CN209835820U - Bath water deep purification system - Google Patents
Bath water deep purification system Download PDFInfo
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- CN209835820U CN209835820U CN201920336339.7U CN201920336339U CN209835820U CN 209835820 U CN209835820 U CN 209835820U CN 201920336339 U CN201920336339 U CN 201920336339U CN 209835820 U CN209835820 U CN 209835820U
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Abstract
本实用新型涉及污水处理技术领域,具体公开了一种洗浴水深度净化系统,包括进水管、混凝剂药箱、混凝剂进药管、臭氧发生器、臭氧进气管、多功能介质泵、出水管、第二联接管、絮凝剂药箱、絮凝剂进药管、管道混合器、沉淀分离区、出浮渣口、浮渣收集槽、集水槽、浮渣排出管、帘式超滤膜组件、排空管、吸水管、吸水泵、出水连接管和净化后出水管,进水管的一端设在水池内,另一端与多功能介质泵的进口连接,净化后出水管的一端与集水槽连接,另一端与水池连接。本实用新型能够将絮凝、气浮、消毒、膜分离的处理方式集成在一个反应器装置内,利用加药絮凝、臭氧消毒和气浮、超滤膜的净化,完成洗浴池内水质的多重净化反应。
The utility model relates to the technical field of sewage treatment, and specifically discloses a deep purification system for bath water, comprising a water inlet pipe, a coagulant medicine box, a coagulant medicine feeding pipe, an ozone generator, an ozone air inlet pipe, a multifunctional medium pump, Outlet pipe, second connecting pipe, flocculant medicine box, flocculant feed pipe, pipeline mixer, sedimentation separation area, scum outlet, scum collection tank, water collection tank, scum discharge pipe, curtain ultrafiltration membrane Components, emptying pipe, water suction pipe, water suction pump, water outlet connection pipe and purified water outlet pipe, one end of the water inlet pipe is set in the pool, the other end is connected to the inlet of the multi-functional medium pump, and one end of the purified water outlet pipe is connected to the sump Connect the other end to the pool. The utility model can integrate the treatment methods of flocculation, air flotation, disinfection, and membrane separation into one reactor device, and complete multiple purification reactions of water quality in the bathing pool by using flocculation with medicine, ozone disinfection, air flotation, and ultrafiltration membrane purification.
Description
技术领域technical field
本实用新型涉及污水处理技术领域,尤其涉及一种洗浴水深度净化系统。The utility model relates to the technical field of sewage treatment, in particular to a deep purification system for bath water.
背景技术Background technique
目前,净化洗浴池内水质的方法主要采用化学药物絮凝沉淀,氯类药品杀菌消毒后,再用一些过滤器进行过滤利用,试图达到节约热能水费的目的,但由于这些过滤器过滤程序简单,滤水质量低劣,水质清澈度不高、异味大、二次污染严重、残留有害成分等而废弃停用。洗浴水具有水量大,温度高,污染轻的特点,对洗浴水处理后回收循环利用是提高利润的一种方式。超滤过滤相对于石英砂过滤器,活性炭过滤器微米级的过滤精度,超滤膜具有纳米级的过滤精度,该超滤设备中的膜组件具有10nm的过滤孔径,可以去除原水中几乎所有的细菌、微生物、病毒、大肠杆菌以及一些大分子的有机物和水中所有不溶解性的胶体等。利用超滤膜技术对洗浴水处理,过滤精度高,处理效率快,处理后的水质清澈,无异味,可直接回用到洗浴池中。At present, the method of purifying the water quality in the bathing pool mainly adopts the flocculation and precipitation of chemical drugs, and after sterilization and disinfection of chlorine-based drugs, some filters are used for filtration and utilization, in an attempt to achieve the purpose of saving heat and water costs. The water quality is poor, the water clarity is not high, the odor is strong, the secondary pollution is serious, and the residual harmful components are discarded. Bathing water has the characteristics of large water volume, high temperature, and light pollution. Recycling and recycling of bathing water after treatment is a way to increase profits. Compared with quartz sand filter and activated carbon filter, ultrafiltration filter has micron-level filtration accuracy, and ultrafiltration membrane has nano-level filtration accuracy. The membrane module in this ultrafiltration equipment has a filter pore size of 10nm, which can remove almost all the pollutants in raw water. Bacteria, microorganisms, viruses, Escherichia coli, and some macromolecular organic matter and all insoluble colloids in water, etc. Using ultrafiltration membrane technology to treat bathing water, the filtration accuracy is high, the treatment efficiency is fast, and the treated water is clear and odorless, and can be directly reused in the bathing pool.
实用新型内容Utility model content
本实用新型的目的是提供一种洗浴水深度净化系统,以将絮凝、气浮、消毒、膜分离的处理方式集成在一个反应器装置内,利用加药絮凝、臭氧消毒和气浮、超滤膜的净化,完成洗浴池内水质的多重净化反应。The purpose of this utility model is to provide a deep purification system for bath water, which integrates the treatment methods of flocculation, air flotation, disinfection, and membrane separation into one reactor device, and utilizes flocculation, ozone disinfection, air flotation, and ultrafiltration membrane Purification, complete multiple purification reactions of water quality in the bathing pool.
