CN107381969B - A kind of processing system of heavy metal industrial effluent - Google Patents
A kind of processing system of heavy metal industrial effluent Download PDFInfo
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Abstract
Description
技术领域technical field
本发明涉及一种含油重金属工业废水的处理系统,属于环境保护中的废水处理领域。The invention relates to a treatment system for oil-containing heavy metal industrial wastewater, which belongs to the field of wastewater treatment in environmental protection.
背景技术Background technique
重金属污染是指由重金属及其化合物所造成的环境污染和生态破坏,其危害程度取决于重金属在环境、食品和生物体中存在的浓度和化学形态。重金属污染主要表现在水污染中,还有一部分在大气和固体废物中。重金属污染与其他有机化合物的污染不同,不少有机化合物可以通过自然界本身的物理、化学或生物效应得以净化,使危害性降低或消除;而重金属具有富集性,很难在环境中降解。Heavy metal pollution refers to environmental pollution and ecological damage caused by heavy metals and their compounds, and the degree of harm depends on the concentration and chemical form of heavy metals in the environment, food and organisms. Heavy metal pollution is mainly manifested in water pollution, and partly in the atmosphere and solid waste. Heavy metal pollution is different from the pollution of other organic compounds. Many organic compounds can be purified through the physical, chemical or biological effects of nature itself, so that the hazards can be reduced or eliminated; while heavy metals are enriched and difficult to degrade in the environment.
从环境污染方面来看,重金属污染最具代表性的是汞、镉、铅以及“类金属”——砷等生物毒性显著的重金属,这些重金属在水环境中不能被分解,人类饮用后毒性放大,与水中的其他毒素结合会生成毒性更大的有机化合物。From the perspective of environmental pollution, the most representative heavy metal pollution is mercury, cadmium, lead, and "metalloids" - arsenic and other heavy metals with significant biological toxicity. , combine with other toxins in the water to produce more toxic organic compounds.
目前,现有的工业废水重金属处理方法包括:化学沉淀法、电解法、吸附法、膜分离法、离子交换法等。At present, the existing industrial wastewater heavy metal treatment methods include: chemical precipitation, electrolysis, adsorption, membrane separation, ion exchange, etc.
(1)化学沉淀法:在工业废水中投加某种化学物质,使其与废水中某些溶解性物质发生反应,生成难溶盐而沉淀下来,这种方法称为化学沉淀法。传统的化学沉淀法包括中和沉淀法、硫化物沉淀法和钡盐沉淀法等。(1) Chemical precipitation method: Dosing a certain chemical substance in industrial wastewater makes it react with certain soluble substances in the wastewater to form insoluble salts and precipitate them. This method is called chemical precipitation method. Traditional chemical precipitation methods include neutralization precipitation, sulfide precipitation and barium salt precipitation.
(2)电解法:应用电解的基本原理,使废水中重金属离子在阳极和阴极上分别发生氧化还原反应,使重金属富集,从而使废水中重金属得以去除,并可回收重金属。电解法处理重金属废水具有运行可靠、重金属去除率高,可回收利用等特点。但由于重金属浓度低时电耗大、投资成本高,电解法只适合处理高浓度重金属废水。(2) Electrolysis method: The basic principle of electrolysis is applied to make the heavy metal ions in the wastewater undergo oxidation-reduction reactions on the anode and cathode respectively, so that the heavy metals are enriched, so that the heavy metals in the wastewater can be removed and the heavy metals can be recovered. Electrolytic treatment of heavy metal wastewater has the characteristics of reliable operation, high removal rate of heavy metals, and recyclability. However, due to the large power consumption and high investment costs when the concentration of heavy metals is low, the electrolysis method is only suitable for treating high-concentration heavy metal wastewater.
