CN2512773Y - Wastewater treatment equipment - Google Patents
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- CN2512773Y CN2512773Y CN02202319U CN02202319U CN2512773Y CN 2512773 Y CN2512773 Y CN 2512773Y CN 02202319 U CN02202319 U CN 02202319U CN 02202319 U CN02202319 U CN 02202319U CN 2512773 Y CN2512773 Y CN 2512773Y
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Abstract
Description
技术领域:Technical field:
本实用新型涉及一种对生活污水进行净化处理的设备。The utility model relates to a device for purifying domestic sewage.
背景技术:Background technique:
目前公开使用的污水处理设备主要有大型污水处理厂和化粪池。大型污水处理厂主要在城市中使用,城市中排放的污水被集中到大型污水处理厂中进行处理,达到排放标准后再排放到河流、湖泊或大海中。大型污水处理厂占地面积大,投资大,它只能对污水进行集中处理,不能解决分散在无污水管网地区的村镇、部队营房、风景旅游区的度假村、宾馆等产生的污水污染问题。因此,大型污水处理厂对分散排入江河的源头和流程的污水无法进行处理。另外,经大型污水处理厂处理过的污水一般都被排放掉,不能实现中水再利用。化粪池是一百多年前就开始使用的污水处理设施,与大型污水处理厂相比,它占地面积小,投资较小,适合对无污水管网地区的分散的污水污染源进行治理。为了解决无污水管网地区的污水处理问题,目前我国还大量采用化粪池对无污水管网的地区的机关、学校、部队营房、度假村、宾馆和工厂等的生活污水进行处理。化粪池只能使粪便的粗颗粒沉淀发酵,没有污水净化功能,它处理过的污水仍然浑浊恶臭,达不到卫生排放标准。如果经化粪池处理后的污水直接排放到河流和湖泊中,仍然会对淡水资源造成污染。另外,经化粪池处理排放的污水中大量散发硫化氢气体,硫化氢对大气会造成严重的污染。由于化粪池对污水的处理效果较差,发达国家早就停止使用。The sewage treatment equipment currently in public use mainly includes large sewage treatment plants and septic tanks. Large-scale sewage treatment plants are mainly used in cities. The sewage discharged from cities is concentrated in large-scale sewage treatment plants for treatment, and then discharged into rivers, lakes or seas after meeting the discharge standards. Large-scale sewage treatment plants occupy a large area and require a large investment. They can only conduct centralized treatment of sewage, and cannot solve the problem of sewage pollution in villages and towns, military barracks, resorts and hotels in scenic tourist areas scattered in areas without sewage pipe networks. Therefore, large-scale sewage treatment plants cannot treat the sewage that is scattered into the source and process of rivers. In addition, the sewage treated by large sewage treatment plants is generally discharged, and reclaimed water cannot be reused. Septic tank is a sewage treatment facility that has been used for more than 100 years. Compared with large sewage treatment plants, it occupies a smaller area and requires less investment. It is suitable for the treatment of scattered sewage pollution sources in areas without sewage pipe networks. In order to solve the problem of sewage treatment in areas without sewage pipe network, septic tanks are also widely used in my country to treat domestic sewage in organs, schools, army barracks, resorts, hotels and factories in areas without sewage pipe network. The septic tank can only precipitate and ferment the coarse particles of feces, and has no sewage purification function. The treated sewage is still turbid and smelly, which cannot meet the sanitary discharge standards. If the sewage treated by septic tanks is directly discharged into rivers and lakes, it will still pollute fresh water resources. In addition, a large amount of hydrogen sulfide gas is released in the sewage discharged from the septic tank, and hydrogen sulfide will cause serious pollution to the atmosphere. Due to the poor treatment effect of septic tanks on sewage, developed countries have long stopped using them.