为了解决上述技术问题,本实用新型提供了一种洗浴水深度净化系统,包括进水管、混凝剂药箱、混凝剂进药管、臭氧发生器、臭氧进气管、多功能介质泵、出水管、第二联接管、絮凝剂药箱、絮凝剂进药管、管道混合器、沉淀分离区、出浮渣口、浮渣收集槽、集水槽、浮渣排出管、帘式超滤膜组件、排空管、吸水管、吸水泵、出水连接管和净化后出水管;所述进水管的一端设在水池内,另一端与所述多功能介质泵的进口连接,所述混凝剂药箱通过所述混凝剂进药管与所述进水管连接,所述臭氧发生器通过所述臭氧进气管与所述多功能介质泵的进口连接,所述多功能介质泵的出口通过出水管与所述管道混合器连接,所述絮凝剂药箱通过所述絮凝剂进药管与所述管道混合器连接,所述管道混合器通过第二联接管与所述沉淀分离区的下端连接,所述沉淀分离区的上端为排水开口,所述出浮渣口位于所述沉淀分离区的上方,所述出浮渣口的外侧依次设有浮渣收集槽和集水槽,所述浮渣排出管与所述浮渣收集槽连接,所述帘式超滤膜组件位于所述沉淀分离区的下方,所述排空管位于所述帘式超滤膜组件的下方,所述帘式超滤膜组件通过所述吸水管与所述吸水泵的进口连接,所述吸水泵的出口通过所述出水连接管与所述集水槽连接,所述净化后出水管的一端与所述集水槽连接,另一端与水池连接。In order to solve the above technical problems, the utility model provides a deep purification system for bath water, which includes a water inlet pipe, a coagulant medicine box, a coagulant medicine inlet pipe, an ozone generator, an ozone inlet pipe, a multifunctional medium pump, an outlet Water pipe, second connection pipe, flocculant medicine box, flocculant feed pipe, pipeline mixer, sedimentation separation area, scum outlet, scum collection tank, water collection tank, scum discharge pipe, curtain ultrafiltration membrane module , emptying pipe, water suction pipe, water suction pump, water outlet connection pipe and purified water outlet pipe; one end of the water inlet pipe is arranged in the pool, and the other end is connected with the inlet of the multifunctional medium pump, and the coagulant medicine The tank is connected to the water inlet pipe through the coagulant feed pipe, the ozone generator is connected to the inlet of the multifunctional medium pump through the ozone inlet pipe, and the outlet of the multifunctional medium pump is connected through the outlet pipe connected to the pipeline mixer, the flocculant tank is connected to the pipeline mixer through the flocculant feed pipe, and the pipeline mixer is connected to the lower end of the sedimentation separation zone through a second connecting pipe, The upper end of the sedimentation separation area is a drainage opening, the scum outlet is located above the sedimentation separation area, and the outside of the scum outlet is sequentially provided with a scum collection tank and a water collection tank, and the scum is discharged The pipe is connected to the scum collection tank, the curtain ultrafiltration membrane module is located below the sediment separation area, the emptying pipe is located below the curtain ultrafiltration membrane module, and the curtain ultrafiltration membrane module is The membrane module is connected to the inlet of the water suction pump through the water suction pipe, the outlet of the water suction pump is connected to the water collection tank through the water outlet connection pipe, and one end of the purified water outlet pipe is connected to the water collection tank, The other end is connected with the pool.
优选的,所述进水管在水池中的一端设有底阀,所述进水管在所述与所述混凝剂进药管的连接处的两侧均设有调节阀,所述进水管上还设有第一真空表。Preferably, one end of the water inlet pipe in the pool is provided with a bottom valve, and both sides of the connection between the water inlet pipe and the coagulant feed pipe are provided with regulating valves. A first vacuum gauge is also provided.
优选的,所述混凝剂进药管通过混凝剂计量泵及混凝剂吸药管与所述混凝剂药箱连接,所述混凝剂进药管上还设有第一阀门,所述絮凝剂进药管通过絮凝剂计量泵及絮凝剂吸药管与所述絮凝剂药箱连接,所述絮凝剂进药管上还设有第二阀门。Preferably, the coagulant feeding pipe is connected to the coagulant medicine box through a coagulant metering pump and a coagulant suction pipe, and a first valve is also arranged on the coagulant feeding pipe, The flocculant medicine feeding pipe is connected to the flocculant medicine box through a flocculant metering pump and a flocculant medicine suction pipe, and a second valve is also arranged on the flocculant medicine feeding pipe.
优选的,所述臭氧进气管上设有臭氧流量计和臭氧调节阀。Preferably, the ozone inlet pipe is provided with an ozone flow meter and an ozone regulating valve.
优选的,所述出水管上设有调节阀、压力表和流量计,所述流量计通过第一联接管与所述管道混合器连接,所述第一联接管上设有调节阀和第一取样水龙头。Preferably, the outlet pipe is provided with a regulating valve, a pressure gauge and a flow meter, and the flow meter is connected to the pipeline mixer through a first connecting pipe, and the first connecting pipe is provided with a regulating valve and a first Sampling tap.
优选的,还包括设备箱体,所述沉淀分离区和帘式超滤膜组件均设在所述设备箱体内,所述沉淀分离区为由第一隔板围成的下窄上宽的料斗状结构,所述第一隔板的内侧设有挡板结构,所述设备箱体的上端通过第二隔板形成出浮渣口,所述第二隔板上通过第三挡板隔成浮渣收集槽和集水槽,所述设备箱体的下端为收集槽结构,所述设备箱体的下端还设有设备支脚。Preferably, it also includes an equipment box, the sedimentation separation area and the curtain ultrafiltration membrane module are both arranged in the equipment box, and the sedimentation separation area is a hopper with a narrow bottom and a wide top surrounded by a first partition The inner side of the first partition is provided with a baffle structure, the upper end of the equipment box forms a scum outlet through the second partition, and the second partition is separated into a scum outlet by a third baffle. A slag collection tank and a water collection tank, the lower end of the equipment box is a collection tank structure, and the lower end of the equipment box is also provided with equipment feet.
