CN107487904A - A kind of iron content waste water pretreatment unit - Google Patents
A kind of iron content waste water pretreatment unit Download PDFInfo
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- CN107487904A CN107487904A CN201710933070.6A CN201710933070A CN107487904A CN 107487904 A CN107487904 A CN 107487904A CN 201710933070 A CN201710933070 A CN 201710933070A CN 107487904 A CN107487904 A CN 107487904A
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- 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
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- 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
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- 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
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
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- 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
- C02F1/70—Treatment of water, waste water, or sewage by reduction
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- 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
- C02F2001/007—Processes including a sedimentation step
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- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F2001/5218—Crystallization
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- 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
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
- C02F2101/203—Iron or iron compound
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- 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
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Abstract
本发明涉及一种含铁废水预处理装置,包括调节池、还原反应池、结晶沉淀池、流砂滤池和储水池,调节池、还原反应池、结晶沉淀池、流砂滤池和储水池依次连通;调节池包括调节池进水管和调节池出水管;还原反应池的中上部设有还原反应池进水管、上部设有还原剂添加计量系统、中部设有还原反应池搅拌器、底部设有还原反应池出水管;结晶沉淀池包括连接结晶沉淀池出水管的溢水堰和连接流砂滤池进水管的出水管;流砂滤池设有流砂滤池进水管和用于排出处理后水的流砂滤池出水管,包括布水区、洗砂区和砂滤区;流砂滤池过滤处理后的水进入储水池。
The invention relates to a pretreatment device for iron-containing wastewater, comprising a regulating tank, a reducing reaction tank, a crystallization sedimentation tank, a quicksand filter and a water storage tank, and the regulating tank, the reduction reaction tank, the crystallization sedimentation tank, the quicksand filter and the water storage tank are connected in sequence The adjustment tank includes the water inlet pipe of the adjustment tank and the water outlet pipe of the adjustment tank; the upper middle part of the reduction reaction tank is provided with the water inlet pipe of the reduction reaction tank, the upper part is provided with a reducing agent addition metering system, the middle part is provided with a reduction reaction tank agitator, and the bottom is provided with a reduction reaction tank The outlet pipe of the reaction tank; the crystallization sedimentation tank includes an overflow weir connected to the outlet pipe of the crystallization sedimentation tank and an outlet pipe connected to the inlet pipe of the quicksand filter; the quicksand filter is provided with a quicksand filter inlet pipe and a quicksand filter for discharging treated water The water outlet pipe includes the water distribution area, the sand washing area and the sand filter area; the water filtered by the quicksand filter enters the water storage tank.
Description
技术领域technical field
本发明涉及环保技术领域,具体涉及一种含铁废水预处理装置。The invention relates to the technical field of environmental protection, in particular to an iron-containing wastewater pretreatment device.
背景技术Background technique
在我国现行的《工业“三废”排放试行标准》中,铁的含量未作任何限制。但若将含铁废水直接排放,废水中存在的溶解性铁离子造成水体中的溶解氧迅速降低,排水呈赤橙色且浑浊,一旦进入生态循环中,会对生态安全与人类健康产生巨大危害。In my country's current "Industrial "Three Wastes" Discharge Trial Standards", there is no restriction on the content of iron. However, if the iron-containing wastewater is discharged directly, the dissolved iron ions in the wastewater will cause the dissolved oxygen in the water to decrease rapidly, and the drainage will be reddish orange and turbid. Once it enters the ecological cycle, it will cause great harm to ecological security and human health.
实际工程中含铁重金属废水主要来源于贵金属加工生产排水,主要包括矿山矿井排水、钢铁生产加工出水、部分金属蚀刻加工与电镀生产工艺出水等,这些加工生产过程中不同环节均会产生大量含有较高浓度不同形态的铁,属于难处理的一类废水。In actual engineering, the iron-containing heavy metal wastewater mainly comes from precious metal processing and production drainage, mainly including mine drainage, steel production and processing effluent, some metal etching processing and electroplating production process effluent, etc. Different links in these processing and production processes will produce a large number of High concentrations of iron in different forms belong to a class of wastewater that is difficult to treat.
中国专利《一种酸洗含铁废水的处理装置及处理办法》(专利号:201410288531.5)公开了一种酸洗含铁废水的处理装置及处理办法,可以对含铁废水进行处理。该发明通过隔油、中和曝气、精调pH、一次沉淀和二次沉淀,在中和曝气时,将块状石灰石分批送入中和曝气反应池,该装置具有简单易行、沉渣少等优点;但该专利存在以下缺点:块状石灰石分批送入中和曝气反应池增大了处理成本与运行费、加重了企业负担。Chinese patent "A treatment device and method for pickling iron-containing wastewater" (patent number: 201410288531.5) discloses a treatment device and method for pickling iron-containing wastewater, which can treat iron-containing wastewater. In this invention, through oil separation, neutralization and aeration, fine adjustment of pH, primary precipitation and secondary precipitation, block limestone is sent into the neutralization and aeration reaction tank in batches during neutralization and aeration. The device is simple and easy , less sediment, etc.; but this patent has the following disadvantages: massive limestone is sent into the neutralization aeration reaction tank in batches, which increases the treatment cost and operating cost, and increases the burden on the enterprise.
