CN207142972U - 一种用于城市污水的高效处理系统 - Google Patents
一种用于城市污水的高效处理系统 Download PDFInfo
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- CN207142972U CN207142972U CN201720857431.9U CN201720857431U CN207142972U CN 207142972 U CN207142972 U CN 207142972U CN 201720857431 U CN201720857431 U CN 201720857431U CN 207142972 U CN207142972 U CN 207142972U
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- 239000010865 sewage Substances 0.000 title claims abstract description 78
- 238000000034 method Methods 0.000 title claims abstract description 19
- 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 148
- 238000005192 partition Methods 0.000 claims abstract description 35
- 238000004062 sedimentation Methods 0.000 claims abstract description 15
- 239000012528 membrane Substances 0.000 claims abstract description 10
- 238000001914 filtration Methods 0.000 claims description 45
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 38
- 239000007788 liquid Substances 0.000 claims description 21
- 239000000463 material Substances 0.000 claims description 19
- 229910052799 carbon Inorganic materials 0.000 claims description 14
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- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound 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- 230000003071 parasitic Effects 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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Abstract
本实用新型公开了一种用于城市污水的高效处理系统，包括池体，池体的左侧顶端设置有进水管，污水进水管延伸进入池体内部且在污水进水管的右端连接有缓冲管，在池体的内部靠左侧设有第一隔板，第一隔板的左侧为缓冲池，缓冲管设置在缓冲池顶部，在第一隔板的底端设置有控制阀，在池体的内部靠右侧设有第二隔板，第一隔板和第二隔板之间为沉淀池，第二隔板的右侧为清水池，沉淀池的底部设置有刮泥器，本实用新型用于城市污水的高效处理系统，采用多级处理设备对污水进行处理，对污水中的小分子污染物进行降解，同时膜组件对污水进行深层过滤，处理效果好、效率高，处理后的水能够达到再利用的要求，避免了污水污染，也节约了宝贵的水资源。
Description
一种用于城市污水的高效处理系统
技术领域 一
[0001] 本实用新型涉及污水处理技术领域，具体是一种用于城市污水的高效处理系统。