优选的,所述集水槽通过回流平衡管与所述设备箱体的下部连接。Preferably, the water collection tank is connected to the lower part of the equipment box through a backflow balance pipe.
优选的,所述吸水管上设有调节阀和第二真空表。Preferably, the water suction pipe is provided with a regulating valve and a second vacuum gauge.
优选的,所述出水连接管通过第四联接管与所述帘式超滤膜组件的下方连接,所述第四联接管上设有调节阀,所述出水连接管在与所述第四联接管的连接处的两侧均设有调节阀,所述出水连接管上还设有第二取样水龙头。Preferably, the outlet connecting pipe is connected to the bottom of the curtain ultrafiltration membrane module through a fourth connecting pipe, and a regulating valve is provided on the fourth connecting pipe, and the outlet connecting pipe is connected with the fourth connecting pipe. Adjusting valves are provided on both sides of the joint of the pipe, and a second sampling faucet is also provided on the water outlet connecting pipe.
优选的,还包括清洗剂药箱、清洗剂加药管、自来水连接管、射水器和第三联接管,所述清洗剂药箱通过所述清洗剂加药管与所述射水器连接,所述清洗剂加药管上设有清洗剂调节阀,所述自来水连接管与所述射水器连接所述自来水连接管上设有调节阀,所述射水器通过第三联接管与所述吸水管连接。Preferably, it also includes a detergent medicine box, a detergent dosing pipe, a running water connection pipe, a water injector and a third connecting pipe, the detergent medicine box is connected to the water injector through the detergent dosing pipe, so The cleaning agent dosing pipe is provided with a cleaning agent regulating valve, and the tap water connecting pipe is connected with the water ejector. The tap water connecting pipe is provided with a regulating valve, and the water ejector is connected with the water suction pipe connect.
优选地,Preferably,
本实用新型的洗浴水深度净化系统能够将絮凝、气浮、消毒、膜分离的处理方式集成在一个反应器装置内,利用加药絮凝、臭氧消毒和气浮、超滤膜的净化,完成洗浴池内水质的多重净化反应,整个装置具有使用简单易操作、占地面积小,无毒无残留,水量循环利用率高,节水节能的特点。本实用新型通过使用混凝剂和絮凝剂与水体充分混合后,使水中可溶胶类物质(如脂肪之类),改变电位,失去稳定,脱稳的胶体颗粒在混合时相互碰撞、凝聚,使细小胶体颗粒成为较大的絮体,进一步吸附悬浮颗粒、细菌,也就是使洗浴水逐渐增大油污绒体的过程。这些绒体被截留在超滤膜外面,超滤膜只允许溶液中的溶剂 (如水分子)、无机盐及小分子有机物透过,而将溶液中的悬浮物、胶体、蛋白质和微生物等大分子物质截留,从而达到净化和分离的目的。膜表面的污染物在一定时间以后经反冲洗除掉,以达到改善洗浴池水质的目的。而水中的一些人体表皮的细菌、携带的病毒和污垢、以及色、嗅、味和酚氯等大多不溶于水的污染物,可通过臭氧的强氧化性可以分解杀灭细菌,分解难生物降解的有机物和三致物质,改善水质却不会造成二次污染。The deep purification system for bath water of the utility model can integrate the treatment methods of flocculation, air flotation, disinfection and membrane separation into one reactor device, and use the flocculation with medicine, ozone disinfection and purification of air flotation and ultrafiltration membrane to complete the cleaning in the bathing pool. Multiple purification reactions of water quality, the whole device has the characteristics of simple use and operation, small footprint, non-toxic and no residue, high water recycling rate, water saving and energy saving. The utility model uses the coagulant and flocculant to fully mix the water body, so that the soluble colloidal substances (such as fat) in the water change the potential, lose stability, and the destabilized colloidal particles collide with each other and coagulate during mixing, so that Small colloidal particles become larger flocs, which further absorb suspended particles and bacteria, which is the process of gradually increasing the oily fluff in the bath water. These villi are trapped outside the ultrafiltration membrane. The ultrafiltration membrane only allows solvents (such as water molecules), inorganic salts, and small molecule organic substances in the solution to pass through, while macromolecules such as suspended solids, colloids, proteins, and microorganisms in the solution are allowed to pass through. Substance interception, so as to achieve the purpose of purification and separation. The pollutants on the surface of the membrane are removed by backwashing after a certain period of time, so as to achieve the purpose of improving the water quality of the bathing pool. In the water, some human skin bacteria, viruses and dirt carried, as well as color, smell, taste and phenolic chlorine and other water-insoluble pollutants can be decomposed and killed by the strong oxidation of ozone, which is difficult to biodegrade. Organic matter and three-causing substances can improve water quality without causing secondary pollution.
附图说明Description of drawings
图1为本实用新型实施例的浴室水深度净化一体化设备的剖视结构示意图。Fig. 1 is a schematic cross-sectional structure diagram of an integrated equipment for deep purification of bathroom water according to an embodiment of the present invention.