发明内容:Invention content:
本实用新型要解决的技术问题是,大型污水处理厂无法对无污水管网的地区的分散的污水污染源进行处理,化粪池对污水的处理达不到卫生排放标准的要求。为解决该技术问题,本实用新型采用以下技术方案:污水处理设备,包括絮凝罐1、沉淀过滤罐2和氧化生化罐3;它的特殊之处是:絮凝罐1与沉淀过滤罐2的下部连通,沉淀过滤罐2的上部与氧化生化罐3的上部连通;沉淀过滤罐2的中部具有过滤板5,过滤板5的上面具有过滤层6;氧化生化罐3中具有水平隔板7,水平隔板7上具有若干水通道8,氧化生化罐3的入口9对准第一条水通道8,相邻的两条水通道8首尾相接,最后一条水通道8与氧化生化罐3的出口10连通;水通道8的底部具有过滤层11,水通道8与大气连同。The technical problem to be solved by the utility model is that large-scale sewage treatment plants cannot treat scattered sewage pollution sources in areas without sewage pipe networks, and the treatment of sewage by septic tanks cannot meet the requirements of sanitary discharge standards. In order to solve this technical problem, the utility model adopts the following technical solutions: sewage treatment equipment, including flocculation tank 1,
絮凝罐1具有污水入口,经过初步处理或者经过化粪池处理的污水通过该入口进入絮凝罐1中。絮凝罐1具有药剂投放口,通过该投放口可以向絮凝罐1中投放三氯化铁等用于使污水中的胶体物质絮凝的药剂。絮凝罐1的主要作用是,通过药剂使污水中的半溶于水的胶体物质絮凝,迫使其分子组合成颗粒析出,并沉淀到罐底,再进行缺氧分解,在厌氧菌的作用下进行酸性发酵,生成二氧化碳、甲烷。如果采用三氯化铁作为絮凝的药剂,三氯化铁与硫化氢起反应可以析出硫沉入罐底,有毒的硫化氢气体就不会排放到大气中。沉淀过滤罐2的主要作用是对经过絮凝罐1处理过的污水中的絮凝颗粒进行过滤和沉淀,它的过滤板5设在中部,可以实现从下向上的反向过滤,污水中的絮凝颗粒被过滤板5过滤在其下表面上,靠自身的重量沉淀到罐底继续分解。过滤层6的空隙中很快会形成“生物膜”,“生物膜”对透过过滤板5的更加细小的絮凝颗粒进一步过滤并进行生化处理,使有机物在“生物膜”的作用下进一步生化降解。氧化生化罐3通过其中的首尾相接的水通道8来加长污水流动的路程,使污水在流动的过程中增加与空气接触的面积。在过滤层11的空隙中很快形成“生物膜”,“生物膜”起生化作用。污水中的有机物与过滤层11上部大气中的氧气起反应,使有机物进一步氧化(湿性燃烧),最终污水变得清洁、无味、透明。The flocculation tank 1 has a sewage inlet through which the sewage that has undergone primary treatment or septic tank treatment enters into the flocculation tank 1 . The flocculation tank 1 has a medicament feeding port, through which a medicament for flocculating colloidal substances in sewage, such as ferric chloride, can be put into the flocculation tank 1 . The main function of the flocculation tank 1 is to flocculate the semi-water-soluble colloidal substances in the sewage through the medicament, forcing its molecules to form particles and precipitate them to the bottom of the tank, and then undergo anoxic decomposition. Under the action of anaerobic bacteria Acidic fermentation is carried out to produce carbon dioxide and methane. If ferric chloride is used as the agent for flocculation, the reaction between ferric chloride and hydrogen sulfide can precipitate sulfur and sink to the bottom of the tank, and the toxic hydrogen sulfide gas will not be discharged into the atmosphere. The main function of the
本实用新型的氧化生化罐3中的水平隔板7分为若干块,它们在氧化生化罐3内上下分布,并且相互平行;氧化生化罐3的入口9对准最上面的水平隔板7上的第一条水通道8,最下面的一块水平隔板7上的最后一条水通道8与氧化生化罐3的出口10连通;中间的每一块水平隔板7上的第一条水通道8的始端都对准相邻的上一块水平隔板7上的最后一条水通道8的末端的出口12,最后一条水通道8的末端都对准相邻的下一块水平隔板7上的第一条水通道8的始端。The
水平隔板7分为若干块,即两块以上,这样既可以在有限的占地面积上增加污水流动的路程,又可以在两块相邻的水平隔板7之间使污水自由下落,使空气中的氧气大量溶于污水中,提高对污水中有机物生化处理的效果。The horizontal dividing
本实用新型的水平隔板7上的水通道8是由若干垂直隔板13相互间隔而成的,垂直隔板13固定在水平隔板7上;垂直隔板13相互平行并且都与水平隔板7垂直,使水通道8呈直槽状;水通道8通过通气管14与大气连通。The
本实用新型的沉淀过滤罐2的过滤板5上具有过滤网15,过滤层6由碎石组成。The filter plate 5 of the
过滤板5上具有若干能够使污水通过的孔,过滤网15安装在这些孔上。污水在沉淀过滤罐2中由下向上通过过滤网15时,较大的絮凝颗粒被过滤网15过滤在其下表面上,最后靠自身的重量沉淀到罐底。过滤层6由碎石组成,在碎石的空隙中很快形成“生物膜”,使透过过滤网15的较小的絮凝颗粒在“生物膜”的作用下进行生化处理。The filter plate 5 has some holes that can allow the sewage to pass through, and the
本实用新型的水通道8底部的过滤层11由碎石组成。The filter layer 11 at the bottom of the
过滤层11由碎石组成,在碎石的空隙中很快形成“生物膜”,使流经水通道8的污水中的有机物在“生物膜”的作用下进行生化处理。The filter layer 11 is composed of gravel, and a "biofilm" is quickly formed in the voids of the gravel, so that the organic matter in the sewage flowing through the
本实用新型的絮凝罐1具有投药管4和充气管16。The flocculation tank 1 of the utility model has a
投药管4用于向絮凝罐1中投放用于使污水中的胶体物质絮凝的药剂,药剂可以选择三氯化铁。充气管16由于向絮凝罐1中的污水中充入高压空气,高压空气对污水进行搅拌,使投入的药剂与污水混合均匀,提高絮凝的效果。The
本实用新型的上述技术方案中,从絮凝罐1的污水入口进入絮凝罐1的污水,一般是经过初步处理的污水,例如经过化粪池处理的污水。In the above technical solution of the utility model, the sewage entering the flocculation tank 1 from the sewage inlet of the flocculation tank 1 is generally treated sewage, such as sewage treated by a septic tank.
