CN203373221U - Laboratory wastewater treatment process equipment - Google Patents
Laboratory wastewater treatment process equipment Download PDFInfo
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- CN203373221U CN203373221U CN201320406180.4U CN201320406180U CN203373221U CN 203373221 U CN203373221 U CN 203373221U CN 201320406180 U CN201320406180 U CN 201320406180U CN 203373221 U CN203373221 U CN 203373221U
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- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 24
- 238000000034 method Methods 0.000 title claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 42
- 238000004062 sedimentation Methods 0.000 claims abstract description 37
- 230000015271 coagulation Effects 0.000 claims abstract description 32
- 238000005345 coagulation Methods 0.000 claims abstract description 32
- 230000001105 regulatory effect Effects 0.000 claims abstract description 26
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 23
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 23
- 239000010802 sludge Substances 0.000 claims abstract description 21
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 20
- 239000012528 membrane Substances 0.000 claims abstract description 15
- 238000009296 electrodeionization Methods 0.000 claims abstract description 13
- 238000004519 manufacturing process Methods 0.000 claims abstract description 13
- 239000006004 Quartz sand Substances 0.000 claims abstract description 11
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000000701 coagulant Substances 0.000 claims description 18
- 239000007788 liquid Substances 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 12
- 238000010979 pH adjustment Methods 0.000 claims description 10
- 239000002253 acid Substances 0.000 claims description 9
- 239000003513 alkali Substances 0.000 claims description 8
- 238000005273 aeration Methods 0.000 claims description 6
- 239000003814 drug Substances 0.000 claims description 4
- 239000000945 filler Substances 0.000 claims description 4
- 229940079593 drug Drugs 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 2
- 150000002500 ions Chemical class 0.000 claims 1
- 239000002351 wastewater Substances 0.000 abstract description 22
- 238000004064 recycling Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract 1
- 239000005416 organic matter Substances 0.000 description 7
- 239000010865 sewage Substances 0.000 description 5
- 238000006386 neutralization reaction Methods 0.000 description 4
- 238000011160 research Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000005352 clarification Methods 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 238000011001 backwashing Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
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Abstract
本实用新型提供一种实验室废水处理工艺设备,包括调节池、混凝沉淀池、电气自控装置;调节池的上方连通有pH调节装置;调节池通过提升泵与上方连通有混凝加药装置的混凝沉淀池相连;混凝沉淀池的上端连接有中间水池,中间水池的上方连通有臭氧发生器;中间水池的另一端依次串联有过滤泵、石英砂过滤器、活性炭过滤器、缓冲水池、超滤膜组件、反渗透模块、电去离子模块、产水池;混凝沉淀池的底端管连接有污泥收集箱,污泥收集箱通过螺杆泵连接有压滤机。本实用新型的有益效果是实验室废水利用本实用新型经处理的实验室废水可回用,也可进行深度处理,获得高品质产水,实现实验室废水的再生利用;具有结构简单、适用范围广、操作简单等优点。
The utility model provides a laboratory wastewater treatment process equipment, including a regulating pool, a coagulation sedimentation pond, and an electrical self-control device; a pH regulating device is connected to the top of the regulating pond; a coagulation dosing device is connected to the top of the regulating pond through a lifting pump The coagulation sedimentation tank is connected; the upper end of the coagulation sedimentation tank is connected to an intermediate pool, and the upper end of the intermediate pool is connected to an ozone generator; the other end of the intermediate pool is connected in series with a filter pump, a quartz sand filter, an activated carbon filter, and a buffer pool. , ultrafiltration membrane module, reverse osmosis module, electrodeionization module, water production tank; the bottom pipe of the coagulation sedimentation tank is connected to a sludge collection box, and the sludge collection box is connected to a filter press through a screw pump. The beneficial effect of the utility model is that the laboratory wastewater treated by the utility model can be reused, and can also be further treated to obtain high-quality water and realize the recycling of laboratory wastewater; it has simple structure and wide application range wide, simple operation and other advantages.