背景技术 4
[0002] 城市污水排入城镇污水系统的污水的统称。在合流制排水系统中，还包括生产废 水和截留的雨水。城市污水主要包括生活污水和工业污水，由城市排水管网汇集并输送到 污水处理厂进行处理。城市污水处理是指为改变污水性质，使其对环境水域不产生危害而 采取的措施。城市污水处理一般分为三级:一级处理，系应用物理处理法去除污水中不溶解 的污染物和寄生虫卵；二级处理，系应用生物处理法将污水中各种复杂的有机物氧化降解 为简单的物质；三级处理，系应用化学沉淀法、生物化学法、物理化学法等，去除污水中的 磷、氮、难降解的有机物、无机盐等。至于采取哪级处理比较合理，应视对最终排出物的处理 要求而定。现有的城市污水处理设备大都净化效果差、处理效率低，不能满足现代化城市污 水处理的使用需求。 实用新型内容
[0003] 本实用新型的目的在于提供一种用于城市污水的高效处理系统，以解决上述背景 技术中提出的问题。
[0004] 为实现上述目的，本实用新型提供如下技术方案：
[0005] 一种用于城市污水的高效处理系统，包括池体，所述池体的左侧顶端设置有进水 管，污水进水管延伸进入池体内部且在污水进水管的右端连接有缓冲管，在池体的内部靠 左侧设有第一隔板，第一隔板的左侧为缓冲池，缓冲管设置在缓冲池顶部，在第一隔板的底 端设置有控制阀，在池体的内部靠右侧设有第二隔板，第一隔板和第二隔板之间为沉淀池， 第二隔板的右侧为清水池，沉淀池的底部设置有刮泥器，刮泥器下端设置有防水电机，防水 电机两侧设置有排泥管，在排泥管的顶部设有排泥阀门，所述池体的右侧设有过滤池，在过 滤池的上侧设有喷淋管，在喷淋管的下侧外壁上均匀设有若干个喷淋头，池体通过第一进 水管与喷淋管的进水口连接，在第一进水管上设有第一水泵，在过滤池内部由上至下依次 设有第一滤料层、第二滤料层、第一活性炭层、填料层和第二活性炭层，过滤池的底部设有 贮水槽，所述过滤池右侧设有消毒处理池，消毒处理池与过滤池之间设有气液混合器，气液 混合器通过输水管与消毒处理池连接，气液混合器上侧依次设有第二水泵和臭氧发生器， 第二水泵通过第二进水管与过滤池底端的出水口连接，第二水泵的出水口通过水泵出水管 与气液混合器连接，臭氧发生器出气口通过出气管与气液混合器连接，在消毒处理池内部 设有精滤膜装置，精滤膜装置的内部设有粗滤活性炭装置，在粗滤活性炭装置内部设有导 流器，在消毒处理池的内壁上设有光触媒涂层。
[0006]作为本实用新型进一步的方案:所述第一隔板和第二隔板均由高分子塑料制成。
[0007]作为本实用新型再进一步的方案:所述第一活性炭层和第二活性炭层之间的密度 之比为1:2。
[0008]作为本实用新型再进一步的方案:所述填料层内的填料为纤维状。
[0009]作为本实f新型再进一步的方案:所述消毒处理池右侧依次设有第一水处理器、 第二水处理器和第三水处理器，消毒处理池的出水口处连接有第二连接水管，第二连接水 管通过第二水泵与进水主管连接，进水主管分别通过三个进水支管和第一水处理器、第二 水处理器、第三水处理器连接，第一水处理器、第二水处理器和第三水处理器都包括水净化 框、旋转接头、外壳、驱动电机和转轴，水净化框位于外壳内部，旋转接头位于水净化框的上 端，驱动电机设置在水净化框的底部，驱动电机通过转轴驱动水净化框，驱动电机的中心轴 线、旋转接头的中心轴线、水净化框的中心轴线和外壳的中心轴线在同一直线上，水净化框 通过旋转接头与进水支管连通，水净化框内侧和外侧均设置有筒状反渗透膜，两个反渗透 膜的中心轴线和水净化框的中心轴线在同一直线上，水净化框的内部通过反渗透膜与外壳 的内部连通，外壳的出水口通过出水支管与出水主管连通，所述旋转接头为单向通道旋转 接头，出水主管连接有收集池。
[0010]与现有技术相比，本实用新型的有益效果是：
[0011] 1、污水进入池体内部，通过设置的沉淀池可以将污泥沉淀到池底，更好地进行水 和淤泥的分离，通过设置的刮泥器，可以将沉淀池底的淤泥进行较为干净的清理，通过设置 的排泥管能够及时将淤泥排出，通过设置的控制阀门可将缓冲池内的污水缓流入沉淀池， 避免湍急的水流造成水质的浑浊，提高污水沉淀效果和效率，随着沉淀池的水位升高，上层 的清水将会通过第二隔板进入清水池，进行后续处理。