在污水没有经过初步处理的情况下,本实用新型还可以包括腐化罐17和腐化罐18;腐化罐17的上部具有污水入口19,腐化罐17的上部通过连通管20与腐化罐18的上部连通,腐化罐18的上部通过连通管21与絮凝罐1的上部连通。In the case that the sewage has not been preliminarily treated, the utility model can also include a
污水经过污水入口19进入腐化罐17中,在腐化罐17中经过处理后再经连通管20进入腐化罐18中。在腐化罐17和腐化罐18中污水中的有机物在微生物的代谢作用下发酵,进行好氧降解。有机物的分解大致分为两个阶段:第一阶段是氧化过程,第二阶段是硝化过程。Sewage enters the
氧化过程主要在腐化罐17中完成,也就是有机物氧化为二氧化碳的过程,化学方程式为:The oxidation process is mainly completed in the
(微生物)(microorganism)
在自然条件下(温度为20℃),一般有机物第一阶段的氧化分解可以在10~20天内完成。Under natural conditions (temperature is 20°C), the first-stage oxidative decomposition of general organic matter can be completed within 10 to 20 days.
硝化过程主要是在腐化罐18中完成的,在硝化菌的作用下,将氨(NH3)氧化为亚硝酸盐和硝酸盐,化学方程式为:The nitrification process is mainly completed in the
本实用新型的腐化罐18内具有纵向放置的隔离板22,隔离板22将腐化罐18纵向隔离成腔室23和腔室24;腔室23的上部通过连通管20与腐化罐17的上部连通,腔室24的上部通过连通管21与絮凝罐1的上部连通;隔离板22的下部通过连通口将腔室23与腔室24连通,连通口处安装有过滤网25。The
过滤网25可以把较大的有机物颗粒和其它杂物阻挡在腐化罐18中继续分解。The
为了使经过处理后得到的中水能够继续利用,本实用新型还包括蓄水罐26;氧化生化罐3的出口10与蓄水罐26连通,蓄水罐26中具有抽水管27。In order to make the treated reclaimed water continue to be utilized, the utility model also includes a
与大型污水处理厂相比,本实用新型占地面积小,造价低,能耗低。由于本实用新型能够实现小型化,可以广泛用于旅游风景区、海岛、农村等无污水管网的地区,对村镇、部队营房、宾馆、工厂等产生的生活污水进行处理。广泛采用本实用新型,可以防止生活污水污染河流的源头和流程,保护淡水资源。由于本实用新型带有蓄水罐26,可以实现对中水的再利用,可以节约大量淡水。与化粪池相比,本实用新型对污水的处理效果非常明显。由于在絮凝罐1中可以投入三氯化铁等药剂,使污水中的胶体物质组合成颗粒析出,并沉淀到罐底进行缺氧分解,在厌氧菌的作用下进行酸性发酵,生成二氧化碳、甲烷、硫化氢。三氯化铁与硫化氢起反应,析出硫沉入罐底。这样,避免了在污水处理过程中产生的硫化氢进入大气造成二次污染。经过本实用新型处理过的生活污水,青岛市崂山区环境监测站的水质监测报告认为:“其出水口污染物PH、CODCR、悬浮物、氨氮和磷酸盐均达到GB8978-1996《污水综合排放标准》一级标准。该污水处理设施对CODCR、悬浮物的处理效果明显,去除率在97.00%以上”[摘自崂环委(水监)字2001年第45号]。Compared with large-scale sewage treatment plants, the utility model has the advantages of small floor area, low cost and low energy consumption. Because the utility model can realize miniaturization, it can be widely used in areas without sewage pipe network, such as tourist attractions, islands, and rural areas, to treat domestic sewage produced in villages, towns, army barracks, hotels, factories, etc. Widely adopting the utility model can prevent domestic sewage from polluting the source and flow of rivers and protect fresh water resources. Because the utility model has the
附图说明:Description of drawings:
图1为本实用新型的实施例1的主视图(即图2中的B-B视图);Fig. 1 is the front view (being the B-B view among Fig. 2) of embodiment 1 of the present utility model;
图2为图1中的A-A视图;Fig. 2 is A-A view among Fig. 1;
图3为图2中的C-C视图;Fig. 3 is the C-C view among Fig. 2;
图4为本实用新型的实施例2的主视图(全剖视);Fig. 4 is the front view (full section) of
图5为图4中的D-D视图;Fig. 5 is the D-D view among Fig. 4;
图6为图4中的E-E视图。FIG. 6 is an E-E view in FIG. 4 .