(3)吸附法:吸附法是利用吸附剂吸附废水中重金属的一种方法,传统的吸附剂有活性炭、沸石、粘土矿物等天然物质。活性炭的吸附能力强,对重金属去除率高,但价格昂贵,使用寿命短。近些年来发现矿物材料具有很强的吸附能力,其中天然沸石吸附能力最强,也是最早用于重金属废水处理的矿物材料。(3) Adsorption method: Adsorption method is a method of using adsorbents to adsorb heavy metals in wastewater. Traditional adsorbents include natural substances such as activated carbon, zeolite, and clay minerals. Activated carbon has strong adsorption capacity and high removal rate of heavy metals, but it is expensive and has a short service life. In recent years, it has been found that mineral materials have strong adsorption capacity, among which natural zeolite has the strongest adsorption capacity, and is also the earliest mineral material used for heavy metal wastewater treatment.
(4)膜分离法:膜分离法是利用一种特殊的半透膜,在外界压力的作用下,不改变溶液的化学形态使溶质和溶剂进行分离和浓缩的方法。膜分离技术在反应过程中不发生相变化,分离效率高,操作及维护方便,分离和浓缩同时进行,可回收有价值的重金属。常见的膜技术有微滤、超滤、纳滤、反渗透、电渗析、液膜等。(4) Membrane separation method: Membrane separation method is to use a special semi-permeable membrane to separate and concentrate the solute and solvent under the action of external pressure without changing the chemical form of the solution. Membrane separation technology has no phase change during the reaction process, high separation efficiency, convenient operation and maintenance, simultaneous separation and concentration, and valuable heavy metals can be recovered. Common membrane technologies include microfiltration, ultrafiltration, nanofiltration, reverse osmosis, electrodialysis, liquid membrane, etc.
(5)离子交换法:离子交换法处理重金属废水是利用离子交换树脂上的可交换离子与重金属离子发生交换反应,从而去除废水中重金属离子的方法。离子交换技术去除废水中的重金属,净化后出水中重金属离子浓度远低于化学沉淀法处理后出水中重金属离子的浓度,通过回收再生后的溶液,可以实现重金属的回收。离子交换树脂性能对重金属离子的去除效果有较大影响。(5) Ion exchange method: The ion exchange method is used to treat heavy metal wastewater by using the exchangeable ions on the ion exchange resin to undergo exchange reactions with heavy metal ions, thereby removing heavy metal ions in wastewater. Ion exchange technology removes heavy metals in wastewater. The concentration of heavy metal ions in the purified water is much lower than that of the effluent treated by chemical precipitation. By recycling the regenerated solution, heavy metals can be recovered. The performance of ion exchange resin has a great influence on the removal effect of heavy metal ions.
但是现在重金属离子经常存在于含油废水中,由于水中油脂的存在严重阻碍了重金属的去除,降低了重金属离子的处理效果。因此,有必要摆脱现有的处理技术思路,开辟出处理工业废水重金属的新途径,进而开发一种全新形式的工业废水重金属处理技术。But now heavy metal ions often exist in oily wastewater. The presence of oil in water seriously hinders the removal of heavy metals and reduces the treatment effect of heavy metal ions. Therefore, it is necessary to get rid of the existing treatment technology ideas, open up a new way to deal with heavy metals in industrial wastewater, and then develop a new form of industrial wastewater heavy metal treatment technology.