[0012] 2、经过处理后的污水进入过滤池内部，通过上下设置的第一滤料层、第二滤料层、 第一活性炭层、填料层和第二活性炭层对污水进行层层过滤，提高了污水处理效果，第一滤 料层和第二滤料层分别为猛砂滤料和石英砂滤料组成，经过层层过滤，过滤后的污水进入 贮水槽中进行下一步处理。
[0013] 3、污水处理过程中，第二水栗通过左侧的第二水管和右侧的水泵出水管将污水抽 到气液混合器内，再通过臭氧发生器将臭氧输送到气液混合器内，气液混合器将臭氧和污 水混合，并产生化学反应，通过输水管将产生反应的污水水送到消毒处理池中，污水通过粗 滤活性炭装置和精滤膜装置对产生反应的污水进行过滤，粗滤活性炭装置和精滤膜装置能 够提高污水中有机物和氨氮的去除率，且能对污水进行臭氧杀菌消毒，进一步的提高了污 水处理的效果，通过设置纳米光触媒涂层，能够充分分解污水中的细菌和有毒物质，从而对 污水进行深层净化，保证了污水处理效果。
[0014] 4、经过消毒处理池处理后的污水被抽入第一水处理器、第二水处理器和第三水处 理器进行处理，驱动电机驱动水净化框转动，利用离心力的作用，使水净化框中的污水产生 压力，从而达到反渗透的要求，净化水则由水净化框中进入到外壳内部，最后净化水经过外 壳的出水口从出水主管流出，经过水处理器处理的净化水进入收集池中被收集，以方便后 续再利用，整个水处理系统，净化效果好、效率高，处理后的水能够达到再利用的要求，避免 了污水污染，也节约了宝贵的水资源。
附图说明 _
[0015] 图1为用于城市污水的高效处理系统的结构示意图。
具体实施方式
[0016]下面将结合本实用新型实施例中的附图，对本实用新型实施例中的技术方案进行 清楚、完整地描述，显然，所描述的实施例仅仅是本实用新型一部分实施例，而不是全部的 实施例。基于本实用新型中的实施例，本领域普通技术人员在没有做出创造性劳动前提下 所获得的所有其他实施例，都属于本实用新型保护的范围。
[0017]请参阅图1，本实用新型实施例中，一种用于城市污水的高效处理系统，包括池体 1，所述池体1的左侧顶端设置有进水管2，污水进水管2延伸进入池体1内部且在污水进水管 2的右端连接有缓冲管201，在池体1的内部靠左侧设有第一隔板101，第一隔板101的左侧 为缓冲池1〇2,缓冲管201设置在缓冲池102顶部，在第一隔板1〇1的底端设置有控制阀103， 在池体1的内部靠右侧设有第二隔板105,第一隔板101和第二隔板1〇5之间为沉淀池104,第 二隔板105的右侧为清水池106,所述第一隔板101和第二隔板1〇5均由高分子塑料制成，沉 淀池104的底部设置有刮泥器5,刮泥器5下端设置有防水电机51，防水电机51两侧设置有排 泥管4，在排泥管4的顶部设有排泥阀门3，污水进入池体1内部，通过设置的沉淀池可以将污 泥沉淀到池底，更好地进行水和淤泥的分离，通过设置的刮泥器，可以将沉淀池底的淤泥进 行较为干净的清理，通过设置的排泥管能够及时将淤泥排出，通过设置的控制阀门可将缓 冲池内的污水缓流入沉淀池，避免湍急的水流造成水质的浑浊，提高污水沉淀效果和效率， 随着沉淀池的水位升高，上层的清水将会通过第二隔板进入清水池，进行后续处理;所述池 体1的右侧设有过滤池8，在过滤池8的上侧设有喷淋管9，在喷淋管9的下侧外壁上均匀设有 若干个喷淋头91，池体1通过第一进水管6与喷淋管9的进水口连接，在第一进水管6上设有 第一水泵7,在过滤池8内部由上至下依次设有第一滤料层81、第二滤料层82、第一活性炭 层83、填料层84和第二活性炭层85,所述第一活性炭层83和第二活性炭层85之间的密度之 比为1:2,所述填料层84内的填料为纤维状，过滤池8的底部设有贮水槽86,经过处理后的 污水进入过滤池8内部，通过上下设置的第一滤料层81、第二滤料层82、第一活性炭层83、 填料层84和第二活性炭层85对污水进行层层过滤，提高了污水处理效果，第一滤料层和第 二滤料层分别为猛砂滤料和石英砂滤料组成，经过层层过滤，过滤后的污水进入贮水槽86 中进行下一步处理;所述过滤池8右侧设有消毒处理池16,消毒处理池16与过滤池8之间设 有气液混合器11，气液混合器11通过输水管17与消毒处理池16连接，气液混合器11上侧依 次设有第二水泵12和臭氧发生器14,第二水栗12通过第二进水管10与过滤池8底端的出水 口连接，第二水栗12的出水口通过水栗出水管13与气液混合器11连接，臭氧发生器14出气 