图中,1:多功能介质泵;2:进水管;3:第一真空表;4:调节阀;5:调节阀;6:底阀;7:水池;8:臭氧进气管;9:臭氧调节阀;10:臭氧流量计; 11:臭氧发生器;12:混凝剂药箱;13:混凝剂吸药管;14:混凝剂计量泵; 15:混凝剂进药管;16:第一阀门;17:出水管;18:调节阀;19:压力表; 20:流量计;21:调节阀;22:第一取样水龙头;23:第一联接管;24:管道混合器;25:调节阀;26:絮凝剂药箱;27:絮凝剂吸药管;28:絮凝剂计量泵;29:絮凝剂进药管;30:第二阀门;31:第二联接管;32:出口;33:第一隔板;34:第二隔板;35:第三隔板;36:出浮渣口;37:浮渣收集槽;38:浮渣排出管;39:吸水泵;40:吸水管;41:第二真空表;42:调节阀;43:帘式超滤膜组件;44:出水连接管;45:调节阀;46:调节阀;47:第二取样水龙头;48:集水槽;49:回流平衡管;50:净化后出水管;51:清洗剂药箱; 52:清洗剂加药管;53:清洗剂调节阀;54:水射器;55:自来水连接管;56:调节阀;57:第三联接管;58:第四联接管;59:调节阀;60:排空管;61:调节阀;62:设备支脚;63:设备箱体。In the figure, 1: Multifunctional medium pump; 2: Water inlet pipe; 3: First vacuum gauge; 4: Regulating valve; 5: Regulating valve; 6: Bottom valve; 7: Pool; 8: Ozone inlet pipe; 9: Ozone Regulating valve; 10: Ozone flow meter; 11: Ozone generator; 12: Coagulant medicine box; 13: Coagulant suction pipe; 14: Coagulant metering pump; 15: Coagulant feed pipe; 16 : first valve; 17: outlet pipe; 18: regulating valve; 19: pressure gauge; 20: flow meter; 21: regulating valve; 22: first sampling faucet; 23: first connecting pipe; 24: pipeline mixer; 25: regulating valve; 26: flocculant medicine box; 27: flocculant suction pipe; 28: flocculant metering pump; 29: flocculant feed pipe; 30: second valve; 31: second connecting pipe; 32: Exit; 33: first partition; 34: second partition; 35: third partition; 36: scum outlet; 37: scum collection tank; 38: scum discharge pipe; 39: suction pump; 40 : Suction pipe; 41: Second vacuum gauge; 42: Regulating valve; 43: Curtain ultrafiltration membrane module; 44: Outlet connecting pipe; 45: Regulating valve; 46: Regulating valve; 47: Second sampling faucet; 48: Sump; 49: Return balance pipe; 50: Outlet pipe after purification; 51: Cleaning agent tank; 52: Cleaning agent dosing pipe; 53: Cleaning agent regulating valve; 54: Water injector; 55: Tap water connecting pipe; 56: regulating valve; 57: third connecting pipe; 58: fourth connecting pipe; 59: regulating valve; 60: emptying pipe; 61: regulating valve; 62: equipment feet; 63: equipment box.
具体实施方式Detailed ways
下面结合附图和实施例对本实用新型的实施方式作进一步详细描述。以下实施例用于说明本实用新型,但不能用来限制本实用新型的范围。The implementation of the present utility model will be further described in detail below in conjunction with the accompanying drawings and examples. The following examples are used to illustrate the utility model, but cannot be used to limit the scope of the utility model.
在本实用新型的描述中,需要说明的是,术语“中心”、“纵向”、“横向”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本实用新型和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本实用新型的限制。此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性。In the description of the present utility model, it should be noted that the terms "center", "longitudinal", "transverse", "upper", "lower", "front", "rear", "left", "right", The orientations or positional relationships indicated by "vertical", "horizontal", "top", "bottom", "inner", "outer", etc. are based on the orientation or positional relationships shown in the drawings, and are only for the convenience of describing the present invention. Novel and simplified descriptions do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operate in a specific orientation, and therefore should not be construed as limiting the utility model. In addition, the terms "first" and "second" are used for descriptive purposes only, and should not be understood as indicating or implying relative importance.
在本实用新型的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本实用新型中的具体含义。此外,在本实用新型的描述中,除非另有说明,“多个”的含义是两个或两个以上。In the description of the present utility model, it should be noted that, unless otherwise clearly stipulated and limited, the terms "installation", "connection" and "connection" should be understood in a broad sense, for example, it can be a fixed connection or a flexible connection. Detachable connection, or integral connection; it can be mechanical connection or electrical connection; it can be direct connection or indirect connection through an intermediary, and it can be the internal communication of two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in the present utility model in specific situations. In addition, in the description of the present utility model, unless otherwise specified, "plurality" means two or more.
如图1所示,本实施例的洗浴水深度净化系统包括:进水管2、混凝剂药箱 12、混凝剂进药管15、臭氧发生器11、臭氧进气管8、多功能介质泵1、出水管 17、第二联接管31、絮凝剂药箱26、絮凝剂进药管29、管道混合器24、沉淀分离区、出浮渣口36、浮渣收集槽37、集水槽48、浮渣排出管38、帘式超滤膜组件43、排空管60、吸水管40、吸水泵39、出水连接管44和净化后出水管50。As shown in Figure 1, the deep purification system of bath water of the present embodiment comprises: water inlet pipe 2, coagulant medicine box 12, coagulant medicine feeding pipe 15, ozone generator 11, ozone inlet pipe 8, multifunctional medium pump 1. Outlet pipe 17, second connecting pipe 31, flocculant medicine box 26, flocculant feed pipe 29, pipeline mixer 24, sedimentation separation area, scum outlet 36, scum collection tank 37, water collection tank 48, Scum discharge pipe 38 , curtain ultrafiltration membrane module 43 , emptying pipe 60 , water suction pipe 40 , water suction pump 39 , water outlet connection pipe 44 and purified water outlet pipe 50 .