发明内容Contents of the invention
本发明要解决的技术问题是:为了解决上述含铁废水的处理问题,本发明提供一种含铁废水预处理装置。The technical problem to be solved by the present invention is: in order to solve the above-mentioned iron-containing wastewater treatment problem, the present invention provides an iron-containing wastewater pretreatment device.
本发明解决其技术问题所采用的技术方案是:一种含铁废水预处理装置,包括调节池、还原反应池、结晶沉淀池、流砂滤池和储水池,调节池、还原反应池、结晶沉淀池、流砂滤池和储水池依次连通。The technical scheme adopted by the present invention to solve the technical problem is: a kind of iron-containing wastewater pretreatment device, including adjustment tank, reduction reaction tank, crystallization sedimentation tank, quicksand filter tank and water storage tank, adjustment tank, reduction reaction tank, crystallization sedimentation tank The pool, the quicksand filter and the storage tank are connected in sequence.
所述的调节池包括调节池进水管和调节池出水管,用于调节废水的水质和水量。The regulating pond includes a regulating pond inlet pipe and a regulating pond outlet pipe for regulating the water quality and quantity of the waste water.
所述的还原反应池的中上部设置有还原反应池进水管,还原反应池的上部设置有还原剂添加计量系统;还原反应池的中部设置有还原反应池搅拌器,还原反应池的底部设置有还原反应池出水管。The middle and upper part of the reduction reaction tank is provided with a reduction reaction tank water inlet pipe, and the upper part of the reduction reaction tank is provided with a reducing agent addition metering system; the middle part of the reduction reaction tank is provided with a reduction reaction tank agitator, and the bottom of the reduction reaction tank is provided with a Restore the outlet pipe of the reaction pool.
所述的还原剂添加计量系统添加的还原剂为亚硫酸氢钠。The reducing agent added by the reducing agent adding metering system is sodium bisulfite.
所述的结晶沉淀池包括结晶区和沉淀区。The crystallization sedimentation tank includes a crystallization area and a precipitation area.
所述的结晶区的中上部设置有结晶沉淀池进水管,结晶区的上部设置有结晶诱导剂添加计量系统;结晶区的中下部设置有结晶区搅拌器。The upper middle part of the crystallization area is provided with a water inlet pipe for a crystallization sedimentation tank, the upper part of the crystallization area is provided with a crystallization inducer adding metering system; the middle and lower part of the crystallization area is provided with a crystallization area stirrer.
所述的结晶诱导剂添加计量系统添加的结晶诱导剂为涂敷碳酸钠的石英砂;所述的结晶诱导剂的制备过程为:The crystallization inducer added by the added metering system of the crystallization inducer is quartz sand coated with sodium carbonate; the preparation process of the crystallization inducer is:
①将石英砂放入1mol/L的碳酸钠溶液中浸泡,在摇床中振荡24h;① Soak the quartz sand in 1mol/L sodium carbonate solution and shake it in a shaker for 24 hours;
②将浸泡后的石英砂过滤;② Filter the soaked quartz sand;
③将过滤后的石英砂用去离子水清洗;③ Wash the filtered quartz sand with deionized water;
④将清洗后的石英干燥,制得结晶诱导剂。④ drying the cleaned quartz to obtain a crystallization inducer.
结晶区和沉淀区之间设有隔板,该隔板与结晶沉淀池的内壁形成作为废水进入沉淀区的废水流道,沉淀区的出口处设有结晶沉淀池三相分离器,沉淀区的出口上部设有结晶沉淀池溢水堰,沉淀区底部设计成锥形结构,在锥形结构底部设置有沉淀物排放阀。结晶沉淀池溢水堰连接结晶沉淀池出水管,结晶沉淀池出水管连接流砂滤池进水管。There is a partition between the crystallization area and the sedimentation area, and the partition and the inner wall of the crystallization sedimentation tank form a waste water flow channel that enters the sedimentation area as wastewater. The upper part of the outlet is equipped with a crystallization sedimentation tank overflow weir, the bottom of the sedimentation area is designed as a conical structure, and a sediment discharge valve is set at the bottom of the conical structure. The overflow weir of the crystallization sedimentation tank is connected to the outlet pipe of the crystallization sedimentation tank, and the outlet pipe of the crystallization sedimentation tank is connected to the water inlet pipe of the quicksand filter.