Description
技术领域technical field
本实用新型涉及一种废水处理工艺设备,尤其是涉及一种实验室废水处理工艺设备。The utility model relates to a wastewater treatment process equipment, in particular to a laboratory wastewater treatment process equipment.
背景技术Background technique
随着科学研究越来越深入、广泛,各高等院校和科研院所的试验室废水处理问题日益突出,由于实验室废水水质极为复杂且难以预测,排放周期不定,废水量亦无规律,故而实验室废水的综合处理乃至资源化回用属于世界性难题。虽然实验室废水的排放量显著少于工业废水,但鉴于其往往含有酸碱液、有毒有害三致物、重金属以及一些新生物质,污染成分复杂,且存在瞬时高污染浓度等风险,极有可能造成污染事故,因此危害性不容小视,加强实验室废水管理,对实验室废水进行有效处理乃至回用势在必行,然而当前国内外关于实验室废水有效处理技术及工艺的研究还很薄弱,尤其是我国对实验室废水排放问题关注极为不够,尚没有完善的管理规范,同时也缺乏相应的配套技术工艺,目前各实验室废水基本未作处理而直接排入市政管网,为尽快制定实验室废水排放的管理措施,急需进行实验室废水处理技术工艺的研究及设备的研制开发。With the deepening and widening of scientific research, the problem of laboratory wastewater treatment in universities and scientific research institutes has become increasingly prominent. Because the quality of laboratory wastewater is extremely complex and difficult to predict, the discharge cycle is uncertain, and the amount of wastewater is also irregular. Therefore, The comprehensive treatment and recycling of laboratory wastewater is a worldwide problem. Although the discharge of laboratory wastewater is significantly less than that of industrial wastewater, since it often contains acid and alkali, toxic and harmful substances, heavy metals and some new substances, the pollution components are complex, and there are risks such as instantaneous high pollution concentrations, it is very likely Pollution accidents are caused, so the hazards cannot be underestimated. It is imperative to strengthen the management of laboratory wastewater and effectively treat and reuse laboratory wastewater. However, the current domestic and foreign research on effective treatment technologies and processes for laboratory wastewater is still very weak. In particular, our country has not paid enough attention to the discharge of laboratory wastewater. There is no perfect management specification, and there is also a lack of corresponding supporting technologies. At present, the wastewater from various laboratories is basically discharged into the municipal pipe network without treatment. There is an urgent need for laboratory wastewater treatment technology research and equipment research and development.
中国专利,专利号为201120302893.7公开了一种“实验室废水处理装置”其由废水收集罐、调节池、反应槽、沉降池和活性炭滤池构成;废水收集罐利用管道和调节池相连;调节池再通过带污水泵的管道和反应槽相连;反应槽的出水管和沉降池相连,沉降池的溢流管和活性炭滤池相连,活性炭滤池连接净水排放管。该装置的缺点是,工艺简单,适用范围较窄,仅能作为简单预处理。Chinese patent, Patent No. 201120302893.7 discloses a "laboratory wastewater treatment device" which is composed of a wastewater collection tank, a regulating tank, a reaction tank, a settling tank and an activated carbon filter; the wastewater collecting tank is connected to the regulating tank by pipes; the regulating tank It is connected to the reaction tank through a pipeline with a sewage pump; the outlet pipe of the reaction tank is connected to the settling tank, the overflow pipe of the settling tank is connected to the activated carbon filter, and the activated carbon filter is connected to the clean water discharge pipe. The disadvantage of this device is that the process is simple, the scope of application is narrow, and it can only be used as a simple pretreatment.
