反渗透膜结构的精滤管23对废水进行精细过滤，过滤级别达到纳米级别，实现对废水的四级过滤，使经净化装置净化后的水体达到饮用水标准，净化后的水通过精滤水管24流入蓄水区9储存，留待使用。
以上所述仅是本发明的优选实施方式，应当理解本发明并非局限于本文所披露的形式，不应看作是对其他实施例的排除，而可用于各种其他组合、修改和环境，并能够在本文所述构想范围内，通过上述教导或相关领域的技术或知识进行改动。而本领域人员所进行的改动和变化不脱离本发明的精神和范围，则都应在本发明所附权利要求的保护范围内。
Claims (6)
1.一种污水净化处理装置，其特征在于，包括壳体、进水管、制氧机构和精滤机构，所述壳体内设置在第一隔板，第一隔板将壳体分割为并列设置的过滤净化室和储水室，所述过滤净化室自上而下依次设置有净化区、吸附填料区、过滤网和沉降区，所述进水管设置在壳体顶部，且进水管依次穿过壳体、净化区、吸附填料区和过滤网，与沉降区连通，所述沉降区的底部上还设置有排渣管，所述过滤网用于过滤废水中的大颗粒杂质，所述吸附填料区内填充有吸附填料，所述制氧机构包括制氧装置、氧气管和排气管，所述制氧装置设置在壳体的侧壁上，所述氧气管设置在净化区内，氧气管与制氧装置通过连通管连接，所述排气管设置在净化区顶部，所述储水室内设置有第二隔板，第二隔板将储水室分割为水质调节区和蓄水区，所述水质调节区设置在蓄水区的上方，水质调节区的侧壁上设置有加药管，所述精滤机构包括精滤管、精滤水管和水泵，所述精滤管设置在水质调节区内，精滤管内设置有水通道，所述精滤水管设置在壳体外，精滤水管的一端与水通道连通，另一端与蓄水区连通，所述水泵设置在精滤水管上，所述蓄水区的侧壁上还设置有出水管；所述第一隔板上还设置有溢流口，净化区通过溢流口与水质调节区连通；所述净化区内还分别设置有活性炭滤网和紫外光照单元，所述活性炭滤网表面负载二氧化钛，且活性炭滤网与溢流口底部齐平设置，所紫外光灯照单元设置在净化区顶部；所述排渣管上设置有排渣阀，所述出水管上还设置有出水阀。
2.根据权利要求1所述的一种污水净化处理装置，其特征在于，所述精滤管为反渗透膜，所述水通道周围被反渗透膜片包裹。
3.根据权利要求1所述的一种污水净化处理装置，其特征在于，所述净化装置还包括混合搅拌机构，所述混合搅拌机构包括驱动装置、搅拌轴和搅拌叶，所述驱动装置设置在水质调节区顶部，所述搅拌叶和搅拌轴分别设置在水质调节区内，搅拌轴的一端穿过壳体与驱动装置连接，所述搅拌叶设置在搅拌轴另一端的侧壁上。
4.根据权利要求3所述的一种污水净化处理装置，其特征在于，所述搅拌叶设置在溢流口下方，所述精滤管设置在搅拌叶的下方。
5.根据权利要求1所述的一种污水净化处理装置，其特征在于，所述氧气管上均匀设置有多个通气孔，氧气管设置在溢流口的下方。
6.根据权利要求1所述的一种污水净化处理装置，其特征在于，所述紫外灯照单元为紫外灯管。
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