CN105753252B - A kind of electroplating waste processing equipment containing ambrose alloy - Google Patents
A kind of electroplating waste processing equipment containing ambrose alloy Download PDFInfo
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- CN105753252B CN105753252B CN201610196883.7A CN201610196883A CN105753252B CN 105753252 B CN105753252 B CN 105753252B CN 201610196883 A CN201610196883 A CN 201610196883A CN 105753252 B CN105753252 B CN 105753252B
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- 238000009713 electroplating Methods 0.000 title claims abstract description 15
- 239000002699 waste material Substances 0.000 title claims description 4
- 239000000956 alloy Substances 0.000 title claims 2
- 229910045601 alloy Inorganic materials 0.000 title claims 2
- 238000005273 aeration Methods 0.000 claims abstract description 88
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 80
- 238000001179 sorption measurement Methods 0.000 claims abstract description 73
- 230000003647 oxidation Effects 0.000 claims abstract description 68
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 68
- 239000002351 wastewater Substances 0.000 claims abstract description 42
- 230000001105 regulatory effect Effects 0.000 claims abstract description 32
- 239000002893 slag Substances 0.000 claims abstract description 30
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 27
- 239000010959 steel Substances 0.000 claims abstract description 27
- 239000003463 adsorbent Substances 0.000 claims abstract description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 18
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 18
- 239000001301 oxygen Substances 0.000 claims abstract description 18
- 238000001556 precipitation Methods 0.000 claims description 11
- 239000013049 sediment Substances 0.000 claims description 11
- 238000002156 mixing Methods 0.000 claims description 6
- 239000000945 filler Substances 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 238000005192 partition Methods 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 claims description 3
- 239000000706 filtrate Substances 0.000 claims 9
- 238000010521 absorption reaction Methods 0.000 claims 7
- 241000876852 Scorias Species 0.000 claims 2
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 239000011148 porous material Substances 0.000 claims 1
- 238000012216 screening Methods 0.000 claims 1
- 238000004062 sedimentation Methods 0.000 abstract description 57
- 239000000463 material Substances 0.000 abstract description 28
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 abstract description 24
- 239000004744 fabric Substances 0.000 abstract description 10
- 238000004065 wastewater treatment Methods 0.000 abstract description 10
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 abstract description 9
- 229910052802 copper Inorganic materials 0.000 abstract description 9
- 239000010949 copper Substances 0.000 abstract description 9
- 229910052759 nickel Inorganic materials 0.000 abstract description 9
- 238000000034 method Methods 0.000 description 11
- 238000005259 measurement Methods 0.000 description 7
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 4
- 229910001431 copper ion Inorganic materials 0.000 description 4
- 229910001453 nickel ion Inorganic materials 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- YOCUPQPZWBBYIX-UHFFFAOYSA-N copper nickel Chemical compound [Ni].[Cu] YOCUPQPZWBBYIX-UHFFFAOYSA-N 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000007747 plating Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- VEQPNABPJHWNSG-UHFFFAOYSA-N Nickel(2+) Chemical compound [Ni+2] VEQPNABPJHWNSG-UHFFFAOYSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000005842 biochemical reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Classifications
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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
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- 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
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/16—Nature of the water, waste water, sewage or sludge to be treated from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
Abstract
一种含镍铜电镀废水处理装置,包括废水调节池、吸附沉淀池、曝气氧化池和好氧滤塔,废水调节池、吸附沉淀池、曝气氧化池和好氧滤塔依次连通;吸附沉淀池包括混合吸附区和沉淀区,混合吸附区的中上部设置有吸附沉淀池进水管,混合吸附区的上部设置有钢渣吸附剂添加计量系统,混合吸附区的中部设置有搅拌器;曝气氧化池中下部设置有曝气氧化池进水管,曝气氧化池进水管下部设有布水三角锥,布水三角锥下部设有曝气调控系统;好氧滤塔包括滤塔顶盖、好氧滤塔进水管、好氧滤塔布水管、滤料、滤料支撑架、进风口和好氧滤塔出水管。
A nickel-containing copper electroplating wastewater treatment device, including a wastewater regulating tank, an adsorption sedimentation tank, an aerated oxidation tank, and an aerobic filter tower, and the wastewater adjustment tank, the adsorption sedimentation tank, an aerated oxidation tank, and an aerobic filter tower are connected in sequence; the adsorption The sedimentation tank includes a mixed adsorption area and a sedimentation area. The upper middle part of the mixed adsorption area is equipped with an adsorption sedimentation tank inlet pipe, the upper part of the mixed adsorption area is equipped with a steel slag adsorbent addition metering system, and the middle part of the mixed adsorption area is equipped with an agitator; aeration The lower part of the oxidation tank is equipped with an aeration oxidation tank inlet pipe, the lower part of the aeration oxidation tank inlet pipe is equipped with a water distribution triangle cone, and the lower part of the water distribution triangle cone is equipped with an aeration control system; the aerobic filter tower includes a filter tower top cover, a well Oxygen filter tower water inlet pipe, aerobic filter tower cloth water pipe, filter material, filter material support frame, air inlet and aerobic filter tower outlet pipe.