中国专利,专利号为200920194435.9,公开了“一种实验室废水处理装置”,该装置包括电控系统和废水处理单元,所述废水处理单元包括前后依次连接的集水池、内电解池、微电解池、生物吸附池和沉淀池,所述内电解池、微电解池和生物吸附池中设有曝气系统;此外,还设置污泥过滤池用于处理污泥。该装置的缺点是,投资和运行费用高,残留有机物浓度高。Chinese patent, patent number 200920194435.9, discloses "a laboratory wastewater treatment device", which includes an electronic control system and a wastewater treatment unit, and the wastewater treatment unit includes a water collection pool, an internal electrolysis pool, a micro electrolysis Pool, biological adsorption tank and sedimentation tank, the inner electrolytic tank, micro-electrolytic tank and biological adsorption tank are provided with an aeration system; in addition, a sludge filter tank is also provided for sludge treatment. The disadvantage of this device is that the investment and operating costs are high, and the concentration of residual organic matter is high.
中国专利,专利号为201210258812.7,公开了“实验室废水处理装置”,该装置包括暂存箱、中和沉淀箱、耐酸泵,暂存箱上设有收集漏斗,中和沉淀箱上安装有pH计、投药箱、主轴,主轴上设有搅拌桨及电热芯,中和沉淀箱侧壁设有清液排放管,上端设有排气管,中和沉淀箱底部为沉降槽,沉降槽底部设有排料绞龙,排料绞龙出料口连接有离心分离机,离心分离机上设有出料口及排液管。该装置缺点是:缺乏有机物处理能力,也仅能作为实验废水的简单预处理,适用范围较小。Chinese patent, patent number 201210258812.7, discloses a "laboratory wastewater treatment device", which includes a temporary storage tank, a neutralization sedimentation tank, and an acid-resistant pump. The temporary storage tank is provided with a collection funnel, and the neutralization precipitation tank is equipped with a pH Meter, dosing box, main shaft, the main shaft is equipped with stirring paddle and electric heating core, the side wall of the neutralization sedimentation tank is equipped with a clear liquid discharge pipe, the upper end is equipped with an exhaust pipe, the bottom of the neutralization sedimentation tank is a sedimentation tank, and the bottom of the sedimentation tank is set There is a discharge auger, the outlet of the discharge auger is connected with a centrifuge, and the centrifuge is provided with a discharge port and a liquid discharge pipe. The disadvantage of this device is that it lacks the ability to treat organic matter, and it can only be used as a simple pretreatment of experimental wastewater, and its scope of application is small.
发明内容Contents of the invention
本实用新型要解决的问题是提供一种适用范围广、造作简单、产水可回用也可继续进行深度处理,获得高品质水实现实验室废水的再生利用的一种实验室废水处理工艺设备,尤其适合各类实验室废水的处理及回用。The problem to be solved by the utility model is to provide a laboratory wastewater treatment process equipment that has a wide application range, is simple to manufacture, and can be reused or continued to be further treated to obtain high-quality water to realize the regeneration and utilization of laboratory wastewater. , especially suitable for the treatment and reuse of various laboratory wastewater.
为解决上述技术问题,本实用新型采用的技术方案是:一种实验室废水处理工艺设备,包括调节池、混凝沉淀池、中间水池、电气自控装置;所述调节池的上方通过加药管连通有pH调节装置;所述调节池通过提升泵与所述混凝沉淀池相连,所述混凝沉淀池的上方通过加药管连通有混凝加药装置;所述混凝沉淀池的上端通过管道连接有中间水池,所述中间水池的上方通过管道连通有臭氧发生器;所述中间水池的另一端通过管道依次串连接有过滤泵、石英砂过滤器、活性炭过滤器、缓冲水池、超滤膜组件、反渗透模块、电去离子模块、产水池;所述混凝沉淀池的底端通过排泥管连接有污泥收集箱,所述污泥收集箱通过螺杆泵连接有压滤机,所述污泥收集箱的上端与调节池的入水口相连;所述pH调节装置、提升泵、混凝加药装置、臭氧发生器、过滤泵、螺杆泵、压滤机均与所述电气自控装置电连接。In order to solve the above technical problems, the technical solution adopted by the utility model is: a laboratory wastewater treatment process equipment, including a regulating tank, a coagulation sedimentation tank, an intermediate pool, and an electrical self-control device; A pH adjustment device is communicated; the adjustment tank is connected to the coagulation-settling tank through a lift pump, and a coagulation dosing device is connected to the top of the coagulation-settling tank through a dosing pipe; the upper end of the coagulation-settling tank An intermediate pool is connected through a pipeline, and an ozone generator is connected to the top of the intermediate pool through a pipeline; the other end of the intermediate pool is connected in series with a filter pump, a quartz sand filter, an activated carbon filter, a buffer pool, an ultra- Membrane module, reverse osmosis module, electrodeionization module, water production tank; the bottom of the coagulation sedimentation tank is connected to a sludge collection box through a sludge discharge pipe, and the sludge collection box is connected to a filter press through a screw pump , the upper end of the sludge collection tank is connected to the water inlet of the adjustment tank; the pH adjustment device, lift pump, coagulation dosing device, ozone generator, filter pump, screw pump, filter press are all connected The automatic control device is electrically connected.