发明内容Contents of the invention
为解决现有技术中存在的不足,本发明提供了一种含油重金属工业废水的处理系统,该系统包括集水井、粗格栅、微泡气浮矿物油吸附装置、矿物油催化重化解吸反应器、原果胶-重金属旋转吸附池、曝气硝化池、生物脱氮池、沉淀池、净水池等;其中,含油重金属工业废水通过废水管线进入集水井,集水井的出口通过废水管线连接粗格栅,粗格栅的出口通过废水管线连接微泡气浮矿物油吸附装置,微泡气浮矿物油吸附装置中的π-烯丙基镍化合物改性硅藻土吸附膜在完全吸附矿物油后会被不锈钢机械臂抓取,并被送入矿物油催化重化解吸反应器,矿物油催化重化解吸反应器中生成的重油从重油排出口排出并被回收再利用,同时微泡气浮矿物油吸附装置的出口通过废水管线连接原果胶-重金属旋转吸附池,原果胶-重金属旋转吸附池排出的污泥物质外运处理,同时原果胶-重金属旋转吸附池的出口通过废水管线连接曝气硝化池,曝气硝化池的出口通过废水管线连接生物脱氮池,生物脱氮池的出口通过废水管线连接沉淀池,沉淀池的出口通过废水管线连接净水池,净水池的出口通过废水管线将经过处理后的净化出水外排;其中,微泡气浮矿物油吸附装置采用高强度玻璃钢材质,其底部装有9支超微细气泡发生器,装置的液面之上可容纳一张横向放置的π-烯丙基镍化合物改性硅藻土吸附膜,其左侧上部装有进水阀门,右侧底部装有出水阀门;矿物油催化重化解吸反应器采用高强度不锈钢材质,其底部装有5部电热鼓风风机,装置内部安装有一套不锈钢膜架,膜架上竖直放置5张待高温处理的π-烯丙基镍化合物改性硅藻土吸附膜,其底部右侧设有重油排出口;经过粗格栅初步去除大粒径物质的废水通过微泡气浮矿物油吸附装置左侧上部的进水阀门进入装置内部,9支超微细气泡发生器开始工作,产生直径小于50μm的超微细气泡,超微细气泡会夹带废水中的矿物油分子一同上浮,并使其被液面之上的π-烯丙基镍化合物改性硅藻土吸附膜吸附,完全吸附矿物油的π-烯丙基镍化合物改性硅藻土吸附膜被不锈钢机械臂抓取,并被竖直放置在矿物油催化重化解吸反应器中的不锈钢膜架上,反应器底部的5部电热鼓风风机可以产生200~250℃的高温空气,在此温度下并在π-烯丙基镍化合物的催化下,矿物油分子中的C-H键会发生短暂的断裂,并快速再结合为C-C键或C-H键,而C-H键会再次发生断裂,C-C键则因π-烯丙基镍化合物的催化作用有限而不会再发生断裂,因此可使碳链较短的矿物油分子逐渐合成为碳链较长的重油分子,同时,重油分子会在高温下从π-烯丙基镍化合物改性硅藻土吸附膜中解吸,汇聚后从反应器底部右侧的重油排出口排出;原果胶-重金属旋转吸附池采用硬质玻璃钢材质,外层涂刷有防水材料,吸附池左侧上方装有进水阀门,左侧下方装有电动伸缩杆推泥装置,右侧上方装有电动钩爪,右侧中部装有出水阀门,右侧下方设有污泥排口,吸附池中部依靠转轴连杆固定有V型网状滚筒,V型网状滚筒上方装有提钩;微泡气浮矿物油吸附装置的出水通过原果胶-重金属旋转吸附池左侧的进水阀门进入吸附池内部,V型网状滚筒在转轴连杆的驱动下充分转动,使废水与南瓜皮充分接触,通过南瓜皮细胞中的非水溶性原果胶的吸附作用使废水中的重金属离子被吸附,经过吸附处理后的废水经出水阀门排出吸附池,V型网状滚筒在吸附近饱和后,可操作电动钩爪抓取V型网状滚筒上方的提钩,将V型网状滚筒提离吸附池,进而完成南瓜皮的更换操作,同时,部分南瓜皮残渣在吸附池底部沉淀,逐渐形成污泥物质,可使用电动伸缩杆推泥装置通过污泥排口排出吸附池,V型网状滚筒更换下的南瓜皮残渣与在吸附池底部沉淀的污泥物质合并后外运处理。In order to solve the deficiencies in the prior art, the present invention provides a treatment system for industrial wastewater containing oily heavy metals. The system includes a water collection well, a coarse grid, a microbubble air flotation mineral oil adsorption device, and a catalytic heavy metal desorption reaction for mineral oil. tanks, protopectin-heavy metal rotary adsorption tanks, aerated nitrification tanks, biological denitrification tanks, sedimentation tanks, water purification tanks, etc.; among them, industrial wastewater containing oil and heavy metals enters the water collection well through the waste water pipeline, and the outlet of the water collection well is connected through the waste water pipeline Coarse grid, the outlet of the coarse grid is connected to the micro-bubble air flotation mineral oil adsorption device through the waste water pipeline, and the π-allyl nickel compound modified diatomite adsorption membrane in the micro-bubble air flotation mineral oil adsorption device completely absorbs the mineral oil Afterwards, the oil will be grabbed by the stainless steel mechanical arm and sent to the mineral oil catalytic desorption reactor. The heavy oil generated in the mineral oil catalytic desorption reactor will be discharged from the heavy oil discharge port and be recycled and reused. At the same time, the microbubble gas The outlet of the floating mineral oil adsorption device is connected to the original pectin-heavy metal rotary adsorption tank through the wastewater pipeline, and the sludge discharged from the original pectin-heavy metal rotary adsorption tank is transported outside for treatment, while the outlet of the original pectin-heavy metal rotary adsorption tank passes through the waste water The pipeline is connected to the aeration nitrification tank, the outlet of the aeration nitrification tank is connected to the biological denitrification tank through the wastewater pipeline, the outlet of the biological denitrification tank is connected to the sedimentation tank through the wastewater pipeline, and the outlet of the sedimentation tank is connected to the purification tank through the wastewater pipeline, and the purification tank The treated purified effluent is discharged through the waste water pipeline; among them, the micro-bubble air flotation mineral oil adsorption device is made of high-strength glass fiber reinforced plastic, and 9 ultra-fine bubble generators are installed at the bottom of the device. It accommodates a horizontally placed π-allyl nickel compound modified diatomite adsorption membrane, with a water inlet valve