Description
技术领域technical field
本发明涉及废水处理技术领域,尤其是一种含镍铜电镀废水处理装置。The invention relates to the technical field of wastewater treatment, in particular to a nickel-containing copper electroplating wastewater treatment device.
背景技术Background technique
每年我国电镀废水的排放量巨大,占工业废水总排放量的十分之一,且电镀废水有毒有害、酸碱度大、重金属含量高,若不及时处理排入自然界,会对环境造成不可修复的严重污染。The discharge of electroplating wastewater in my country is huge every year, accounting for one-tenth of the total discharge of industrial wastewater, and electroplating wastewater is toxic and harmful, with high pH and high content of heavy metals. If it is not treated in time and discharged into nature, it will cause irreparable serious damage to the environment. Pollution.
镀铜工艺和镀镍工艺是最常见的两种工艺,并且一般利用相同设备,因而铜离子和镍离子同时存在于同一电镀废水中。Copper plating process and nickel plating process are the two most common processes, and generally use the same equipment, so copper ions and nickel ions exist in the same electroplating wastewater at the same time.
治理含镍铜电镀废水的方法众多,其中吸附法因操作简单方便,处理成本低、处理效果好成为处理含镍铜电镀废水的首选方法。而对于吸附法而言,寻求一种低廉高效的吸附材料来替代价格昂贵的活性炭和离子交换树脂是关键,因此近年来,廉价高效、环境友好的吸附材料逐渐受到关注。There are many methods for treating nickel-containing copper electroplating wastewater, among which the adsorption method is the preferred method for treating nickel-containing copper electroplating wastewater because of its simple and convenient operation, low treatment cost and good treatment effect. For the adsorption method, it is the key to find a cheap and efficient adsorbent material to replace the expensive activated carbon and ion exchange resin. Therefore, in recent years, cheap, efficient and environmentally friendly adsorbent materials have gradually attracted attention.
钢渣属于工业固体废物,面临处置难题。Steel slag belongs to industrial solid waste and faces disposal problems.
发明内容Contents of the invention
本发明的目的是解决含镍铜电镀废水的处理问题,解决钢渣的处置难题,提供一种含镍铜电镀废水处理装置,将钢渣用于镍铜离子的吸附。The purpose of the present invention is to solve the problem of the treatment of nickel-copper electroplating wastewater, solve the problem of steel slag disposal, provide a nickel-copper electroplating wastewater treatment device, and use steel slag for the adsorption of nickel and copper ions.
本发明解决其技术问题所采用的技术方案是:一种含镍铜电镀废水处理装置,包括调节池、吸附沉淀池、曝气氧化池和好氧滤塔,调节池、吸附沉淀池、曝气氧化池和好氧滤塔依次连通。The technical solution adopted by the present invention to solve the technical problem is: a nickel-containing copper electroplating wastewater treatment device, including a regulating tank, an adsorption sedimentation tank, an aeration oxidation tank and an aerobic filter tower, a regulating tank, an adsorption sedimentation tank, an aeration The oxidation pool and the aerobic filter tower 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pH值、水质和水量。废水由调节池进水管进入调节池,由调节池出水管流出、进入吸附沉淀池进水管。The regulating pond includes a regulating pond inlet pipe and a regulating pond outlet pipe for regulating the pH value, water quality and water quantity of the waste water. The waste water enters the regulating tank from the water inlet pipe of the regulating pool, flows out from the water outlet pipe of the regulating pool, and enters the water inlet pipe of the adsorption sedimentation tank.