所述臭氧发生器用于降解污水中的有机物。The ozone generator is used for degrading organic matter in sewage.
进一步,所述调节池的入水口处设有格栅,且所述调节池内设有液位计、pH计以及搅拌器;所述中间水池、缓冲水池上均设有液位计;所述液位计、pH计均与所述电气自控装置电连接。Further, a grid is provided at the water inlet of the regulating pool, and a liquid level gauge, a pH meter and an agitator are provided in the regulating pool; a liquid level gauge is provided on the intermediate pool and the buffer pool; Both the position meter and the pH meter are electrically connected with the electric automatic control device.
进一步,所述pH调节装置包括酸加药箱和碱加药箱;所述混凝加药装置包括混凝剂加药箱和助凝剂加药箱,且所述酸加药箱、碱加药箱、混凝剂加药箱、助凝剂加药箱上均设有加药计量泵;所述加药计量泵与所述电气自控装置电连接。Further, the pH adjustment device includes an acid dosing box and an alkali dosing box; the coagulation dosing device includes a coagulant dosing box and a coagulant aid dosing box, and the acid dosing box, alkali dosing The medicine box, the coagulant dosing box, and the coagulant aid dosing box are all equipped with dosing metering pumps; the dosing metering pumps are electrically connected to the electrical automatic control device.
进一步,所述混凝沉淀池包括相连通的搅拌池和沉淀池,所述搅拌池内设有搅拌器,所述混凝加药装置与所述搅拌池的进水口处相连,所述沉淀池上设有斜管。Further, the coagulation-sedimentation tank includes a connected stirring tank and a sedimentation tank, the stirring tank is provided with an agitator, the coagulation dosing device is connected to the water inlet of the stirring tank, and the settling tank is equipped with There are inclined tubes.
进一步,在所述臭氧发生器和中间水池之间的管道上设有水射器,且在所述管道的底端设有穿孔曝气管;所述中间水池内设有填料,所述填料用于增加臭氧气体的停留时间。Further, a water ejector is provided on the pipeline between the ozone generator and the intermediate pool, and a perforated aeration tube is provided at the bottom of the pipeline; fillers are provided in the intermediate pool, and the fillers are used To increase the residence time of ozone gas.
进一步,所述过滤泵与所述臭氧发生器的另一端相连通;所述过滤泵与所述电气自控装置电连接。Further, the filter pump is connected to the other end of the ozone generator; the filter pump is electrically connected to the electrical automatic control device.
进一步,所述石英砂过滤器与所述产水池之间设有反洗泵;所述反洗泵与所述电气自控装置电连接,所述反洗泵对石英砂过滤器和活性炭过滤器定期进行反洗,反洗后的水流回调节池。Further, a backwash pump is provided between the quartz sand filter and the water-producing pool; the backwash pump is electrically connected to the electrical automatic control device, and the backwash pump is regularly used for the quartz sand filter and the activated carbon filter. Backwashing is carried out, and the water after backwashing flows back to the regulating tank.