进水管2的一端设在水池内,另一端与多功能介质泵1的进口连接,混凝剂药箱12通过混凝剂进药管15与进水管2连接,臭氧发生器11通过臭氧进气管8与多功能介质泵1的进口连接,多功能介质泵1的出口通过出水管17与管道混合器 24连接,絮凝剂药箱26通过絮凝剂进药管29与管道混合器24连接,管道混合器 24通过第二联接管31与沉淀分离区的下端连接,沉淀分离区的上端为排水开口,出浮渣口36位于沉淀分离区的上方,出浮渣口36的外侧依次设有浮渣收集槽37 和集水槽48,浮渣排出管38与浮渣收集槽37连接,帘式超滤膜组件43位于沉淀分离区的下方,排空管60位于帘式超滤膜组件43的下方,帘式超滤膜组件43通过吸水管40与吸水泵39的进口连接,吸水泵39的出口通过出水连接管44与集水槽48连接,净化后出水管50的一端与集水槽48连接,另一端与水池7连接。One end of the water inlet pipe 2 is set in the pool, and the other end is connected to the inlet of the multifunctional medium pump 1. The coagulant medicine box 12 is connected to the water inlet pipe 2 through the coagulant medicine inlet pipe 15. The ozone generator 11 is connected to the water inlet pipe 1 through the ozone inlet pipe. 8 is connected to the inlet of the multifunctional medium pump 1, the outlet of the multifunctional medium pump 1 is connected to the pipeline mixer 24 through the water outlet pipe 17, the flocculant medicine box 26 is connected to the pipeline mixer 24 through the flocculant feed pipe 29, and the pipeline mixes The device 24 is connected to the lower end of the sedimentation separation area through the second connecting pipe 31, the upper end of the sedimentation separation area is a drainage opening, and the scum outlet 36 is located above the sedimentation separation area, and the outside of the scum outlet 36 is sequentially provided with scum collectors. Groove 37 and sump 48, scum discharge pipe 38 is connected with scum collecting tank 37, and curtain type ultrafiltration membrane assembly 43 is positioned at the below of precipitation separation area, and emptying pipe 60 is positioned at the below of curtain type ultrafiltration membrane assembly 43, and curtain type ultrafiltration membrane assembly 43 is positioned at Type ultrafiltration membrane assembly 43 is connected with the inlet of water suction pump 39 by water suction pipe 40, and the outlet of water suction pump 39 is connected with sump 48 by water outlet connection pipe 44, and one end of outlet pipe 50 is connected with sump 48 after purification, and the other end is connected with sump 48. The pool 7 is connected.
进水管2在水池7中的一端设有底阀6,进水管2在与混凝剂进药管15的连接处的两侧均设有调节阀4和调节阀5,进水管2上还设有第一真空表3。混凝剂进药管15通过混凝剂计量泵14及混凝剂吸药管13与混凝剂药箱12连接,混凝剂进药管15上还设有第一阀门16,吸进混凝剂药液后通过混凝剂进药管15和第一阀门16进入进水管2中,参与混凝反应,絮凝剂进药管29通过絮凝剂计量泵28及絮凝剂吸药管27与絮凝剂药箱26连接,絮凝剂进药管29上还设有第二阀门30,吸进絮凝剂药液后通过絮凝剂进药管29和第二阀门30进入管道混合器24中,参与絮凝反应。臭氧进气管8上设有臭氧流量计10和臭氧调节阀9。出水管17上设有调节阀18、压力表19和流量计20,流量计20通过第一联接管23与管道混合器24 连接,第一联接管23上设有调节阀21和第一取样水龙头22。第二联接管31上设有调节阀25,第二联接管31的出口32位于沉淀分离器的下部。集水槽48通过回流平衡管49与设备箱体63的下部连接,经超滤膜组件净化后的出水通过吸水泵 39吸出后排入集水槽48内,集水槽48内设置回流平衡管49,净化后的水通过回流平衡管49回流至膜组件净化区,可实现进一步净化,而集水槽48外壁连接出水管50,使集水槽48内的水排出到水池7。吸水管40上设有调节阀42和第二真空表41。出水连接管44通过第四联接管58与帘式超滤膜组件43的下方连接,第四联接管58上设有调节阀59,出水连接管44在与第四联接管58的连接处的两侧均设有调节阀45和调节阀46,出水连接管44上还设有第二取样水龙头47。排空管 60上设有调节阀61。One end of the water inlet pipe 2 in the pool 7 is provided with a bottom valve 6, the water inlet pipe 2 is provided with a regulating valve 4 and a regulating valve 5 on both sides of the joint with the coagulant feeding pipe 15, and the water inlet pipe 2 is also provided with a regulating valve 4 and a regulating valve 5. There are 3 first vacuum gauges. The coagulant medicine feeding pipe 15 is connected with the coagulant medicine box 12 through the coagulant metering pump 14 and the coagulant medicine suction pipe 13, and the coagulant medicine feeding pipe 15 is also provided with a first valve 16 to suck in the mixed medicine. The coagulant medicine liquid enters the water inlet pipe 2 through the coagulant medicine feeding pipe 15 and the first valve 16, and participates in the coagulation reaction. The agent medicine box 26 is connected, and the second valve 30 is also arranged on the flocculant medicine inlet pipe 29, after sucking in the flocculant medicine liquid, enter the pipeline mixer 24 through the flocculant medicine inlet pipe 29 and the second valve 30, and participate in the flocculation reaction . An ozone flow meter 10 and an ozone regulating valve 9 are provided on the ozone inlet pipe 8 . The outlet pipe 17 is provided with a regulating valve 18, a pressure gauge 19 and a flowmeter 20, the flowmeter 20 is connected with the pipeline mixer 24 through the first connecting pipe 23, and the first connecting pipe 23 is provided with a regulating valve 21 and a first sampling faucet twenty two. A regulating valve 25 is provided on the second connecting pipe 31, and the outlet 32 of the second connecting pipe 31 is located at the lower part of the sedimentation separator. The sump 48 is connected to the lower part of the equipment box 63 through the backflow balance pipe 49, and the outlet water purified by the ultrafiltration membrane module is sucked out by the water suction pump 39 and then discharged into the sump 48. A backflow balance pipe 49 is arranged in the sump 48 to purify The final water flows back to the purification area of the membrane module through the return balance pipe 49, which can realize further purification, and the outer wall of the sump 48 is connected to the outlet pipe 50, so that the water in the sump 48 is discharged to the pool 7. The water suction pipe 40 is provided with a regulating valve 42 and a second vacuum gauge 41 . The outlet connecting pipe 44 is connected to the bottom of the curtain ultrafiltration membrane assembly 43 through the fourth connecting pipe 58, the fourth connecting pipe 58 is provided with a regulating valve 59, and the outlet connecting pipe 44 is connected to the fourth connecting pipe 58 at the two ends of the joint. A regulating valve 45 and a regulating valve 46 are provided on each side, and a second sampling faucet 47 is also provided on the outlet connecting pipe 44 . The emptying pipe 60 is provided with a regulating valve 61.