所述的吸附沉淀池包括混合吸附区和沉淀区。The adsorption sedimentation tank includes a mixed adsorption area and a sedimentation area.
所述的混合吸附区的中上部设置有吸附沉淀池进水管,混合吸附区的上部设置有钢渣吸附剂添加计量系统;混合吸附区的中下部设置有搅拌器。The upper middle part of the mixed adsorption area is provided with an adsorption sedimentation tank inlet pipe, and the upper part of the mixed adsorption area is equipped with a steel slag adsorbent addition metering system; the middle and lower part of the mixed adsorption area is provided with a stirrer.
钢渣吸附剂的制备过程为:The preparation process of steel slag adsorbent is as follows:
①利用20~100目金属筛将钢渣碎料筛分;①Use a 20-100 mesh metal sieve to screen the steel slag fragments;
②将筛分后的钢渣放入干燥箱,在150~200摄氏度条件下干燥一小时,制得钢渣吸附剂。②Put the sieved steel slag into a drying box and dry it at 150-200 degrees Celsius for one hour to prepare the steel slag adsorbent.
所述混合吸附区和沉淀区之间设有隔板,该隔板与吸附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吸附沉淀池三相分离器,沉淀区的出口上部设有吸附沉淀池溢水堰,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。吸附沉淀池溢水堰连接吸附沉淀池出水管,吸附沉淀池出水管连接曝气氧化池进水管。A dividing plate is arranged between the mixed adsorption zone and the sedimentation zone, and the barrier plate and the inner wall of the adsorption sedimentation tank form a waste water flow channel that enters the sedimentation zone as waste water, and an adsorption sedimentation tank three-phase separator is provided at the outlet of the sedimentation zone. The upper part of the outlet of the sedimentation area is provided with an adsorption 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 adsorption sedimentation tank is connected to the outlet pipe of the adsorption sedimentation tank, and the outlet pipe of the adsorption sedimentation tank is connected to the inlet pipe of the aeration oxidation tank.
所述曝气氧化池中下部设置有曝气氧化池进水管,所述曝气氧化池进水管下部设有布水三角锥;所述布水三角锥下部设有曝气调控系统,所述曝气调控系统包括曝气盘、鼓风机和溶解氧测量调控装置;所述的曝气盘是均匀设置有微孔的微孔式曝气盘,所述曝气盘通过曝气管连接鼓风机,鼓风机设置在曝气氧化池外,曝气氧化池的上部和废水水面下设置溶解氧测量调控装置,所述溶解氧测量调控装置根据氧容量调控鼓风机工作;所述曝气氧化池进水管上部内置有填料;所述曝气氧化池的出水口处布设有曝气氧化池溢流堰。曝气氧化池溢流堰连接曝气氧化池出水管,曝气氧化池出水管连接好氧滤塔进水管。The lower part of the aeration oxidation tank is provided with an aeration oxidation tank inlet pipe, and the lower part of the aeration oxidation tank water inlet pipe is provided with a water distribution triangular cone; the lower part of the water distribution triangular cone is provided with an aeration control system, and the aeration The gas control system includes an aeration pan, a blower and a dissolved oxygen measurement and control device; the aeration pan is a microporous aeration pan with micropores evenly arranged therein, and the aeration pan is connected to the blower through an aeration pipe, and the blower is set Outside the aeration oxidation tank, a dissolved oxygen measurement and control device is installed on the upper part of the aeration oxidation tank and under the water surface of the wastewater, and the dissolved oxygen measurement and control device regulates the work of the blower according to the oxygen capacity; the upper part of the inlet pipe of the aeration oxidation tank is filled with fillers ; The outlet of the aeration oxidation tank is equipped with an overflow weir of the aeration oxidation tank. The overflow weir of the aeration oxidation tank is connected to the water outlet pipe of the aeration oxidation tank, and the water outlet pipe of the aeration oxidation tank is connected to the water inlet pipe of the aerobic filter tower.