所述流砂滤池包括流砂滤池进水管和用于排出处理后水的流砂滤池出水管,所述的流砂滤池包括布水区、洗砂区和砂滤区;所述的布水区位于流砂滤池的下部,布水区设有流砂滤池布水管,流砂滤池布水管连接流砂滤池进水管,为了废水处理的效果更好,所述的流砂滤池布水管设置成同心圆形状,流砂滤池布水管上具有向下辐射出水口;所述的洗砂区位于流砂滤池的中心,为圆柱形筒状结构,圆柱形筒状结构下端开口位于流砂滤池的最底部,圆柱形筒状结构上端开口位于流砂滤池的上部,洗砂区的中部设有气提管,气提管连接流砂滤池外的流砂滤池鼓风机,洗砂区的上部设有砂水沉淀分离区,砂水沉淀分离区的上部设有洗砂区溢水堰,洗砂区溢水堰连接洗砂水排放管和结晶沉淀池进水管,砂水沉淀分离区的下部设有回砂通道;所述的砂滤区位于洗砂区的外围,砂滤区内充填有细砂,砂滤区上部设有砂滤区溢水堰,砂滤区溢水堰连接流砂滤池出水管,流砂滤池过滤处理后的水进入储水池。The quicksand filter includes a quicksand filter inlet pipe and a quicksand filter outlet pipe for discharging treated water, and the quicksand filter includes a water distribution area, a sand washing area and a sand filter area; the water distribution area Located at the lower part of the quicksand filter, the water distribution area is provided with a quicksand filter water distribution pipe, and the quicksand filter water distribution pipe is connected to the quicksand filter water inlet pipe. In order to achieve a better wastewater treatment effect, the quicksand filter water distribution pipes are arranged in concentric circles Shape, the water distribution pipe of the quicksand filter has a downward radiating water outlet; the sand washing area is located in the center of the quicksand filter, and is a cylindrical cylindrical structure, and the lower end opening of the cylindrical cylindrical structure is located at the bottom of the quicksand filter. The upper opening of the cylindrical cylindrical structure is located on the upper part of the quicksand filter, and the middle part of the sand washing area is equipped with an air lift pipe, which is connected to the quick sand filter blower outside the quick sand filter, and the upper part of the sand washing area is equipped with sand and water sedimentation and separation The upper part of the sand-water sedimentation separation area is provided with an overflow weir in the sand washing area, and the overflow weir in the sand washing area is connected to the sand washing water discharge pipe and the water inlet pipe of the crystallization sedimentation tank, and the lower part of the sand-water sedimentation separation area is provided with a sand return channel; The sand filter area is located on the periphery of the sand washing area. The sand filter area is filled with fine sand. The sand filter area is equipped with an overflow weir on the upper part of the sand filter area. The overflow weir in the sand filter area is connected to the outlet pipe of the quicksand filter. water into the storage tank.
一种采用上述含铁废水处理装置进行废水处理的方法,具有如下步骤:A method for wastewater treatment using the above-mentioned iron-containing wastewater treatment device has the following steps:
①含铁废水通过调节池进水管进入调节池,调节水质、水量和pH值。①The iron-containing wastewater enters the regulating pond through the inlet pipe of the regulating pond to adjust the water quality, water quantity and pH value.
②调节后的废水进入还原反应池,还原剂添加计量系统添加还原剂亚硫酸氢钠,还原反应池搅拌器对废水进行搅拌,将废水中的三价铁离子还原成易发生异相结晶的二价铁离子。②The adjusted wastewater enters the reduction reaction tank, the reducing agent addition metering system adds the reducing agent sodium bisulfite, and the agitator in the reduction reaction tank stirs the wastewater to reduce the ferric ions in the wastewater to ferric ions that are prone to heterogeneous crystallization. Valence iron ions.
③还原反应后的废水通过结晶沉淀池进水管进入结晶区,结晶诱导剂添加计量系统添加结晶诱导剂,结晶区搅拌器对废水进行搅拌混合。③The waste water after the reduction reaction enters the crystallization area through the water inlet pipe of the crystallization sedimentation tank, the crystallization inducer adding metering system adds the crystallization inducer, and the agitator in the crystallization area stirs and mixes the waste water.
④然后废水进入沉淀区的废水流道,废水发生结晶反应,结晶沉淀池三相分离器实现废水和固体的分离,沉淀物在重力的作用下下沉到沉淀区的下部,通过底部的沉淀物排放阀排出,沉淀后的废水通过结晶沉淀池溢水堰和结晶沉淀池出水管进入流砂滤池进水管。④ Then the wastewater enters the wastewater flow channel in the sedimentation area, and the wastewater undergoes a crystallization reaction. The three-phase separator in the crystallization sedimentation tank realizes the separation of wastewater and solids, and the sediment sinks to the lower part of the sedimentation area under the action of gravity, and passes through the sediment at the bottom The discharge valve is discharged, and the settled wastewater enters the water inlet pipe of the quicksand filter through the overflow weir of the crystallization sedimentation tank and the outlet pipe of the crystallization sedimentation tank.