本实施例中的洗浴水深度净化系统还包括:设备箱体63,沉淀分离区和帘式超滤膜组件43均设在设备箱体63内,沉淀分离区为由第一隔板33围成的下窄上宽的料斗状结构,第一隔板33的内侧设有挡板结构,来水从下口进入从上口溢出第一隔板33内侧按有与隔板垂直的小挡板,进水后水流向上而小挡板起到挡流作用使在此形成旋流状态,有利于水体充分混合絮凝的作用。超滤是一种能将溶液进行净化和分离的技术,超滤膜系统是以超滤膜丝为过滤介质,膜两侧的压力差为驱动力的溶液分离装置,超滤膜只允许溶液中的溶剂(如水分子)、无机盐及小分子有机物透过,而溶液中的悬浮物、胶体、蛋白质和微生物等大分子物质截留,从而达到净化和分离的目的。设备箱体63的上端通过第二隔板 34形成出浮渣口36,第二隔板34上通过第三挡板35隔成浮渣收集槽37和集水槽 48,设备箱体63的下端为收集槽结构,设备箱体63的下端还设有设备支脚62。The deep purification system for bathing water in this embodiment also includes: an equipment box body 63, the sedimentation separation area and the curtain ultrafiltration membrane assembly 43 are all arranged in the equipment box body 63, and the precipitation separation area is surrounded by the first dividing plate 33 The lower narrow upper wide hopper-shaped structure, the inner side of the first partition 33 is provided with a baffle structure, incoming water enters from the lower port and overflows from the upper port. After entering the water, the water flows upwards and the small baffle acts as a flow barrier to form a swirl state here, which is conducive to the full mixing and flocculation of the water body. Ultrafiltration is a technology that can purify and separate solutions. The ultrafiltration membrane system uses ultrafiltration membrane filaments as the filter medium, and the pressure difference on both sides of the membrane is the driving force for the solution separation device. The ultrafiltration membrane only allows Solvents (such as water molecules), inorganic salts and small molecular organic substances pass through, while suspended solids, colloids, proteins, microorganisms and other macromolecular substances in the solution are intercepted, so as to achieve the purpose of purification and separation. The upper end of equipment box body 63 forms scum mouth 36 by second dividing plate 34, and the second dividing plate 34 is separated into scum collecting tank 37 and sump 48 by third baffle plate 35, and the lower end of equipment box body 63 is The collection tank structure, the lower end of the equipment box 63 is also provided with equipment feet 62 .
本实施例的洗浴水深度净化系统还包括:清洗剂药箱51、清洗剂加药管52、自来水连接管55、射水器54和第三联接管57,清洗剂药箱51通过清洗剂加药管 52与射水器54连接,清洗剂加药管52上设有清洗剂调节阀53,自来水连接管55 与射水器54连接自来水连接管55上设有调节阀,射水器54通过第三联接管57与吸水管40连接。The bathing water deep purification system of the present embodiment also includes: a cleaning agent medicine box 51, a cleaning agent dosing pipe 52, a tap water connecting pipe 55, a water jet 54 and a third connecting pipe 57, and the cleaning agent medicine box 51 is fed with a cleaning agent The pipe 52 is connected with the water ejector 54, and the cleaning agent dosing pipe 52 is provided with a cleaning agent regulating valve 53, and the tap water connecting pipe 55 is connected with the water ejector 54. 57 is connected with suction pipe 40.