on the upper left side and an outlet valve on the bottom right side; the mineral oil catalytic desorption reactor adopts high-strength Made of stainless steel, 5 electric blowers are installed at the bottom, and a set of stainless steel membrane frame is installed inside the device, and 5 pieces of π-allyl nickel compound modified diatomite adsorption membranes to be treated at high temperature are placed vertically on the membrane frame, There is a heavy oil outlet on the right side of the bottom; the waste water that has initially removed large particle size substances through the coarse grid enters the device through the water inlet valve on the upper left side of the micro-bubble air flotation mineral oil adsorption device, and 9 ultra-fine bubble generators start Work, produce ultra-fine bubbles with a diameter of less than 50 μm, the ultra-fine bubbles will entrain the mineral oil molecules in the wastewater and float together, and make them be adsorbed by the π-allyl nickel compound modified diatomite adsorption film above the liquid surface, The π-allyl nickel compound modified diatomite adsorption membrane that completely adsorbs mineral oil is grasped by a stainless steel manipulator, and placed vertically on a stainless steel membrane frame in the mineral oil catalytic reforming desorption reactor, at the bottom of the reactor The 5 electric blowers of the company can produce high-temperature air at 200~250°C. At this temperature and under the catalysis of π-allyl nickel compounds, the C-H bonds in the mineral oil molecules will be temporarily broken and quickly regenerated. The combination is a C-C bond or a C-H bond, and the C-H bond will be broken again, and the C-C bond will not be broken again due to the limited catalytic effect of the π-allyl nickel compound, so mineral oil molecules with shorter carbon chains can gradually synthesized as a carbon chain Longer heavy oil molecules, at the same time, heavy oil molecules will be desorbed from the π-allyl nickel compound modified diatomite adsorption membrane at high temperature, and will be discharged from the heavy oil discharge port on the right side of the bottom of the reactor after converging; protopectin- The heavy metal rotary adsorption pool is made of hard glass fiber reinforced plastic, and the outer layer is painted with waterproof materials. The water inlet valve is installed on the upper left side of the adsorption pool, the electric telescopic rod pushing mud device is installed on the lower left side, and the electric hook claw is installed on the upper right side. The middle part of the right side is equipped with a water outlet valve, and the lower part of the right side is equipped with a sludge discharge port. The middle part of the adsorption tank is fixed with a V-shaped mesh roller by means of a rotating shaft connecting rod, and a lifting hook is installed above the V-shaped mesh roller; microbubble air flotation mineral oil The outlet water of the adsorption device enters the interior of the adsorption tank through the water inlet valve on the left side of the original pectin-heavy metal rotary adsorption tank. The V-shaped mesh drum is fully rotated under the drive of the rotating shaft and connecting rod, so that the wastewater can fully contact with the pumpkin skin and pass through the pumpkin skin. The adsorption of water-insoluble protopectin in the cells makes the heavy metal ions in the wastewater adsorbed, and the wastewater after adsorption treatment is discharged from the adsorption pool through the outlet valve. After the V-shaped mesh roller is saturated near the suction, the electric hook can be operated. Grab the lifting hook above the V-shaped mesh roller, lift the V-shaped mesh roller away from the adsorption tank, and then complete the replacement operation of the pumpkin skin. Use the electric telescopic rod to push the sludge out of the adsorption tank through the sludge outlet, and the pumpkin peel residue replaced by the V-shaped mesh roller is combined with the sludge settled at the bottom of the adsorption tank before being transported outside for treatment.