⑤废水通过流砂滤池进水管、流砂滤池布水管进入流砂滤池的下部,流砂滤池布水管实现均匀布水,废水进入砂滤区,废水中的污染物被进一步过滤,然后废水穿过砂滤区由砂滤区溢水堰和流砂滤池出水管流出,进入储水池;流砂滤池鼓风机产生的气流带动洗砂区中的砂和水向上流动,同时对砂进行冲洗,气流带动洗砂区中的砂和水进入砂水沉淀分离区,由于砂和水的比重不同,细砂沉淀下去并通过回砂通道流入砂滤区,实现砂滤区中的细砂不断从上往下的移动,砂水沉淀分离区中的水通过洗砂区溢水堰和洗砂水排放管进入结晶沉淀池进行再处理。⑤Wastewater enters the lower part of the quicksand filter through the water inlet pipe of the quicksand filter and the water distribution pipe of the quicksand filter. The water distribution pipe of the quicksand filter realizes uniform water distribution, and the waste water enters the sand filter area. The sand filter area flows out from the overflow weir of the sand filter area and the outlet pipe of the quicksand filter, and enters the storage tank; the airflow generated by the blower of the quicksand filter drives the sand and water in the sand washing area to flow upwards, and at the same time washes the sand, and the airflow drives the sand washing The sand and water in the zone enter the sand-water sedimentation and separation zone. Due to the different specific gravity of sand and water, the fine sand settles down and flows into the sand filter zone through the sand return channel, so that the fine sand in the sand filter zone moves from top to bottom continuously. , the water in the sand-water sedimentation separation area enters the crystallization sedimentation tank for retreatment through the overflow weir in the sand washing area and the sand washing water discharge pipe.
⑥储水池的出水回用或进一步处理。⑥Reuse or further treatment of the effluent from the storage tank.
⑦结晶沉淀池产生的沉淀物经浓缩、脱水回收利用。⑦ The sediment produced in the crystallization and sedimentation tank is recycled by concentration and dehydration.
本发明的有益效果是:因地制宜,基建投资少,维护方便,能耗较低,对废水具有比较好的处理效果。The invention has the beneficial effects of adapting measures to local conditions, less infrastructure investment, convenient maintenance, lower energy consumption and better treatment effect on waste water.
附图说明Description of drawings
下面结合附图和实施例对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.
图1中:1.还原反应池,1-1.还原反应池进水管,1-2.还原剂添加计量系统,1-3.还原反应池搅拌器,1-4.还原反应池出水管。In Fig. 1: 1. Reduction reaction tank, 1-1. Reduction reaction tank water inlet pipe, 1-2. Reductant adding metering system, 1-3. Reduction reaction tank agitator, 1-4. Reduction reaction tank outlet pipe.
图2是本发明实施例结晶沉淀池的结构示意图。Fig. 2 is a schematic structural diagram of a crystallization sedimentation tank according to an embodiment of the present invention.
图2中:2.结晶沉淀池,2-1.结晶区,2-2.沉淀区,2-3.结晶沉淀池进水管,2-4.结晶诱导剂添加计量系统,2-5.结晶区搅拌器,2-6.隔板,2-7.结晶沉淀池三相分离器,2-8.结晶沉淀池溢水堰,2-9.沉淀物排放阀。In Fig. 2: 2. crystallization sedimentation tank, 2-1. crystallization area, 2-2. precipitation area, 2-3. crystallization sedimentation tank inlet pipe, 2-4. crystallization inducer adding metering system, 2-5. crystallization Zone agitator, 2-6. Partition plate, 2-7. Three-phase separator of crystallization sedimentation tank, 2-8. Overflow weir of crystallization sedimentation tank, 2-9. Sediment discharge valve.
图3是本发明实施例流砂滤池的结构示意图。Fig. 3 is a schematic structural view of a quicksand filter according to an embodiment of the present invention.
图3中:3.流砂滤池,3-1.流砂滤池进水管,3-2.流砂滤池布水管,3-3.气提管,3-4.流砂滤池鼓风机,3-5.洗砂区溢水堰,3-6.回砂通道,3-7.砂滤区溢水堰。Among Fig. 3: 3. quicksand filter, 3-1. quicksand filter inlet pipe, 3-2. quicksand filter cloth water pipe, 3-3. gas lift pipe, 3-4. quicksand filter air blower, 3-5 . Sand washing area overflow weir, 3-6. Sand return channel, 3-7. Sand filter area overflow weir.
图4是本发明实施例的工艺流程图。Fig. 4 is a process flow diagram of an embodiment of the present invention.
具体实施方式detailed description
现在结合附图对本发明作进一步详细的说明。这些附图均为简化示意图,仅以示意方式说明本发明的基本结构,因此其仅显示与本发明有关的构成。The present invention is described in further detail now in conjunction with accompanying drawing. These drawings are all simplified schematic diagrams, and only illustrate the basic structure of the present invention in a schematic manner, so they only show the configurations related to the present invention.
实施例Example
如图1~图4所示,本发明一种含铁废水预处理装置,包括调节池、还原反应池1、结晶沉淀池2、流砂滤池3和储水池,调节池、还原反应池1、结晶沉淀池2、流砂滤池3和储水池依次连通。As shown in Figures 1 to 4, an iron-containing wastewater pretreatment device of the present invention includes a regulating tank, a reduction reaction tank 1, a crystallization sedimentation tank 2, a quicksand filter tank 3 and a water storage tank, a regulating tank, a reduction reaction tank 1, The crystallization sedimentation tank 2, the quicksand filter tank 3 and the water storage tank are connected in sequence.