所述好氧滤塔包括滤塔顶盖、好氧滤塔进水管、好氧滤塔布水管、滤料、滤料支撑架、进风口和好氧滤塔出水管;好氧滤塔采用多层设置,最顶部设有滤塔顶盖,滤塔顶盖与塔体之间留有出风口;滤塔顶盖下面设有好氧滤塔进水管,好氧滤塔进水管连接好氧滤塔布水管;好氧滤塔布水管安置在最上面一层的滤料上部;滤料放置在每层滤料支撑架上,从上层到下层,滤料的粒径逐渐变小;每层滤塔的滤料支撑架设计成倒梯形抽屉式,一方面加强通风,避免产生臭气,另一方面便于观察和更换滤料,当该层滤料堵塞严重,滤速很低时,只需把该层滤料抽出更换即可;滤塔的底部设有进风口和好氧滤塔出水管。The aerobic filter tower includes a filter tower top cover, an aerobic filter tower water inlet pipe, an aerobic filter tower cloth water pipe, a filter material, a filter material support frame, an air inlet and an aerobic filter tower outlet pipe; the aerobic filter tower adopts multiple Layer setting, the top of the filter tower is provided with a filter tower top cover, and an air outlet is left between the filter tower top cover and the tower body; the aerobic filter tower water inlet pipe is arranged under the filter tower top cover, and the aerobic filter tower water inlet pipe is connected to the aerobic filter tower. The tower cloth water pipe; the aerobic filter tower cloth water pipe is placed on the upper part of the filter material of the uppermost layer; the filter material is placed on the support frame of each layer of filter material, and the particle size of the filter material gradually becomes smaller from the upper layer to the lower layer; each layer of filter material The support frame of the filter material in the tower is designed as an inverted trapezoidal drawer. On the one hand, it enhances ventilation and avoids odor. On the other hand, it is convenient to observe and replace the filter material. This layer of filter material can be pulled out and replaced; the bottom of the filter tower is provided with an air inlet and an aerobic filter tower outlet pipe.
好氧滤塔处理后的水通过好氧滤塔出水管达标排放。The water treated by the aerobic filter tower is discharged up to the standard through the outlet pipe of the aerobic filter tower.
一种采用上述含镍铜电镀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 nickel-containing copper electroplating wastewater treatment device has the following steps:
①废水通过调节池进水管进入调节池,调节废水的pH值、水质和水量。①Wastewater enters the regulating pond through the inlet pipe of the regulating pond to adjust the pH value, water quality and water quantity of the waste water.
②然后废水通过吸附沉淀池进水管进入吸附沉淀池的混合吸附区,钢渣吸附剂添加计量系统添加钢渣吸附剂,搅拌器对废水进行搅拌混合,废水中的镍铜离子被钢渣吸附剂吸附和吸收。② Then the wastewater enters the mixed adsorption area of the adsorption sedimentation tank through the inlet pipe of the adsorption sedimentation tank. The steel slag adsorbent is added to the metering system to add the steel slag adsorbent, and the agitator stirs and mixes the wastewater. The nickel and copper ions in the wastewater are adsorbed and absorbed by the steel slag adsorbent. .
③然后废水进入沉淀区的废水流道,吸附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,沉淀后的废水通过吸附沉淀池溢水堰和吸附沉淀池出水管进入曝气氧化池进水管。③ Then the waste water enters the waste water channel of the sedimentation area, and the three-phase separator of the adsorption sedimentation tank realizes the separation of waste water and solids. The sediment sinks to the lower part of the sedimentation area under the action of gravity, and is discharged through the sediment discharge valve at the bottom, and the sediment The final wastewater enters the inlet pipe of the aeration oxidation tank through the overflow weir of the adsorption sedimentation tank and the outlet pipe of the adsorption sedimentation tank.
④废水通过曝气氧化池进水管进入曝气氧化池的中下部,在布水三角锥的作用下均匀布水,曝气氧化池的曝气盘产生大量的微气泡,溶解氧测量调控装置根据氧容量调控鼓风机工作,确保曝气氧化池水中的溶解氧大于2mg/L。曝气氧化池处理后的水经曝气氧化池溢流堰和曝气氧化池出水管进入好氧滤塔进水管。④ Wastewater enters the middle and lower part of the aeration oxidation tank through the inlet pipe of the aeration oxidation tank, and the water is evenly distributed under the action of the water distribution triangle cone. The aeration plate of the aeration oxidation tank produces a large number of microbubbles. Oxygen capacity regulates the work of the blower to ensure that the dissolved oxygen in the aeration oxidation tank water is greater than 2mg/L. The treated water in the aeration oxidation tank enters the water inlet pipe of the aerobic filter tower through the overflow weir of the aeration oxidation tank and the outlet pipe of the aeration oxidation tank.