进一步,所述缓冲水池与所述超滤膜组件之间设有超滤泵,所述超滤膜组件与所述反渗透模块之间设有增压泵;所述超滤泵和增压泵均与所述电气自控装置电连接,所述超滤泵为超滤膜组件供水,所述增压泵为反渗透模块增压。Further, an ultrafiltration pump is provided between the buffer pool and the ultrafiltration membrane assembly, and a booster pump is provided between the ultrafiltration membrane assembly and the reverse osmosis module; the ultrafiltration pump and booster pump Both are electrically connected with the electric automatic control device, the ultrafiltration pump supplies water for the ultrafiltration membrane module, and the booster pump pressurizes the reverse osmosis module.
进一步,所述反渗透模块和电去离子模块之间以及电去离子模块与所述产水池之间均设有与所述电气自控装置电连接的流量计。Further, a flow meter electrically connected to the electric automatic control device is provided between the reverse osmosis module and the electrodeionization module and between the electrodeionization module and the produced water tank.
进一步,所述反渗透模块上连接有并联的电磁阀和调节阀;所述电磁阀和调节阀均与所述电气自控装置电连接;所述压滤机为板框压滤机。Further, the reverse osmosis module is connected with a parallel solenoid valve and a regulating valve; both the solenoid valve and the regulating valve are electrically connected to the electrical automatic control device; the filter press is a plate and frame filter press.
本实用新型具有的优点和积极效果是:由于采用上述技术方案,实验室废水利用本发明经加药调质调量阶段、沉淀澄清阶段、高级氧化阶段、深度过滤阶段、污泥处理阶段,能有效处理水中的悬浮物及有机物,由此经处理的实验室废水可回用,也可进行深度处理,获得高品质产水,实现实验室废水的再生利用;具有结构简单、适用范围广、操作简单等优点。The advantages and positive effects of the utility model are: due to the adoption of the above-mentioned technical scheme, the laboratory waste water can be processed through the stages of drug-adding and quality-adjusting, the stage of sedimentation and clarification, the stage of advanced oxidation, the stage of deep filtration and the stage of sludge treatment by using the present invention. Effectively treat suspended solids and organic matter in water, so that the treated laboratory wastewater can be reused, and can also be subjected to advanced treatment to obtain high-quality water and realize the recycling of laboratory wastewater; it has simple structure, wide application range, and easy operation. Simple and other advantages.
附图说明Description of drawings
图1是本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;
图2是图1的加药调质调量阶段、沉淀澄清阶段及高级氧化阶段的局部放大图;Fig. 2 is a partial enlarged view of the stage of dosing, quality and quantity adjustment, sedimentation and clarification stage and advanced oxidation stage of Fig. 1;
图3是本实用新型的深度处理阶段的局部放大图;Fig. 3 is the partial enlarged view of the deep processing stage of the present utility model;
图4是本实用新型的污泥处理阶段的局部放大图。Fig. 4 is a partially enlarged view of the sludge treatment stage of the present invention.
图中:In the picture:
1、调节池 2、中间水池 3、电气自控装置1. Adjusting
4、提升泵 5、臭氧发生器 6、过滤泵4. Lift pump 5.
7、石英砂过滤器 8、活性炭过滤器 9、缓冲水池7.
10、超滤膜组件 11、反渗透模块 12、电去离子模块10.
13、产水池 14、污泥收集箱 15、螺杆泵13.
16、压滤机 17、格栅 18、液位计16.
19、pH计 20、酸加药箱 21、碱加药箱19.
22、混凝剂加药箱 23、助凝剂加药箱 24、加药计量泵22.
25、搅拌池 26、沉淀池 27、搅拌器25.
28、斜管 29、水射器 30、穿孔曝气管28.
31、反洗泵 32、超滤泵 33、增压泵31.
34、流量计 35、电磁阀 36、调节阀34. Flow meter 35.