口通过出气管15与气液混合器11连接，在消毒处理池16内部设有精滤膜装置18,精滤膜装 置18的内部设有粗滤活性炭装置19,在粗滤活性炭装置19内部设有导流器171，在消毒处 理池16的内壁上设有光触媒涂层161，污水处理过程中，第二水泵通过左侧的第二水管和 右侧的水栗出水管将污水抽到气液混合器内，再通过臭氧发生器将臭氧输送到气液混合器 内，气液混合器将臭氧和污水混合，并产生化学反应，通过输水管将产生反应的污水水送到 消毒处理池中，污水通过粗滤活性炭装置和精滤膜装置对产生反应的污水进行过滤，粗滤 活性炭装置和精滤膜装置能够提高污水中有机物和氨氮的去除率，且能对污水进行臭氧杀 菌消毒，进一步的提高了污水处理的效果，通过设置纳米光触媒涂层161，能够充分分解污 水中的细菌和有毒物质，从而对污水进行深层净化，保证了污水处理效果;所述消毒处理池 16右侧依次设有第一水处理器23、第二水处理器24和第三水处理器25，消毒处理池16的出 水口处连接有第二连接水管，第二连接水管通过第二水泵20与进水主管21连接，进水主管 21分别通过三个进水支管22和第一水处理器23、第二水处理器24、第三水处理器25连接，第 一水处理器23、第二水处理器24和第三水处理器25都包括水净化框26、旋转接头27、外壳 28、驱动电机29和转轴30，水净化框26位于外壳28内部，旋转接头27位于水净化框26的上 端，驱动电机29设置在水净化框26的底部，驱动电机29通过转轴30驱动水净化框26，驱动电 机29的中心轴线、旋转接头27的中心轴线、水净化框26的中心轴线和外壳28的中心轴线在 同一直线上，水净化框26通过旋转接头27与进水支管22连通，水净化框26内侧和外侧均设 置有筒状反渗透膜，两个反渗透膜的中心轴线和水净化框26的中心轴线在同一直线上，水 净化框26的内部通过反渗透膜与外壳28的内部连通，外壳28的出水口通过出水支管31与 出水主管32连通，所述旋转接头27为单向通道旋转接头，出水主管32连接有收集池，经过消 毒处理池ie处理后的污水被抽入第一水处理器23、第二水处理器24和第三水处理器25进行 处理，驱动电机29驱动水净化框26转动，利用离心力的作用，使水净化框3中的污水产生压 力，从而达到反渗透的要求，净化水则由水净化框26中进入到外壳28内部，最后净化水经过 外壳28的出水口从出水主管32流出，经过水处理器处理的净化水进入收集池中被收集，以 方便后续再利用，整个水处理系统，净化效果好、效率高，处理后的水能够达到再利用的要 求，避免了污水污染，也节约了宝贵的水资源。本实用新型用于城市污水的高效处理系统， 采用多级处理设备对污水进行处理，对污水中的小分子污染物进行降解，同时膜组件对污 水进行深层过滤，处理效果好、效率高，处理后的水能够达到再利用的要求，避免了污水污 染，也节约了宝贵的水资源。
[0018]对于本领域技术人员而言，显然本实用新型不限于上述示范性实施例的细节，而 且在不背离本实用新型的精神或基本特征的情况下，能够以其他的具体形式实现本实用新 型。因此，无论从哪一点来看，均应将实施例看作是示范性的，而且是非限制性的，本实用新 型的范围由所附权利要求而不是上述说明限定，因此旨在将落在权利要求的等同要件的含 义和范围内的所有变化囊括在本实用新型内。不应将权利要求中的任何附图标记视为限制 所涉及的权利要求。
[0019]此外，应当理解，虽然本说明书按照实施方式加以描述，但并非每个实施方式仅包 含一个独立的技术方案，说明书的这种叙述方式仅仅是为清楚起见，本领域技术人员应当 将说明书作为一个整体，各实施例中的技术方案也可以经适当组合，形成本领域技术人员 可以理解的其他实施方式。
Claims (5)