⑤废水通过好氧滤塔进水管、好氧滤塔布水管进入好氧滤塔,空气与废水在滤料中交汇发生生化反应,同时滤料对废水进行过滤,好氧滤塔处理后的水通过好氧滤塔出水管达标排放。⑤Wastewater enters the aerobic filter tower through the inlet pipe of the aerobic filter tower and the cloth pipe of the aerobic filter tower. Discharge up to the standard through the outlet pipe of the aerobic filter tower.
⑥吸附沉淀池的沉淀物排放阀排出的吸附饱和后的钢渣脱水后和原始钢渣相同,仍旧是一种很好的工程应用材料,通过选择合理安全的技术手段对吸附后的废渣进行固定化利用,从而减少重金属离子对环境的污染。⑥ The saturated steel slag discharged from the sediment discharge valve of the adsorption sedimentation tank is the same as the original steel slag after dehydration, and is still a good engineering application material. The adsorbed waste slag can be immobilized and utilized by choosing reasonable and safe technical means , thereby reducing the pollution of heavy metal ions to the environment.
附图说明Description of drawings
图1是本发明实施例吸附沉淀池的结构示意图;Fig. 1 is the structural representation of the adsorption sedimentation tank of the embodiment of the present invention;
图1中:1.吸附沉淀池,1-1.混合吸附区,1-2.沉淀区,1-3.吸附沉淀池进水管,1-4.钢渣吸附剂添加计量系统,1-5.搅拌器,1-6.隔板,1-7.吸附沉淀池三相分离器,1-8.吸附沉淀池溢水堰,1-9.沉淀物排放阀。In Fig. 1: 1. Adsorption sedimentation tank, 1-1. Mixed adsorption area, 1-2. Sedimentation area, 1-3. Adsorption sedimentation tank inlet pipe, 1-4. Steel slag adsorbent addition metering system, 1-5. Agitator, 1-6. Partition plate, 1-7. Three-phase separator of adsorption sedimentation tank, 1-8. Overflow weir of adsorption sedimentation tank, 1-9. Sediment discharge valve.
图2是本发明实施例曝气氧化池的结构示意图。Fig. 2 is a schematic structural diagram of an aeration oxidation tank according to an embodiment of the present invention.
图2中:2.曝气氧化池,2-1.曝气氧化池进水管,2-2.布水三角锥,2-3.曝气调控系统,2-4.填料,2-5.曝气氧化池溢流堰。In Fig. 2: 2. Aeration oxidation tank, 2-1. Aeration oxidation tank inlet pipe, 2-2. Water distribution triangle cone, 2-3. Aeration control system, 2-4. Filler, 2-5. Aeration oxidation tank overflow weir.
图3是本发明实施例好氧滤塔的结构示意图。Fig. 3 is a schematic structural view of an aerobic filter tower according to an embodiment of the present invention.
图3中:3.好氧滤塔,3-1.滤塔顶盖,3-2.好氧滤塔进水管,3-3.好氧滤塔布水管,3-4.滤料,3-5.滤料支撑架,3-6.进风口,3-7.好氧滤塔出水管。Among Fig. 3: 3. aerobic filter tower, 3-1. filter tower top cover, 3-2. aerobic filter tower water inlet pipe, 3-3. aerobic filter tower cloth water pipe, 3-4. filter material, 3 -5. Support frame for filter material, 3-6. Air inlet, 3-7. Outlet pipe of aerobic filter tower.
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 ways
现在结合附图对本发明作进一步详细的说明。The present invention is described in further detail now in conjunction with accompanying drawing.