所述的调节池包括调节池进水管和调节池出水管,用于调节废水的水质、水量和pH值。The regulating pond includes a regulating pond inlet pipe and a regulating pond outlet pipe for regulating the water quality, water quantity and pH value of the waste water.
所述的还原反应池1的中上部设置有还原反应池进水管1-1,还原反应池的上部设置有还原剂添加计量系统1-2;还原反应池的中部设置有还原反应池搅拌器1-3,还原反应池的底部设置有还原反应池出水管1-4。The middle and upper part of the reduction reaction tank 1 is provided with a reduction reaction tank water inlet pipe 1-1, and the upper part of the reduction reaction tank is provided with a reducing agent addition metering system 1-2; the middle part of the reduction reaction tank is provided with a reduction reaction tank agitator 1 -3, the bottom of the reduction reaction tank is provided with a reduction reaction tank outlet pipe 1-4.
所述的还原剂添加计量系统1-2添加的还原剂为亚硫酸氢钠。The reducing agent added by the reducing agent adding metering system 1-2 is sodium bisulfite.
所述的结晶沉淀池2包括结晶区2-1和沉淀区2-2。The crystallization sedimentation tank 2 includes a crystallization area 2-1 and a precipitation area 2-2.
所述的结晶区2-1的中上部设置有结晶沉淀池进水管2-3,结晶区的上部设置有结晶诱导剂添加计量系统2-4,结晶区的下部设置有结晶区搅拌器2-5。The middle and upper part of the crystallization zone 2-1 is provided with a crystallization sedimentation tank water inlet pipe 2-3, the upper part of the crystallization zone is provided with a crystallization inducer addition metering system 2-4, and the lower part of the crystallization zone is provided with a crystallization zone agitator 2- 5.
所述的结晶诱导剂添加计量系统添加的结晶诱导剂为涂敷碳酸钠的石英砂;所述的结晶诱导剂的制备过程为:The crystallization inducer added by the added metering system of the crystallization inducer is quartz sand coated with sodium carbonate; the preparation process of the crystallization inducer is:
①将石英砂放入1mol/L的碳酸钠溶液中浸泡,在摇床中振荡24h;① Soak the quartz sand in 1mol/L sodium carbonate solution and shake it in a shaker for 24 hours;
②将浸泡后的石英砂过滤;② Filter the soaked quartz sand;
③将过滤后的石英砂用去离子水清洗;③ Wash the filtered quartz sand with deionized water;
④将清洗后的石英干燥,制得结晶诱导剂。④ drying the cleaned quartz to obtain a crystallization inducer.
所述结晶区2-1和沉淀区2-2之间设有隔板2-6,该隔板与结晶沉淀池的内壁形成作为废水进入沉淀区2-2的废水流道,沉淀区2-2的出口处设有结晶沉淀池三相分离器2-7,沉淀区的出口上部设有结晶沉淀池溢水堰2-8,沉淀区底部设计成锥形结构,在锥形结构底部设置有沉淀物排放阀2-9。结晶沉淀池溢水堰2-8连接结晶沉淀池出水管,结晶沉淀池出水管连接流砂滤池进水管。A partition 2-6 is provided between the crystallization zone 2-1 and the precipitation zone 2-2, and the partition plate and the inner wall of the crystallization sedimentation tank form a waste water flow channel that enters the precipitation zone 2-2 as waste water, and the precipitation zone 2-2 The outlet of 2 is provided with a crystallization sedimentation tank three-phase separator 2-7, the upper part of the outlet of the sedimentation area is provided with a crystallization sedimentation tank overflow weir 2-8, the bottom of the sedimentation area is designed as a conical structure, and a sedimentation tank is arranged at the bottom of the conical structure. Material discharge valve 2-9. The overflow weir 2-8 of the crystallization sedimentation tank is connected to the outlet pipe of the crystallization sedimentation tank, and the outlet pipe of the crystallization sedimentation tank is connected to the water inlet pipe of the quicksand filter.