进一步,原果胶-重金属旋转吸附池,其池体有效容积为340m3,其V型网状滚筒容积为31m3,孔径为7.5mm,其转轴连杆的工作电压为380V,转速为15转/min。Furthermore, the original pectin-heavy metal rotary adsorption tank has an effective volume of 340m 3 , a V-shaped mesh drum with a volume of 31m 3 and a hole diameter of 7.5mm. /min.
进一步,微泡气浮矿物油吸附装置,其有效容积为300m3,超微细气泡发生器能够产生直径小于50μm的超微细气泡,工作电压为36V。Furthermore, the micro-bubble air flotation mineral oil adsorption device has an effective volume of 300m 3 , and the ultra-fine bubble generator can generate ultra-fine bubbles with a diameter of less than 50 μm, and the working voltage is 36V.
进一步,π-烯丙基镍化合物改性硅藻土吸附膜的面积为12.6m2,π-烯丙基镍化合物的含量为22.4g/m2,π-烯丙基镍化合物的纯度为96.2%。Furthermore, the area of the π-allyl nickel compound modified diatomite adsorption membrane is 12.6m 2 , the content of π-allyl nickel compound is 22.4g/m 2 , and the purity of π-allyl nickel compound is 96.2 %.
本发明的优点在于:The advantages of the present invention are:
(1)本系统摆脱了现有的工业废水重金属净化处理原理,创造性的利用了含有丰富原果胶与果胶酶的南瓜皮作为重金属离子的吸附材料,采用装有南瓜皮的V型网状滚筒为接触反应介质,当含有重金属的废水与南瓜皮充分混合,通过果皮细胞中的非水溶性原果胶的吸附作用使废水中的重金属离子被吸附,从而使含重金属的工业废水得到净化,其重金属去除效率可达97.9%(1) This system gets rid of the existing principle of heavy metal purification and treatment of industrial wastewater, creatively uses pumpkin peel rich in protopectin and pectinase as the adsorption material for heavy metal ions, and adopts a V-shaped mesh with pumpkin peel The drum is the contact reaction medium. When the wastewater containing heavy metals is fully mixed with the pumpkin peel, the heavy metal ions in the wastewater will be adsorbed by the adsorption of the insoluble protopectin in the peel cells, thereby purifying the industrial wastewater containing heavy metals. Its heavy metal removal efficiency can reach 97.9%
(2)本系统摆脱了现有的工业废水矿物油净化处理模式,创造性的采用了物理手段与化学方法相结合的技术路线,充分利用改性硅藻土的吸附作用和π-烯丙基镍化合物的催化合成作用,使工业废水中的矿物油被吸附富集,并发生合成反应,生成可利用的重油,其矿物油的去除效率达到99.7%。本系统中所使用的改性硅藻土吸附膜经热解吸过程后得以再生,可被重新用于吸附废水中的矿物油,实现了物料的重复利用,大大降低了运行成本。(2) This system gets rid of the existing industrial wastewater mineral oil purification treatment mode, creatively adopts the technical route of combining physical means and chemical methods, and makes full use of the adsorption of modified diatomite and π-allyl nickel The catalytic synthesis of the compound makes the mineral oil in the industrial wastewater be adsorbed and enriched, and a synthesis reaction occurs to generate usable heavy oil, and the removal efficiency of the mineral oil reaches 99.7%. The modified diatomite adsorption membrane used in this system can be regenerated after the thermal desorption process, and can be reused to adsorb mineral oil in wastewater, realizing the reuse of materials and greatly reducing operating costs.