这些附图均为简化的示意图,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。These drawings are all simplified schematic diagrams, which 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所示的一种含镍铜电镀废水处理装置,包括调节池、吸附沉淀池1、曝气氧化池2和好氧滤塔3,调节池、吸附沉淀池1、曝气氧化池2和好氧滤塔3依次连通。A nickel-containing copper electroplating wastewater treatment device as shown in Figures 1 to 4, including a regulating tank, an adsorption sedimentation tank 1, an aeration oxidation tank 2 and an aerobic filter tower 3, a regulating tank, an adsorption sedimentation tank 1, an aeration The oxidation pool 2 and the aerobic filter tower 3 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pH值、水质和水量。废水由调节池进水管进入调节池,由调节池出水管流出进入吸附沉淀池进水管。The regulating pond includes a regulating pond inlet pipe and a regulating pond outlet pipe for regulating the pH value, water quality and water quantity of the waste water. Wastewater enters the regulating tank from the inlet pipe of the regulating tank, and flows out from the outlet pipe of the regulating tank into the inlet pipe of the adsorption sedimentation tank.
所述的吸附沉淀池1包括混合吸附区1-1和沉淀区1-2。The adsorption sedimentation tank 1 includes a mixed adsorption area 1-1 and a precipitation area 1-2.
所述的混合吸附区1-1的中上部设置有吸附沉淀池进水管1-3,混合吸附区的上部设置有钢渣吸附剂添加计量系统1-4;混合吸附区的中下部设置有搅拌器1-5。The upper middle part of the mixed adsorption area 1-1 is provided with an adsorption sedimentation tank inlet pipe 1-3, and the upper part of the mixed adsorption area is provided with a steel slag adsorbent addition metering system 1-4; the middle and lower part of the mixed adsorption area is provided with a stirrer 1-5.
钢渣吸附剂的制备过程为:The preparation process of steel slag adsorbent is as follows:
①利用50目金属筛将钢渣碎料筛分;① Use a 50-mesh metal sieve to screen the steel slag;
②将筛分后的钢渣放入干燥箱,在150摄氏度条件下干燥一小时,制得钢渣吸附剂。②Put the sieved steel slag into a drying oven, and dry it at 150 degrees Celsius for one hour to prepare the steel slag adsorbent.
所述混合吸附区1-1和沉淀区1-2之间设有隔板1-6,该隔板与吸附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吸附沉淀池三相分离器1-7,沉淀区的出口上部设有吸附沉淀池溢水堰1-8,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1-9。吸附沉淀池溢水堰1-8连接吸附沉淀池出水管,吸附沉淀池出水管连接曝气氧化池进水管2-1。A dividing plate 1-6 is arranged between the mixed adsorption zone 1-1 and the settling zone 1-2, and the dividing plate and the inner wall of the adsorption sedimentation tank form a waste water flow channel as waste water entering the settling zone, and a settling plate is set at the outlet of the settling zone There are adsorption sedimentation tank three-phase separator 1-7, the upper part of the outlet of the sedimentation area is provided with an adsorption sedimentation tank overflow weir 1-8, the bottom of the sedimentation area is designed as a conical structure, and a sediment discharge valve 1- 9. The overflow weir 1-8 of the adsorption sedimentation tank is connected to the outlet pipe of the adsorption sedimentation tank, and the outlet pipe of the adsorption sedimentation tank is connected to the inlet pipe 2-1 of the aeration oxidation tank.