具体实施方式Detailed ways
如图1、2、3、4所示,本实用新型一种实验室废水处理工艺设备,包括调节池1、混凝沉淀池26、中间水池2、电气自控装置3;所述调节池1的上方通过加药管连通有pH调节装置;所述调节池1通过提升泵4与所述混凝沉淀池26相连,所述混凝沉淀池26的上方通过加药管连通有混凝加药装置;所述混凝沉淀池26的上端通过管道连接有中间水池2,所述中间水池2的上方通过管道连通有臭氧发生器5;所述中间水池2的另一端通过管道依次串连接有过滤泵6、石英砂过滤器7、活性炭过滤器8、缓冲水池9、超滤膜组件10、反渗透模块11、电去离子模块12、产水池13;所述混凝沉淀池26的底端通过排泥管连接有污泥收集箱14,所述污泥收集箱14通过螺杆泵15连接有压滤机16,所述污泥收集箱14的上端与调节池1的入水口相连;所述pH调节装置、提升泵4、混凝加药装置、臭氧发生器5、过滤泵6、螺杆泵15、压滤机16均与所述电气自控装置3电连接。As shown in Figures 1, 2, 3, and 4, a laboratory wastewater treatment process equipment of the present invention includes a regulating tank 1, a
所述臭氧发生器5用于降解污水中的有机物。The ozone generator 5 is used to degrade organic matter in sewage.
优选的,所述调节池1的入水口处设有格栅17,且所述调节池1内设有液位计18、pH计19以及搅拌器27;所述中间水池2、缓冲水池9上均设有液位计18;所述液位计18、pH计19均与所述电气自控装置3电连接。Preferably, the water inlet of the regulating pool 1 is provided with a
优选的,所述pH调节装置包括酸加药箱20和碱加药箱21;所述混凝加药装置包括混凝剂加药箱22和助凝剂加药箱23,且所述酸加药箱20、碱加药箱21、混凝剂加药箱22、助凝剂加药箱23上均设有加药计量泵24;所述加药计量泵24与所述电气自控装置3电连接。Preferably, the pH adjustment device includes an
优选的,所述混凝沉淀池26包括相连通的搅拌池25和沉淀池26,所述搅拌池25内设有搅拌器27,所述混凝加药装置与所述搅拌池25的进水口处相连,所述沉淀池26上设有斜管28。Preferably, the
优选的,在所述臭氧发生器5和中间水池2之间的管道上设有水射器29,且在所述管道的底端设有穿孔曝气管30;所述中间水池2内设有填料,所述填料用于增加臭氧气体的停留时间。Preferably, a
优选的,所述过滤泵6与所述臭氧发生器5的另一端相连通;所述过滤泵6与所述电气自控装置3电连接。Preferably, the
优选的,所述石英砂过滤器7与所述产水池13之间设有反洗泵31;所述反洗泵31与所述电气自控装置3电连接,所述反洗泵31对石英砂过滤器7和活性炭过滤器8定期进行反洗,反洗后的水流回调节池1。Preferably, a
优选的,所述缓冲水池9与所述超滤膜组件10之间设有超滤泵32,所述超滤膜组件10与所述反渗透模块11之间设有增压泵33;所述超滤泵32和增压泵33均与所述电气自控装置3电连接,所述超滤泵32为超滤膜组件10供水,所述增压泵33为反渗透模块11增压。Preferably, an
优选的,所述反渗透模块11和电去离子模块12之间以及电去离子模块12与所述产水池13之间均设有与所述电气自控装置3电连接的流量计34。Preferably, a
优选的,所述反渗透模块11上连接有并联的电磁阀35和调节阀36;所述电磁阀35和调节阀36均与所述电气自控装置3电连接;通过电气自控装置3控制电磁阀35的开启时间,可以调整反渗透模块11的冲洗时间,也可以通过电气自控装置3控制调节阀36调节反渗透模块11的浓水流量,同时电磁阀35或调节阀36还可控制电去离子模块12产水时间,避免产水过多或过少,保证了产水效果,节省了电能,所述压滤机16为板框压滤机16。Preferably, the
本实例的工作过程:1)加药调质调量阶段,实验室废水通过格栅17进入调节池1后,进行水质均化,通过pH调节装置调节pH值,pH一般调节到6-8,均化后的废水进入混凝沉淀池26与混凝剂和助凝剂在搅拌池25内进行混合并在沉淀池26内进行沉淀;The working process of this example: 1) In the stage of drug dosing, quality adjustment and volume adjustment, after the laboratory wastewater enters the adjustment pool 1 through the
2)沉淀澄清阶段,混有混凝剂和助凝剂的废水在沉淀池26中进行固液分离,固体沉降在沉淀池26底部,上清液溢流进入中间水池2;2) In the sedimentation and clarification stage, the wastewater mixed with coagulants and coagulants is separated from solid and liquid in the
3)高级氧化阶段,中间水池2上方设置臭氧发生器5,穿孔曝气管30向中间水池2内通入臭氧,用于降解污水中的有机物;3) In the advanced oxidation stage, an ozone generator 5 is installed above the