(3)本系统回收利用了南瓜皮这种农业生产过程中所产生的废弃物,能够实现废物利用,变废为宝,显著缩减了农业生产中的废弃物产生量;同时,南瓜皮作为一种低值耗材,可根据使用消耗情况进行替换,替换成本低。不使用任何有毒化学物质,从而消除了引入新的、危害更大的污染物的风险。(3) This system recycles pumpkin rind, which is a waste produced in the process of agricultural production, which can realize waste utilization, turn waste into treasure, and significantly reduce the amount of waste generated in agricultural production; at the same time, pumpkin rind is used as a A low-value consumable, which can be replaced according to the usage and consumption, and the replacement cost is low. No toxic chemicals are used, thereby eliminating the risk of introducing new, more harmful contaminants.
(4)本系统原理简单易行,设计施工成本较低,并且处理效果较好,运行维护成本很低,有利于大范围推广应用。(4) The principle of this system is simple and easy to implement, the cost of design and construction is low, and the treatment effect is good, and the cost of operation and maintenance is very low, which is conducive to large-scale promotion and application.
附图说明Description of drawings
图1是本发明的设备示意图。Figure 1 is a schematic diagram of the device of the present invention.
图中:1-集水井、2-粗格栅、3-微泡气浮矿物油吸附装置、4-矿物油催化重化解吸反应器、5-原果胶-重金属旋转吸附池、6-曝气硝化池、7-生物脱氮池、8-沉淀池、9-净水池In the figure: 1-water collection well, 2-coarse grid, 3-microbubble air flotation mineral oil adsorption device, 4-mineral oil catalytic heavy chemical desorption reactor, 5-protopectin-heavy metal rotary adsorption tank, 6-exposure Gas nitrification tank, 7- biological denitrification tank, 8- sedimentation tank, 9- water purification tank
图2是微泡气浮矿物油吸附装置和矿物油催化重化解吸反应器的示意图。Fig. 2 is a schematic diagram of a microbubble air flotation mineral oil adsorption device and a mineral oil catalytic reforming desorption reactor.
32-超微细气泡发生器、33-超微细气泡、34-不锈钢机械臂、35-转珠轴承、36-进水阀门、37-出水阀门;41-气凝胶毡隔热层、42-π-烯丙基镍化合物改性硅藻土吸附膜、43-不锈钢膜架、44-电热鼓风风机、45-重油排出口32-Ultrafine bubble generator, 33-Ultrafine bubble, 34-Stainless steel mechanical arm, 35-Rotary ball bearing, 36-Water inlet valve, 37-Water outlet valve; 41-Aerogel felt insulation layer, 42-π -Allyl nickel compound modified diatomite adsorption membrane, 43-stainless steel membrane frame, 44-electric blower, 45-heavy oil outlet
图3是原果胶-重金属旋转吸附池的示意图。Figure 3 is a schematic diagram of a protopectin-heavy metal spin adsorption cell.
51-玻璃钢池体、52-转轴连杆、53-V型网状滚筒、54-提钩、55-进水阀门、56-出水阀门、57-电动伸缩杆推泥装置、58-污泥排口、59-电动钩爪。51-FRP tank body, 52-Rotating shaft connecting rod, 53-V-shaped mesh drum, 54-Hook, 55-Inlet valve, 56-Outlet valve, 57-Electric telescopic rod pushing mud device, 58-Sludge discharge Mouth, 59-electric claw.