所述曝气氧化池2中下部设置有曝气氧化池进水管2-1,所述曝气氧化池进水管2-1下部设有布水三角锥2-2;所述布水三角锥2-2下部设有曝气调控系统2-3,所述曝气调控系统2-3包括曝气盘、鼓风机和溶解氧测量调控装置;进一步,所述的曝气盘是均匀设置有微孔的微孔式曝气盘。所述曝气盘通过曝气管连接鼓风机,鼓风机设置在曝气氧化池外,曝气氧化池的上部、废水水面下设置溶解氧测量调控装置,所述溶解氧测量调控装置根据氧容量调控曝气氧化池鼓风机工作;所述曝气氧化池进水管上部内置有填料2-4;曝气氧化池的出口处布设有曝气氧化池溢流堰2-5。曝气氧化池溢流堰连接曝气氧化池出水管,曝气氧化池出水管连接好氧滤塔进水管3-2。The lower part of the aeration oxidation tank 2 is provided with an aeration oxidation tank inlet pipe 2-1, and the lower part of the aeration oxidation tank inlet pipe 2-1 is provided with a water distribution triangle cone 2-2; the water distribution triangle cone 2 The lower part of -2 is provided with an aeration control system 2-3, and the aeration control system 2-3 includes an aeration pan, a blower and a dissolved oxygen measurement and control device; further, the aeration pan is uniformly provided with micropores Microporous aeration disc. The aeration pan is connected to a blower through an aeration pipe, and the blower is arranged outside the aeration oxidation tank, and a dissolved oxygen measurement and control device is installed on the upper part of the aeration and oxidation tank and under the water surface of the wastewater, and the dissolved oxygen measurement and control device regulates the aeration according to the oxygen capacity. The air blower of the aeration oxidation tank works; the upper part of the water inlet pipe of the aeration oxidation tank has a filler 2-4 built in; the outlet of the aeration oxidation tank is arranged with an overflow weir 2-5 of the aeration oxidation tank. The overflow weir of the aeration oxidation tank is connected to the water outlet pipe of the aeration oxidation tank, and the water outlet pipe of the aeration oxidation tank is connected to the water inlet pipe 3-2 of the aerobic filter tower.
好氧滤塔3包括滤塔顶盖3-1、好氧滤塔进水管3-2、好氧滤塔布水管3-3、滤料3-4、滤料支撑架3-5、进风口3-6和好氧滤塔出水管3-7;好氧滤塔3采用多层设置,最顶部设有滤塔顶盖3-1,滤塔顶盖3-1与塔体之间留有出风口;滤塔顶盖3-1下面设有好氧滤塔进水管3-2,好氧滤塔进水管3-2连接好氧滤塔布水管3-3;好氧滤塔布水管3-3安置在最上面一层的滤料上部;滤料3-4放置在滤料支撑架3-5上,从上层到下层,滤料的粒径逐渐变小;每层滤塔的滤料支撑架设计成倒梯形抽屉式,一方面加强通风,避免产生臭气,另一方面便于观察和更换滤料,当该层滤料堵塞严重,滤速很低时,只需把该层滤料抽出更换即可;滤塔的底部设有进风口3-6和好氧滤塔出水管3-7。Aerobic filter tower 3 includes filter tower top cover 3-1, aerobic filter tower water inlet pipe 3-2, aerobic filter tower cloth water pipe 3-3, filter material 3-4, filter material support frame 3-5, air inlet 3-6 and the outlet pipe 3-7 of the aerobic filter tower; the aerobic filter tower 3 adopts multi-layer settings, and the top of the filter tower is provided with a filter tower top cover 3-1, and there is a gap between the filter tower top cover 3-1 and the tower body Air outlet; the aerobic filter tower water inlet pipe 3-2 is arranged under the filter tower top cover 3-1, and the aerobic filter tower water inlet pipe 3-2 is connected to the aerobic filter tower cloth water pipe 3-3; the aerobic filter tower cloth water pipe 3 -3 is placed on the upper part of the filter material on the top layer; filter material 3-4 is placed on the filter material support frame 3-5, and the particle size of the filter material gradually becomes smaller from the upper layer to the lower layer; the filter material of each layer of filter tower The support frame is designed as an inverted trapezoidal drawer. On the one hand, it enhances ventilation and avoids odor. On the other hand, it is convenient to observe and replace the filter material. Just pull out and replace; the bottom of the filter tower is provided with an air inlet 3-6 and an aerobic filter tower outlet pipe 3-7.
好氧滤塔处理后的水通过好氧滤塔出水管3-7达标排放。The water treated by the aerobic filter tower is discharged up to the standard through the outlet pipe 3-7 of the aerobic filter tower.
一种采用上述含镍铜电镀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 nickel-containing copper electroplating wastewater treatment device has the following steps:
①废水通过调节池进水管进入调节池,调节废水的pH值、水质和水量。①Wastewater enters the regulating pond through the inlet pipe of the regulating pond to adjust the pH value, water quality and water quantity of the waste water.