具体实施方式:Detailed ways:
下面结合附图对本实用新型的最佳实施例进行详细描述。The preferred embodiment of the utility model will be described in detail below in conjunction with the accompanying drawings.
实施例1:Example 1:
如图1至图3所示,本实施例是一种方型污水处理设备,它由腐化罐17、腐化罐18、絮凝罐1、沉淀过滤罐2、氧化生化罐3和蓄水罐26组成。絮凝罐1、沉淀过滤罐2、氧化生化罐3、腐化罐17、腐化罐18和蓄水罐26都采用混凝土制造,它们都为长方体的罐,并且都埋在地下。腐化罐17、腐化罐18、絮凝罐1、沉淀过滤罐2、氧化生化罐3和蓄水罐26的上表面上分别具有盖28、29、30、31、32和33。腐化罐17的一个侧面的上部具有污水入口19,在腐化罐17与腐化罐18的相邻的两个侧面的上部通过连通管20将腐化罐17与腐化罐18连通,腐化罐18与絮凝罐1的相邻的两个侧面的上部通过连通管21将腐化罐18与絮凝罐1连通。絮凝罐1与沉淀过滤罐2的相邻的两个侧面的下部通过连通口34将絮凝罐1与沉淀过滤罐2连通,沉淀过滤罐2与氧化生化罐3相邻的两个侧面的上部通过连通管9将沉淀过滤罐2与氧化生化罐3连通。氧化生化罐3的出水口10与蓄水罐26连通。腐化罐18内的一个角上具有纵向放置的隔离板22,隔离板22将腐化罐18纵向隔离成腔室23和腔室24。腔室23的上部通过连通管20与腐化罐17的上部连通,腔室24的上部通过连通管21与絮凝罐1的上部连通。隔离板22的下部通过连通口将腔室23与腔室24连通,连通口处安装有过滤网25。絮凝罐1的上表面上安装有投药管4和充气管16,投药管4的外端与加药剂的泵连通,充气管16的外端与空气压缩机连通。沉淀过滤罐2的中部具有过滤板5,过滤板5上具有若干能够是污水通过的孔,这些孔上安装有过滤网15。过滤板5的上面具有过滤层6,过滤层6由碎石组成。氧化生化罐3中安装有四块水平隔板7,四块水平隔板7在氧化生化罐3内上下分布,并且相互平行。每一块水平隔板7上都具有几条水通道8,水通道8由几块垂直隔板13相互间隔而成。垂直隔板13都固定在水平隔板7上,同一块水平隔板7上的垂直隔板13相互平行并且都与水平隔板7垂直,使水通道8呈直槽状。氧化生化罐3的上表面上安装有通气管14。水通道8通过通气管14与大气连通。水通道8的底部具有过滤层11,过滤层11由碎石组成。氧化生化罐3的入口9(即连通管9)对准最上面的水平隔板7上的第一条水通道8,最下面的一块水平隔板7上的最后一条水通道8与氧化生化罐3的出口10连通。中间的每一块水平隔板7上的第一条水通道8的始端都对准相邻的上一块水平隔板7上的最后一条水通道8的末端的出口12,最后一条水通道8的末端都对准相邻的下一块水平隔板7上的第一条水通道8的始端。蓄水罐26中安装有抽水管27,抽水管27的上端与抽水泵连通。As shown in Figures 1 to 3, this embodiment is a square sewage treatment equipment, which consists of a
实施例2:Example 2:
如图4至图6所示,本实施例是一种圆形污水处理设备,它由腐化罐17、腐化罐18、絮凝罐1、沉淀过滤罐2和氧化生化罐3组成。絮凝罐1、沉淀过滤罐2、氧化生化罐3、腐化罐17、腐化罐18和蓄水罐26都采用混凝土制造,它们都为圆柱体的罐,并且都埋在地下。沉淀过滤罐2套在絮凝罐1中,沉淀过滤罐2的圆柱面侧壁与絮凝罐1的圆柱面侧壁之间的空间构成絮凝罐1的内腔。腐化罐17、腐化罐18、沉淀过滤罐2和氧化生化罐3的上表面上分别具有盖28、29、31和32。沉淀过滤罐2的下部与絮凝罐1连通,连通处安装有过滤网36。本实施例除了腐化罐17、腐化罐18、絮凝罐1、沉淀过滤罐2、氧化生化罐3都为圆柱体的罐、腐化罐18中没有隔离板22、沉淀过滤罐2套在絮凝罐1中和没有蓄水罐26等与实施例1不同以外,其他部分与实施例1基本相同。As shown in FIGS. 4 to 6 , this embodiment is a circular sewage treatment equipment, which consists of a