本实施例的洗浴水深度净化系统的工作原理为:打开水池7中进水底阀6、调节阀4、调节阀5、第一阀门16和臭氧调节阀9,开启多功能介质泵1、混凝剂计量泵14、臭氧发生器11,所述多功能介质泵1将水池7内的水、混凝剂进药管 15进入的混凝剂PAC同时吸入进水管2中,通过相应调节阀调节好进水流量、PAC 加药量、臭氧进气量,通过多功能介质泵1一同吸入,所述多功能介质泵的前端设有真空表3,后端有压力表19和流量计20,打开所述流量计前后调节阀18和调节阀21,可通过取样水龙头22水样检验,调节好相应流量后流入管道混合器24,再打开第二阀门30、絮凝剂计量泵28,调节好进药量后,絮凝剂PAM通过絮凝剂进药管29加入PAM到所述管道混合器中,此时可将原水、PAC、PAM、臭氧充分混合,打开调节阀25,出水通过混合器后的联接管31和出口32进入一体化设备的沉淀分离区中心底部。在沉淀分离区进水后,水流向上而小挡板起到挡流作用使在此区形成旋流状态,水体充分接触混合,PAC通过它或它的水解产物的压缩双电层、电性中和、卷带网捕以及吸附架桥等四个方面的作用,将能被氧化剂氧化造成COD的颗粒物沉淀下来;而PAM是有机高分子絮凝剂,具有在颗粒间形成更大的絮体由此产生巨大表面吸附力,使细小胶体颗粒成为较大的絮体,进一步吸附悬浮颗粒、细菌的作用,也就是使洗浴水逐渐增大油污绒体的过程;而臭氧气体在沉淀分离区中形成大量细微气泡,气泡的上浮作用使悬浮状态的污染物上浮至水的表面,浮渣通过出浮渣口36溢流到浮渣收集槽37内,通过浮渣排出管38排出设备;而水中的一些人体表皮的细菌、携带的病毒和污垢、以及色、嗅、味和酚氯等大多不溶于水的污染物,通过臭氧的强氧化性可以分解杀灭细菌,分解难生物降解的有机物和三致物质;分离室中的混合液被絮凝和杀菌消毒作用以后,继续下流至超滤膜净化区,打开调节阀42、调节阀45、调节阀46,开启吸水泵39,调节真空表41,超滤膜以膜两侧的压力差为驱动力,以超滤膜为过滤介质,在一定的压力下,当原液流过膜表面时,超滤膜表面密布的许多细小的微孔只允许水及小分子物质通过而成为透过液,而原液中体积大于膜表面微孔径的物质则被截留在膜的进液侧,实现了对原液的净化、分离和浓缩的目的,被沉降在装置底部的污泥通过排空管60与调节阀161排出;净水被吸水泵39经吸水管40吸入后通过出水连接管44排出,出水连接管44连接取样水龙头47,经取样检验后排入集水槽48中。所述集水槽内设置回流平衡管 49,净化后的水通过回流平衡管49回流至膜组件净化区,可实现进一步净化;而集水槽外壁连接出水管50,使所述集水槽48内的水排出到水池7供给循环使用。The working principle of the deep purification system for bathing water in this embodiment is as follows: open the water inlet bottom valve 6, regulating valve 4, regulating valve 5, first valve 16 and ozone regulating valve 9 in the pool 7, open the multifunctional medium pump 1, coagulate agent metering pump 14, ozone generator 11, the multi-functional medium pump 1 sucks the water in the pool 7 and the coagulant PAC that enters the coagulant medicine feeding pipe 15 into the water inlet pipe 2 at the same time, and adjusts it through the corresponding regulating valve Inlet water flow, PAC dosing amount, and ozone air intake are sucked together by multifunctional medium pump 1. The front end of the multifunctional medium pump is provided with a vacuum gauge 3, and the rear end is provided with a pressure gauge 19 and a flow meter 20. The regulating valve 18 and the regulating valve 21 before and after the flow meter can be checked by sampling the tap 22 water sample, and after the corresponding flow is adjusted, it flows into the pipeline mixer 24, and then the second valve 30 and the flocculant metering pump 28 are opened to adjust the amount of medicine Finally, the flocculant PAM is added to the pipeline mixer through the flocculant feed pipe 29, at this time, the raw water, PAC, PAM, and ozone can be fully mixed, the regulating valve 25 is opened, and the outlet water passes through the connecting pipe 31 behind the mixer. And the outlet 32 enters the center bottom of the precipitation separation zone of the integrated equipment. After water enters the sedimentation separation area, the water flows upwards and the small baffle acts as a barrier to form a swirling flow state in this area. The water body is fully contacted and mixed, and PAC passes through it or its hydrolyzed products. And, coiled net catch and adsorption bridging, the particles that can be oxidized by the oxidant to cause COD will be precipitated; and PAM is an organic polymer flocculant, which has the ability to form larger flocs between particles. Generate huge surface adsorption force, make fine colloidal particles become larger flocs, and further absorb suspended particles and bacteria, that is, the process of gradually increasing oily fluff in bath water; while ozone gas forms a large amount of flocs in the precipitation separation area Fine air bubbles, the floating effect of the air bubbles make the pollutants in the suspended state float to the surface of the water, and the scum overflows into the scum collecting tank 37 through the scum outlet 36, and is discharged from the equipment through the scum discharge pipe 38; while some in the water Bacteria, viruses and dirt carried by the human skin, as well as color, smell, taste, phenolic chlorine and other water-insoluble pollutants, can be decomposed and killed by the strong oxidation of ozone, and decompose refractory organic matter and three pathogens Substance; After the mixed solution in the separation chamber is flocculated and sterilized, it continues to flow down to the ultrafiltration membrane purification area, and the regulating valve 42, regulating valve 45, and regulating valve 46 are opened, the suction pump 39 is opened, the vacuum gauge 41 is adjusted, and the ultrafiltration The membrane is driven by the pressure difference on both sides of the membrane, and the ultrafiltration membrane is used as the filter medium. Under a certain pressure, when the stock solution flows through the surface of the membrane, many small pores on the surface of the ultrafiltration membrane can only allow water and small Molecular substances pass through to become the permeate, while the substances in the original solution with a volume larger than the micropore diameter of the membrane surface are trapped on the liquid inlet side of the membrane, realizing the purpose of purification, separation and concentration of the original solution, and the sewage settled at the bottom of the device The mud is discharged through the emptying pipe 60 and the regulating valve 161; the clean water is sucked by the water suction pump 39 through the water suction pipe 40 and discharged through the water outlet connecting pipe 44, and the water outlet connecting pipe 44 is connected to the sampling faucet 47, and is discharged into the sump 48 after sampling inspection . A backflow balance pipe 49 is arranged in the sump, and the purified water flows back to the purification area of the membrane module through the backflow balance pipe 49 to realize further purification; Discharge to pool 7 for recycling.