②然后废水通过调节池出水管和吸附沉淀池进水管1-3进入吸附沉淀池的混合吸附区1-1,钢渣吸附剂添加计量系统1-4添加钢渣吸附剂,搅拌器1-5对废水进行搅拌混合,废水中的镍铜离子被钢渣吸附剂吸附和吸收。② Then the wastewater enters the mixed adsorption area 1-1 of the adsorption sedimentation tank through the outlet pipe of the regulating tank and the inlet pipe 1-3 of the adsorption sedimentation tank. The steel slag adsorbent is added to the metering system 1-4 to add the steel slag adsorbent. Stirring and mixing are carried out, and the nickel and copper ions in the wastewater are adsorbed and absorbed by the steel slag adsorbent.
③然后废水进入沉淀区的废水流道,吸附沉淀池三相分离器1-7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1-9排出,沉淀后的废水通过吸附沉淀池溢水堰1-8和吸附沉淀池出水管进入曝气氧化池进水管2-1。③ Then the waste water enters the waste water channel of the sedimentation area, and the three-phase separator 1-7 of the adsorption 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 sediment discharge valve at the bottom 1-9 are discharged, and the settled wastewater enters the aeration oxidation tank inlet pipe 2-1 through the adsorption sedimentation tank overflow weir 1-8 and the adsorption sedimentation tank outlet pipe.
④废水通过曝气氧化池进水管2-1进入曝气氧化池的中下部,在布水三角锥2-2的作用下均匀布水,曝气氧化池的曝气盘产生大量的微气泡,溶解氧测量调控装置根据氧容量调控鼓风机工作,确保曝气氧化池水中的溶解氧大于2mg/L。曝气氧化池处理后的水经曝气氧化池溢流堰2-5和曝气氧化池出水管进入好氧滤塔进水管3-2。④ The waste water enters the middle and lower part of the aeration oxidation tank through the water inlet pipe 2-1 of the aeration oxidation tank, and the water is evenly distributed under the action of the water distribution triangle 2-2, and the aeration plate of the aeration oxidation tank generates a large number of micro-bubbles, The dissolved oxygen measurement and control device regulates the work of the blower according to the oxygen capacity to ensure that the dissolved oxygen in the aeration oxidation tank water is greater than 2mg/L. The water treated in the aeration oxidation tank enters the aerobic filter tower water inlet pipe 3-2 through the overflow weir 2-5 of the aeration oxidation tank and the outlet pipe of the aeration oxidation tank.
⑤废水通过好氧滤塔进水管3-2、好氧滤塔布水管3-3进入好氧滤塔,空气与废水在滤料3-4中交汇发生生化反应,同时滤料对废水进行过滤,好氧滤塔处理后的水通过好氧滤塔出水管3-7达标排放。⑤Wastewater enters the aerobic filter tower through the aerobic filter tower water inlet pipe 3-2 and the aerobic filter tower cloth water pipe 3-3, and the air and waste water meet in the filter material 3-4 to undergo biochemical reactions, and the filter material filters the waste water at the same time , the water treated by the aerobic filter tower is discharged up to the standard through the outlet pipe 3-7 of the aerobic filter tower.
⑥吸附沉淀池的沉淀物排放阀排出的吸附饱和后的钢渣脱水后和原始钢渣相同,仍旧是一种很好的工程应用材料,通过选择合理安全的技术手段对吸附后的废渣进行固定化利用,从而减少重金属离子对环境的污染。⑥ The saturated steel slag discharged from the sediment discharge valve of the adsorption sedimentation tank is the same as the original steel slag after dehydration, and is still a good engineering application material. The adsorbed waste slag can be immobilized and utilized by choosing reasonable and safe technical means , thereby reducing the pollution of heavy metal ions to the environment.
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.
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Effective date of registration: 20230628 Address after: Room 1703J3, No. 25 Yixian Road, Yangpu District, Shanghai, 200433 Patentee after: Shanghai doctoral high environmental protection technology Co.,Ltd. Address before: Gehu Lake Road Wujin District 213164 Jiangsu city of Changzhou province No. 1 Patentee before: CHANGZHOU University |
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Denomination of invention: A device for treating nickel copper electroplating wastewater Granted publication date: 20180612 Pledgee: The Bank of Shanghai branch Caohejing Limited by Share Ltd. Pledgor: Shanghai doctoral high environmental protection technology Co.,Ltd. Registration number: Y2024980024496 |