具体实施方式Detailed ways
如图1所示的去除工业废水中重金属的处理系统,该系统包括集水井1、粗格栅2、微泡气浮矿物油吸附装置3、矿物油催化重化解吸反应器4、原果胶-重金属旋转吸附池5、曝气硝化池6、生物脱氮池7、沉淀池8、净水池9;其中,含油重金属的工业废水通过废水管线进入集水井1,在此进行集中收集和初步稳定调节,集水井1的出口通过废水管线连接粗格栅2,在此去除工业废水中的大直径固体物质,粗格栅2的出口通过废水管线连接微泡气浮矿物油吸附装置3,微泡气浮矿物油吸附装置3中的含π-烯丙基镍化合物改性硅藻土吸附膜42在完全吸附矿物油后会被不锈钢机械臂34抓取,并被送入矿物油催化重化解吸反应器4,矿物油催化重化解吸反应器4中生成的重油从重油排出口45排出并被回收再利用,同时,微泡气浮矿物油吸附装置3的出口通过废水管线连接原果胶-重金属旋转吸附池5,原果胶-重金属旋转吸附池5的出口通过废水管线连接曝气硝化池6,在此通过好氧曝气过程,使废水中的各种含氮物质均转化为硝酸盐氮,曝气硝化池6的出口通过废水管线连接生物脱氮池7,其作用是通过生物活性反应过程,将废水中的硝酸盐氮分解转化,从而去除硝酸盐氮,生物脱氮池7的出口通过废水管线连接沉淀池8,在此将废水中的剩余不溶物质全部除去,沉淀池8的出口通过废水管线连接净水池9,净水池9的出口通过废水管线将经过本系统处理后的净化出水外排;其中,微泡气浮矿物油吸附装置3采用高强度玻璃钢材质,有效容积为300m3,其底部装有9支超微细气泡发生器32,能够产生直径小于50μm的超微细气泡33,装置的液面之上可容纳一张横向放置的π-烯丙基镍化合物改性硅藻土吸附膜42,该吸附膜面积为12.6m2,π-烯丙基镍化合物的含量为22.4g/m2,π-烯丙基镍化合物的纯度为96.2%,其左侧上部装有进水阀门36,右侧底部装有出水阀门37,该装置右侧壁因与高温的矿物油催化重化解吸反应器4相连,故贴覆有气凝胶毡隔热层41,气凝胶毡隔热层41顶端装有不锈钢机械臂34及转珠轴承35;矿物油催化重化解吸反应器4采用高强度不锈钢材质,容积为330m3,其底部装有5部电热鼓风风机44,能够产生200~250℃的热空气,装置内部安装有一套不锈钢膜架43,膜架上可竖直放置5张待高温处理的π-烯丙基镍化合物改性硅藻土吸附膜42,其底部右侧设有重油排出口45;经过粗格栅2初步去除大粒径物质的含有矿物油的工业废水通过微泡气浮矿物油吸附装置3左侧上部的进水阀门36进入装置内部,9支超微细气泡发生器32开始工作,产生直径小于50μm的超微细气泡33,超微细气泡33会夹带废水中的矿物油分子一同上浮,并使其被液面之上的含π-烯丙基镍化合物改性硅藻土吸附膜42吸附,完全吸附矿物油的含π-烯丙基镍化合物改性硅藻土吸附膜42被不锈钢机械臂34抓取,并被竖直放置在矿物油催化重化解吸反应器4中的不锈钢膜架43上,反应器底部的5部电热鼓风风机44开始工作,产生200~250℃的高温空气,在π-烯丙基镍化合物的催化下,矿物油分子中的C-H键会发生短暂的断裂,并快速再结合为C-C键或C-H键,而C-H键会再次发生断裂,C-C键则因π-烯丙基镍化合物的催化作用有限而不会再发生断裂,因此可使碳链较短的矿物油分子逐渐合成为碳链较长的重油分子。同时,重油分子会在高温下从含π-烯丙基镍化合物改性硅藻土吸附膜42中解吸,汇聚后从反应器底部右侧的重油排出口45排出,可被集中收集和再利用。As shown in Figure 1, the treatment system for removing heavy metals in industrial wastewater, the system includes a water collection well 1, a coarse grid 2, a microbubble air flotation mineral oil adsorption device 3, a catalytic heavy desorption reactor 4 for mineral oil, and protopectin -Heavy metal rotary adsorption tank 5, aeration nitrification tank 6, biological denitrification tank 7, sedimentation tank 8, water purification tank 9; among them, the industrial wastewater containing oil and heavy metals enters the water collection well 1 through the wastewater pipeline, where centralized collection and preliminary Stable adjustment, the outlet of the water collection well 1 is connected to the coarse grid 2 through the wastewater pipeline, where large-diameter solid matter in the industrial wastewater is removed, and the outlet of the coarse grid 2 is connected to the microbubble air flotation mineral oil adsorption device 3 through the wastewater pipeline, and the micro After the π-allyl nickel compound-modified diatomite adsorption film 42 in the air-bubble flotation mineral oil adsorption device 3 completely absorbs mineral oil, it will be grabbed by the stainless steel mechanical arm 34 and sent to the catalytic re-decomposition of mineral oil. Absorption reactor 4, the heavy oil generated in the desorption reactor 4 for catalytic heavy conversion of mineral oil is discharged from the heavy oil outlet 45 and recycled, and at the same time, the outlet of the microbubble air flotation mineral oil adsorption device 3 is connected to the original pectin -Heavy metal rotary adsorption tank 5, the outlet of protopectin-heavy metal rotary adsorption tank 5 is connected to the aeration nitrification tank 6 through the waste water pipeline, and various nitrogen-containing substances in the wastewater are converted into nitric acid through