所述流砂滤池3包括流砂滤池进水管3-1和用于排出处理后水的流砂滤池出水管,所述的流砂滤池包括布水区、洗砂区和砂滤区;所述的布水区位于流砂滤池的下部,布水区设有流砂滤池布水管3-2,流砂滤池布水管3-2连接流砂滤池进水管3-1,为了废水处理的效果更好,所述的流砂滤池布水管3-2设置成同心圆形状,流砂滤池布水管上具有向下辐射出水口;所述的洗砂区位于流砂滤池的中心,为圆柱形筒状结构,圆柱形筒状结构下端开口位于流砂滤池的最底部,圆柱形筒状结构上端开口位于流砂滤池的上部,洗砂区的中部设有气提管3-3,气提管3-3连接流砂滤池外的流砂滤池鼓风机3-4,洗砂区的上部设有砂水沉淀分离区,砂水沉淀分离区的上部设有洗砂区溢水堰3-5,洗砂区溢水堰3-5连接洗砂水排放管和结晶沉淀池进水管,砂水沉淀分离区的下部设有回砂通道3-6;所述的砂滤区位于洗砂区的外围,砂滤区内充填有细砂,砂滤区上部设有砂滤区溢水堰3-7,砂滤区溢水堰3-7连接流砂滤池出水管,流砂滤池过滤处理后的水进入储水池回用。The quicksand filter 3 includes a quicksand filter inlet pipe 3-1 and a quicksand filter outlet pipe for discharging treated water, and the quicksand filter includes a water distribution area, a sand washing area and a sand filter area; The water distribution area is located at the lower part of the quicksand filter, and the water distribution area is provided with a quicksand filter water distribution pipe 3-2, and the quicksand filter water distribution pipe 3-2 is connected to the quicksand filter inlet pipe 3-1, so that the effect of wastewater treatment is better , the quicksand filter water distribution pipe 3-2 is arranged in a concentric circle shape, and the quicksand filter water distribution pipe has a downward radiating water outlet; the described sand washing area is located in the center of the quicksand filter and is a cylindrical tubular structure , the lower opening of the cylindrical cylindrical structure is located at the bottom of the quicksand filter, the upper opening of the cylindrical cylindrical structure is located at the upper part of the quicksand filter, and the middle part of the sand washing area is provided with an air lift pipe 3-3, and an air lift pipe 3-3 Connect the quicksand filter blower 3-4 outside the quicksand filter. The upper part of the sand washing area is provided with a sand-water sedimentation separation area. The upper part of the sand-water sedimentation separation area is equipped with a sand washing area overflow weir 3-5. 3-5 Connect the sand washing water discharge pipe and the water inlet pipe of the crystallization sedimentation tank, and the lower part of the sand water sedimentation separation area is provided with a sand return channel 3-6; the sand filter area is located on the periphery of the sand washing area, and the sand filter area is filled with There is fine sand, and the upper part of the sand filter area is provided with a sand filter area overflow weir 3-7, and the sand filter area overflow weir 3-7 is connected to the outlet pipe of the quicksand filter, and the water filtered by the quicksand filter enters the storage tank for reuse.
一种采用上述含铁废水处理装置进行废水处理的方法,具有如下步骤:A method for wastewater treatment using the above-mentioned iron-containing wastewater treatment device has the following steps:
①含铁废水通过调节池进水管进入调节池,调节水质、水量和pH值。①The iron-containing wastewater enters the regulating pond through the inlet pipe of the regulating pond to adjust the water quality, water quantity and pH value.
②调节后的废水进入还原反应池1,还原剂添加计量系统1-2添加还原剂亚硫酸氢钠,还原反应池搅拌器1-3对废水进行搅拌,将废水中的三价铁离子还原成易发生异相结晶的二价铁离子。②The adjusted wastewater enters the reduction reaction tank 1, the reducing agent addition metering system 1-2 adds the reducing agent sodium bisulfite, and the reduction reaction tank agitator 1-3 stirs the wastewater to reduce the ferric ions in the wastewater to Divalent iron ions prone to heterogeneous crystallization.
③还原反应后的废水通过结晶沉淀池进水管2-3进入结晶区2-1,结晶诱导剂添加计量系统2-4添加结晶诱导剂,结晶区搅拌器2-5对废水进行搅拌混合。③ The waste water after the reduction reaction enters the crystallization area 2-1 through the water inlet pipe 2-3 of the crystallization sedimentation tank, the crystallization inducer adding metering system 2-4 adds the crystallization inducer, and the agitator 2-5 in the crystallization area stirs and mixes the wastewater.
④然后废水进入沉淀区的废水流道,废水发生结晶反应,结晶沉淀池三相分离器2-7实现废水和固体的分离,沉淀物在重力的作用下下沉到沉淀区的下部,通过底部的沉淀物排放阀2-9排出,沉淀后的废水通过结晶沉淀池溢水堰2-8和结晶沉淀池出水管进入流砂滤池进水管3-1。④ Then the waste water enters the waste water flow channel of the sedimentation area, and the waste water undergoes a crystallization reaction, and the three-phase separator 2-7 of the crystallization sedimentation tank realizes the separation of waste water and solids, and the sediment sinks to the lower part of the sedimentation area under the action of gravity, and passes through the bottom The sediment discharge valve 2-9 discharges, and the waste water after the precipitation enters the quicksand filter tank inlet pipe 3-1 through the crystallization sedimentation tank overflow weir 2-8 and the crystallization sedimentation tank outlet pipe.