由于在运行过程中,进水中的颗粒物会逐渐累积在膜的外表面,从而使过滤系统的跨膜压差增加。膜组件为了保持一定的膜过通量和延长寿命,超滤系统要停止过滤进行周期性的反洗。反洗过程就是将超滤产水或自来水反向透过中空纤维膜,擦洗中空纤维膜丝表面去除沉积物。反洗启动后,进水调节阀25 关闭,吸水泵39继续运行,打开清洗剂调节阀53、水射器54、自来水连接调节阀56,使吸水泵39吸入集水槽48中的净水后,在出水时与同时加入一定比例的清洗药剂相混合,一同通过吸水管多功能介质泵40反向进入膜中,对膜进行短时间浸泡后,反洗水从清液侧进入超滤纤维中透过膜流向浓水侧,通过大流量的反洗水,将膜孔道和帘式超滤膜表面的污染物冲洗掉,并通过排空管60和调节阀61将被冲洗掉的污染物排出。During the operation, the particles in the feed water will gradually accumulate on the outer surface of the membrane, which will increase the transmembrane pressure difference of the filtration system. In order to maintain a certain membrane flux and prolong the life of the membrane module, the ultrafiltration system should stop the filtration and perform periodic backwashing. The backwashing process is to reversely pass the ultrafiltration water or tap water through the hollow fiber membrane, and scrub the surface of the hollow fiber membrane to remove sediment. After the backwash starts, the water inlet regulating valve 25 is closed, and the suction pump 39 continues to run, and the cleaning agent regulating valve 53, the water injector 54, the tap water connection regulating valve 56 are opened, and after the water suction pump 39 is sucked into the clean water in the sump 48, When the water is discharged, it is mixed with a certain proportion of cleaning agents, and together they enter the membrane in the opposite direction through the multi-functional medium pump 40 of the water suction pipe. It flows through the membrane to the concentrated water side, and the pollutants on the surface of the membrane pores and the curtain ultrafiltration membrane are washed away by a large flow of backwash water, and the washed pollutants are discharged through the emptying pipe 60 and the regulating valve 61.
本实用新型的洗浴水深度净化系统能够将絮凝、气浮、消毒、膜分离的处理方式集成在一个反应器装置内,利用加药絮凝、臭氧消毒和气浮、超滤膜的净化,完成洗浴池内水质的多重净化反应,整个装置具有使用简单易操作、占地面积小,无毒无残留,水量循环利用率高,节水节能的特点。本实用新型通过使用混凝剂和絮凝剂与水体充分混合后,使水中可溶胶类物质(如脂肪之类),改变电位,失去稳定,脱稳的胶体颗粒在混合时相互碰撞、凝聚,使细小胶体颗粒成为较大的絮体,进一步吸附悬浮颗粒、细菌,也就是使洗浴水逐渐增大油污绒体的过程。这些绒体被截留在超滤膜外面,超滤膜只允许溶液中的溶剂 (如水分子)、无机盐及小分子有机物透过,而将溶液中的悬浮物、胶体、蛋白质和微生物等大分子物质截留,从而达到净化和分离的目的。膜表面的污染物在一定时间以后经反冲洗除掉,以达到改善洗浴池水质的目的。而水中的一些人体表皮的细菌、携带的病毒和污垢、以及色、嗅、味和酚氯等大多不溶于水的污染物,可通过臭氧的强氧化性可以分解杀灭细菌,分解难生物降解的有机物和三致物质,改善水质却不会造成二次污染。The deep purification system for bath water of the utility model can integrate the treatment methods of flocculation, air flotation, disinfection and membrane separation into one reactor device, and use the flocculation with medicine, ozone disinfection and purification of air flotation and ultrafiltration membrane to complete the cleaning in the bathing pool. Multiple purification reactions of water quality, the whole device has the characteristics of simple use and operation, small footprint, non-toxic and no residue, high water recycling rate, water saving and energy saving. The utility model uses the coagulant and flocculant to fully mix the water body, so that the soluble colloidal substances (such as fat) in the water change the potential, lose stability, and the destabilized colloidal particles collide with each other and coagulate during mixing, so that Small colloidal particles become larger flocs, which further absorb suspended particles and bacteria, which is the process of gradually increasing the oily fluff in the bath water. These villi are trapped outside the ultrafiltration membrane. The ultrafiltration membrane only allows solvents (such as water molecules), inorganic salts, and small molecule organic substances in the solution to pass through, while macromolecules such as suspended solids, colloids, proteins, and microorganisms in the solution are allowed to pass through. Substance interception, so as to achieve the purpose of purification and separation. The pollutants on the surface of the membrane are removed by backwashing after a certain period of time, so as to achieve the purpose of improving the water quality of the bathing pool. In the water, some human skin bacteria, viruses and dirt carried, as well as color, smell, taste and phenolic chlorine and other water-insoluble pollutants can be decomposed and killed by the strong oxidation of ozone, which is difficult to biodegrade. Organic matter and three-causing substances can improve water quality without causing secondary pollution.
本实用新型的实施例是为了示例和描述起见而给出的,而并不是无遗漏的或者将本实用新型限于所公开的形式。很多修改和变化对于本领域的普通技术人员而言是显而易见的。选择和描述实施例是为了更好说明本实用新型的原理和实际应用,并且使本领域的普通技术人员能够理解本实用新型从而设计适于特定用途的带有各种修改的各种实施例。The embodiments of the invention have been presented for purposes of illustration and description, but are not intended to be exhaustive or to limit the invention to the forms disclosed. Many modifications and changes will be apparent to those of ordinary skill in the art. The embodiment was chosen and described in order to better explain the principle and practical application of the invention, and to enable those of ordinary skill in the art to understand the invention and design various embodiments with various modifications suitable for particular purposes.
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