1. 一种用于城市污水的高效处理系统，包括池体（1)，其特征在于，所述池体（1)的左侧 顶端设置有进水管(2)，污水进水管⑵延伸进入池体(1)内部且在污水进水管(2)的右端连 接有缓冲管(201)，在池体（1)的内部靠左侧设有第一隔板（101)，第一隔板(101)的左侧为 缓冲池（102)，缓冲管(201)设置在缓冲池（102)顶部，在第一隔板（101)的底端设置有控制 阀（103)，在池体(1)的内部靠右侧设有第二隔板(105)，第一隔板(101)和第二隔板(105)之 间为沉淀池（104)，第二隔板（105)的右侧为清水池（106)，沉淀池（104)的底部设置有刮泥 器(5)，刮泥器(5)下端设置有防水电机(51)，防水电机(51)两侧设置有排泥管(4)，在排泥 管⑷的顶部设有排泥阀门⑶，所述池体⑴的右侧设有过滤池⑻，在过滤池⑻的上侧设 有喷淋管(9)，在喷淋管⑼的下侧外壁上均匀设有若干个喷淋头(91)，池体(1)通过第一进 水管⑹与喷淋管⑼的进水口连接，在第一进水管⑹上设有第一水栗(7)，在过滤池⑻内 部由上至下依次设有第一滤料层(81)、第二滤料层(82)、第一活性炭层(83)、填料层(84)和 第二活性炭层(85)，过滤池(8)的底部设有贮水槽(86)，所述过滤池(8)右侧设有消毒处理 池（16)，消毒处理池（16)与过滤池⑻之间设有气液混合器(11)，气液混合器(11)通过输水 管（17)与消毒处理池（16)连接，气液混合器(11)上侧依次设有第二水泵（12)和臭氧发生器 (14) ，第二水栗（12)通过第二进水管（10)与过滤池(8)底端的出水口连接，第二水泵（12)的 出水口通过水泵出水管（13)与气液混合器（11)连接，臭氧发生器（14)出气口通过出气管 (15) 与气液混合器（11)连接，在消毒处理池（16)内部设有精滤膜装置（18)，精滤膜装置 (18)的内部设有粗滤活性炭装置(19)，在粗滤活性炭装置(⑼内部设有导流器(171)，在消 毒处理池(16)的内壁上设有光触媒涂层(161)。
2. 根据权利要求1所述的用于城市污水的高效处理系统，其特征在于，所述第一隔板 (101)和第二隔板(105)均由高分子塑料制成。
3. 根据权利要求1所述的用于城市污水的高效处理系统，其特征在于，所述第一活性炭 层(83)和第二活性炭层(85)之间的密度之比为1: 2。
4. 根据权利要求1所述的用于城市污水的高效处理系统，其特征在于，所述填料层(84) 内的填料为纤维状。
5. 根据权利要求1所述的用于城市污水的高效处理系统，其特征在于，所述消毒处理池 (16) 右侧依次设有第一水处理器(23)、第二水处理器(24)和第三水处理器(25)，消毒处理 池(16)的出水口处连接有第二连接水管，第二连接水管通过第二水泵(20)与进水主管(21) 连接，进水主管(21)分别通过三个进水支管(22)和第一水处理器(23)、第二水处理器(24)、 第三水处理器(25)连接，第一水处理器(23)、第二水处理器(24)和第三水处理器(25)都包 括水净化框(26)、旋转接头(27)、外壳(28)、驱动电机(29)和转轴(30)，水净化框(26)位于 外壳（28)内部，旋转接头（27)位于水净化框(26)的上端，驱动电机(29)设置在水净化框 (26)的底部，驱动电机(29)通过转轴(30)驱动水净化框(26)，驱动电机(29)的中心轴线、旋 转接头(27)的中心轴线、水净化框(26)的中心轴线和外壳(28)的中心轴线在同一直线上， 水净化框(26)通过旋转接头(27)与进水支管(22)连通，水净化框(26)内侧和外侧均设置有 筒状反渗透膜，两个反渗透膜的中心轴线和水净化框(26)的中心轴线在同一直线上，水净 化框(26)的内部通过反渗透膜与外壳(28)的内部连通，外壳(28)的出水口通过出水支管 (31)与出水主管(32)连通，所述旋转接头(2乃为单向通道旋转接头，出水主管(3¾连接有 收集池。
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| CN111977824A (zh) * | 2020-07-21 | 2020-11-24 | 安徽科技学院 | 一种农村人居环境整治用污水处理装置 |
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| CN109133422A (zh) * | 2018-09-22 | 2019-01-04 | 深圳欧赛技术有限公司 | 一种水解臭氧生活用水循环净化设备 |
| CN111977824A (zh) * | 2020-07-21 | 2020-11-24 | 安徽科技学院 | 一种农村人居环境整治用污水处理装置 |
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