上述实施例1和实施例2在使用时,生活污水经污水入口19进入腐化罐17中。在腐化罐17中,污水中的有机物在微生物的代谢作用下发酵,进行好氧降解,该过程为氧化过程。在腐化罐17中经过氧化分解的污水经连通管20进入腐化罐18中。在腐化罐18中,污水在硝化菌的作用下,将氨(NH3)氧化为亚硝酸盐和硝酸盐物质,该过程为硝化阶段。经过腐化罐处理的污水通过连通管21进入絮凝罐1中。通过投药管4向絮凝罐1中泵入5%的三氯化铁浓溶液,同时通过充气管16向絮凝罐1中充入高压空气对污水进行“搅拌”,使污水中半溶于水的胶体物质絮凝,迫使其分子组合成颗粒析出,并沉淀到罐底,再进行缺氧分解,在厌氧菌的作用下进行酸性发酵,生成二氧化碳、甲烷。三氯化铁与硫化氢化合可析出硫沉于罐底,有毒的硫化氢即可消失。过滤网25和过滤网36可以将较大的有机物颗粒和其它杂物阻挡住。被絮凝罐1絮凝的污水通过连通口34进入沉淀过滤罐2中。在沉淀过滤罐2中,污水经过过滤网15和过滤层6过滤,被过滤在过滤网15下表面上的絮凝颗粒,在自身重量的作用下,沉淀到灌底,继续分解。过滤网15和过滤层6的空隙中很快形成“生物膜”,“生物膜”既可起到过滤作用,又可起到生化作用。经过沉淀过滤罐2处理后的污水中悬浮物大量减少,浊度降低。被沉淀过滤罐处理过的污水通过连通管9进入氧化生化罐3中。在氧化生化罐3中,过滤层11的空隙中很快生成“生物膜”,“生物膜”对污水中残留的有机物进行生化处理和过滤,残留的有机物在这大面积的生化层中进行生物降解。同时,由于通气管14向水通道8中通入空气,充足的氧气使污水中的有机物进一步氧化(湿性燃烧),经出口10排入蓄水罐26中的水清洁、无味,达到一级排放标准。启动抽水泵可以通过抽水管27抽取蓄水罐26中的中水进行回用。When the above-mentioned embodiment 1 and
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN1907883B (en) * | 2005-08-02 | 2012-05-16 | 栗田工业株式会社 | Method for treating organic wastewater |
CN103043794A (en) * | 2013-01-25 | 2013-04-17 | 哈尔滨工业大学 | Sewage treatment method based on municipal sewage pipeline reinforcement and sewage recycling |
CN106007241A (en) * | 2016-07-21 | 2016-10-12 | 罗志明 | Novel urban pipeline sewage treatment method |
CN108816027A (en) * | 2018-07-20 | 2018-11-16 | 陈雪飞 | A kind of efficient gas purification device |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1907883B (en) * | 2005-08-02 | 2012-05-16 | 栗田工业株式会社 | Method for treating organic wastewater |
CN103043794A (en) * | 2013-01-25 | 2013-04-17 | 哈尔滨工业大学 | Sewage treatment method based on municipal sewage pipeline reinforcement and sewage recycling |
CN106007241A (en) * | 2016-07-21 | 2016-10-12 | 罗志明 | Novel urban pipeline sewage treatment method |
CN108816027A (en) * | 2018-07-20 | 2018-11-16 | 陈雪飞 | A kind of efficient gas purification device |
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