4)深度处理阶段,经臭氧氧化的污水依次进入石英砂过滤器7、活性炭过滤器8、缓冲水池9、超滤膜组件10、反渗透模块11、电去离子模块12,用于去除水中的悬浮物和有机物,最后进入产水池13。4) In the advanced treatment stage, the ozone-oxidized sewage enters the
5)污泥处理阶段:沉淀池26底部的污泥通过排泥管定期排入污泥收集箱14内,经加药后通过螺杆泵15排至板框压滤机16进行脱水。5) Sludge treatment stage: The sludge at the bottom of the
以上对本实用新型的一个实施例进行了详细说明,但所述内容仅为本实用新型的较佳实施例,不能被认为用于限定本实用新型的实施范围。凡依本实用新型申请范围所作的均等变化与改进等,均应仍归属于本实用新型的专利涵盖范围之内。An embodiment of the present utility model has been described in detail above, but the content described is only a preferred embodiment of the present utility model, and cannot be considered as limiting the implementation scope of the present utility model. All equal changes and improvements made according to the application scope of the utility model should still belong to the scope covered by the patent of the utility model.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103992005A (en) * | 2014-04-28 | 2014-08-20 | 安徽华盛科技控股股份有限公司 | CIT intelligent control laboratory wastewater treatment device and method |
CN107089767A (en) * | 2017-05-19 | 2017-08-25 | 上海俊逸节能环保科技有限公司 | A kind of group technology of advanced treating laboratory sewage |
CN108558087A (en) * | 2018-01-25 | 2018-09-21 | 嘉兴市欣欣仪器设备有限公司 | Laboratory experiment waste water integral intelligent processing system |
CN111892192A (en) * | 2019-05-05 | 2020-11-06 | 中国科学院过程工程研究所 | A reduction treatment method of laboratory inorganic waste liquid based on membrane separation |
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2013
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103992005A (en) * | 2014-04-28 | 2014-08-20 | 安徽华盛科技控股股份有限公司 | CIT intelligent control laboratory wastewater treatment device and method |
CN103992005B (en) * | 2014-04-28 | 2016-01-20 | 安徽华盛科技控股股份有限公司 | CIT intelligent control laboratory waste water treatment device and method |
CN107089767A (en) * | 2017-05-19 | 2017-08-25 | 上海俊逸节能环保科技有限公司 | A kind of group technology of advanced treating laboratory sewage |
CN108558087A (en) * | 2018-01-25 | 2018-09-21 | 嘉兴市欣欣仪器设备有限公司 | Laboratory experiment waste water integral intelligent processing system |
CN111892192A (en) * | 2019-05-05 | 2020-11-06 | 中国科学院过程工程研究所 | A reduction treatment method of laboratory inorganic waste liquid based on membrane separation |
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