⑤废水通过流砂滤池进水管3-1、流砂滤池布水管3-2进入流砂滤池的下部,流砂滤池布水管3-2实现均匀布水,废水进入砂滤区,废水中的污染物被进一步过滤,然后废水穿过砂滤区,由砂滤区溢水堰3-7和流砂滤池出水管流出,进入储水池;流砂滤池鼓风机3-4产生的气流带动洗砂区中的砂和水向上流动,同时对砂进行冲洗,然后砂和水进入砂水沉淀分离区,由于砂和水的比重不同,细砂沉淀下去并通过回砂通道3-6流入砂滤区,实现砂滤区中的细砂不断从上往下的移动,砂水沉淀分离区中的水通过洗砂区溢水堰3-5和洗砂水排放管进入结晶沉淀池进行再处理。⑤The waste water enters the lower part of the quicksand filter through the water inlet pipe 3-1 of the quicksand filter and the water distribution pipe 3-2 of the quicksand filter. The waste water is further filtered, and then the waste water passes through the sand filter area, flows out from the sand filter area overflow weir 3-7 and the quicksand filter outlet pipe, and enters the storage tank; the air flow produced by the quick sand filter air blower 3-4 drives the sand washing area The sand and water flow upwards and wash the sand at the same time, and then the sand and water enter the sand-water sedimentation and separation area. Due to the different specific gravity of the sand and water, the fine sand settles down and flows into the sand filter area through the sand return channel 3-6 to realize sand filtration. The fine sand in the filter area moves continuously from top to bottom, and the water in the sand-water sedimentation separation area passes through the overflow weir 3-5 in the sand washing area and the sand washing water discharge pipe into the crystallization sedimentation tank for reprocessing.
⑥储水池的出水回用或进一步处理。⑥Reuse or further treatment of the effluent from the storage tank.
⑦结晶沉淀池产生的沉淀物经浓缩、脱水回收利用。⑦ The sediment produced in the crystallization and sedimentation tank is recycled by concentration and dehydration.
以上述依据本发明的理想实施例为启示,通过上述的说明内容,相关工作人员完全可以在不偏离本项发明技术思想的范围内进行多样的变更以及修改。本项发明的技术性范围并不局限于说明书上的内容,必须要根据权利要求范围来确定其技术性范围。Inspired by the above-mentioned ideal embodiment according to the present invention, through the above-mentioned description content, relevant workers can make various changes and modifications within the scope of not departing from the technical idea of the present invention. The technical scope of the present invention is not limited to the content in the specification, but must be determined according to the scope of the claims.
Claims (2)
- A kind of 1. iron content waste water pretreatment unit, it is characterised in that:Including regulating reservoir, reduction reaction pond (1), crystalline deposit pond (2), quicksand filter tank (3) and tank, regulating reservoir, reduction reaction pond (1), crystalline deposit pond (2), quicksand filter tank (3) and water storage Pond is sequentially communicated;Described regulating reservoir includes regulating reservoir water inlet pipe and regulating reservoir outlet pipe, for adjusting the water quality, water and pH value of waste water;The middle and upper part of described reduction reaction pond (1) is provided with reduction reaction pond water inlet pipe (1-1), and the top of reduction reaction pond is set It is equipped with reducing agent addition metering system (1-2);Reduction reaction pond agitator (1-3) is provided with the middle part of reduction reaction pond, is reduced The bottom of reaction tank is provided with reduction reaction pond outlet pipe (1-4);The reducing agent of described reducing agent addition metering system (1-2) addition is sodium hydrogensulfite;Described crystalline deposit pond (2) includes crystal region (2-1) and settling zone (2-2);The middle and upper part of described crystal region (2-1) is provided with crystalline deposit pond water inlet pipe (2-3), and the top of crystal region is provided with knot Brilliant derivant addition metering system (2-4), the bottom of crystal region is provided with crystal region agitator (2-5);The crystallization derivant of described crystallization derivant addition metering system addition is the quartz sand of coating sodium carbonate;The preparation process of described crystallization derivant is:Soaked 1. quartz sand is put into 1mol/L sodium carbonate liquor, 24h is vibrated in shaking table;2. by the quartz sand filtration after immersion;3. the quartz sand after filtering is cleaned with deionized water;4. the quartz after cleaning is dried, crystallization derivant is made;Dividing plate (2-6), the dividing plate and the inwall shape in crystalline deposit pond are provided between the crystal region (2-1) and settling zone (2-2) Into the waste water runner for entering settling zone (2-2) as waste water, the exit of settling zone (2-2) is provided with crystalline deposit pond three phase separation Device (2-7), the outlet top of settling zone are provided with crystalline deposit pond overfalling weir (2-8), the tapered structure of settling zone bottom design, Pyramidal structure bottom is provided with sediment discharge valve (2-9);Crystalline deposit pond overfalling weir (2-8) connects crystalline deposit pond water outlet Pipe, crystalline deposit pond outlet pipe connection flow sand filter water inlet pipe;The quicksand filter tank outlet pipe of water after the quicksand filter tank (3) includes quicksand filter tank water inlet pipe (3-1) and handled for discharge, Described quicksand filter tank includes water distribution area, washed-out sand area and sand filtration area;Described water distribution area is located at the bottom in quicksand filter tank, water distribution area Provided with quicksand filter tank water distributor (3-2), quicksand filter tank water distributor (3-2) connection flow sand filter water inlet pipe (3-1), at waste water The effect of reason is more preferable, and described quicksand filter tank water distributor (3-2) is arranged to concentric circles, have on the water distributor of quicksand filter tank to Lower radiation delivery port;Described washed-out sand area is located at the center in quicksand filter tank, is cylindrical barrel structure, under cylindrical barrel structure End opening is located at the bottommost in quicksand filter tank, and cylindrical barrel structure upper end open is located at the top in quicksand filter tank, washed-out sand area Middle part is provided with stripping tube (3-3), the quicksand filter tank air blower (3-4) outside stripping tube (3-3) connection flow sand filter, washed-out sand area it is upper Portion is provided with sand water sedimentation Disengagement zone, and the top of sand water sedimentation Disengagement zone is provided with washed-out sand area overfalling weir (3-5), washed-out sand area overfalling weir (3-5) connects washed-out sand water discharge spout and crystalline deposit pond water inlet pipe, the bottom of sand water sedimentation Disengagement zone are provided with back sand passage (3- 6);Described sand filtration area is located at the periphery in washed-out sand area, and fine sand is filled with sand filtration area, and sand filtration area top is provided with sand filtration area overfalling weir (3-7), sand filtration area overfalling weir (3-7) connection flow sand filter outlet pipe, the water after the processing of quicksand filter return into tank With.
- A kind of 2. iron content waste water pretreatment unit according to claim 1, it is characterised in that:It is pre- using above-mentioned iron content waste water The method that processing unit carries out wastewater treatment, has following steps;1. iron content waste water enters regulating reservoir, regulating water quality, water and pH value by regulating reservoir water inlet pipe;2. the waste water after regulation enters reduction reaction pond (1), reducing agent addition metering system (1-2) addition reducing agent bisulfite Sodium, reduction reaction pond agitator (1-3) are stirred to waste water, the ferric ion in waste water are reduced into out-phase knot easily occurs Brilliant ferrous ion;3. the waste water after reduction reaction enters knot by reduction reaction pond outlet pipe (1-4) and crystalline deposit pond water inlet pipe (2-3) Crystalline region (2-1), crystallization derivant addition metering system (2-4) addition crystallization derivant, crystal region agitator (2-5) enter to waste water Row is stirred;4. and then waste water enters the waste water runner of settling zone, crystallization reaction, crystalline deposit pond three phase separator (2-7) occur for waste water The separation of waste water and solid is realized, sediment sinks to the bottom of settling zone under gravity, passes through the sediment of bottom Drain valve (2-9) is discharged, and the waste water after precipitation enters to become a mandarin by crystalline deposit pond overfalling weir (2-8) and crystalline deposit pond outlet pipe Sand filter water inlet pipe (3-1);5. waste water enters the bottom in quicksand filter tank, quicksand by quicksand filter tank water inlet pipe (3-1), quicksand filter tank water distributor (3-2) Filter tank water distributor (3-2) realizes water distribution uniformity, and waste water enters sand filtration area, and the pollutant in waste water is further filtered, and is then given up Water passes through sand filtration area, is flowed out by sand filtration area overfalling weir (3-7) and quicksand filter tank outlet pipe, into tank;The air blast of quicksand filter tank Air-flow caused by machine (3-4) drives the Sha Heshui in washed-out sand area to flow up, while sand is rinsed, and then sand and water enter Sand water sedimentation Disengagement zone, because sand is different with the proportion of water, fine deposition goes down and flows into sand filtration by returning sand passage (3-6) Area, realizes the movement of fine sand in sand filtration area constantly from top to bottom, and the water in sand water sedimentation Disengagement zone passes through washed-out sand area overfalling weir (3-5) and washed-out sand water discharge spout are reprocessed into crystalline deposit pond;6. the effluent reuse of tank or further processing;7. sediment caused by crystalline deposit pond is concentrated, dehydration recycles.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108947147A (en) * | 2018-08-30 | 2018-12-07 | 常州大学 | A kind of DMF advanced waste treatment apparatus |
| CN109133526A (en) * | 2018-09-25 | 2019-01-04 | 常州大学 | A kind of phenol resin production waste water processing unit |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1525163A1 (en) * | 2002-07-22 | 2005-04-27 | J. Ming Zhuang | Method for treating metal-contaminated water and soil |
| CN105836909A (en) * | 2016-05-04 | 2016-08-10 | 常州大学 | Arsenic and lead containing wastewater treatment device |
| CN106044997A (en) * | 2016-07-08 | 2016-10-26 | 哈尔滨工业大学深圳研究生院 | A kind of treatment method containing Fe3+ heavy metal wastewater |
-
2017
- 2017-10-10 CN CN201710933070.6A patent/CN107487904A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1525163A1 (en) * | 2002-07-22 | 2005-04-27 | J. Ming Zhuang | Method for treating metal-contaminated water and soil |
| CN105836909A (en) * | 2016-05-04 | 2016-08-10 | 常州大学 | Arsenic and lead containing wastewater treatment device |
| CN106044997A (en) * | 2016-07-08 | 2016-10-26 | 哈尔滨工业大学深圳研究生院 | A kind of treatment method containing Fe3+ heavy metal wastewater |
Non-Patent Citations (1)
| Title |
|---|
| 熊娅等: "诱导结晶工艺中诱晶载体的选择与改性", 《环境工程学报》 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108947147A (en) * | 2018-08-30 | 2018-12-07 | 常州大学 | A kind of DMF advanced waste treatment apparatus |
| CN109133526A (en) * | 2018-09-25 | 2019-01-04 | 常州大学 | A kind of phenol resin production waste water processing unit |
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