the process of aerobic aeration here Salt nitrogen, the outlet of the aeration nitrification tank 6 is connected to the biological denitrification tank 7 through the wastewater pipeline, and its function is to decompose and transform the nitrate nitrogen in the wastewater through the biological activity reaction process, thereby removing nitrate nitrogen, and the biological denitrification tank 7 The outlet of the sedimentation tank 8 is connected to the sedimentation tank 8 through the waste water pipeline, and all the remaining insoluble substances in the waste water are removed here. The outlet of the sedimentation tank 8 is connected to the clean water tank 9 through the waste water pipeline, and the outlet of the clean water tank 9 is processed by the system through the waste water pipeline. The purified effluent is discharged outside; among them, the micro-bubble air flotation mineral oil adsorption device 3 is made of high-strength fiberglass, with an effective volume of 300m 3 , and 9 ultra-fine bubble generators 32 are installed at the bottom, which can generate ultra-fine bubbles with a diameter of less than 50 μm. The micro-bubbles 33 can accommodate a horizontally placed π-allyl nickel compound modified diatomite adsorption film 42 on the liquid surface of the device. The area of the adsorption film is 12.6m 2 , and the π-allyl nickel compound The content is 22.4g/m 2 , the purity of π-allyl nickel compound is 96.2%, the water inlet valve 36 is installed on the upper left side, and the water outlet valve 37 is installed on the bottom right side. Mineral oil catalytic desorption reactor 4 is connected, so it is covered with an airgel felt insulation layer 41, and the top of the airgel felt insulation layer 41 is equipped with a stainless steel mechanical arm 34 and a ball bearing 35; The suction reactor 4 is made of high-strength stainless steel, with a volume of 330m 3 . Five electric blowers 44 are installed at the bottom, which can generate hot air at 200-250°C. A set of stainless steel membrane frame 43 is installed inside the device. Five sheets of π-allyl nickel compound modified diatomite adsorption membranes 42 to be treated at high temperature can be placed vertically, and a heavy oil outlet 45 is provided on the right side of the bottom; Mineral oil industrial waste water enters the interior of the device through the water inlet valve 36 on the upper left side of the micro-bubble air flotation mineral oil adsorption device 3, and 9 ultra-fine bubble generators 32 start to work to generate ultra-fine bubbles 33 with a diameter of less than 50 μm. Bubbles 33 will entrain the mineral oil molecules in the waste water and float up together, and make them be adsorbed by the modified diatomite adsorption film 42 containing π-allyl nickel compound on the liquid surface, completely absorbing the π-allyl containing mineral oil The nickel-based compound modified diatomite adsorption membrane 42 is grasped by the stainless steel mechanical arm 34, and placed vertically on the stainless steel membrane frame 43 in the mineral oil catalytic reforming desorption reactor 4, and the five electric heating drums at the bottom of the reactor The blower 44 starts to work to generate high-temperature air at 200~250°C. Under the catalysis of the π-allyl nickel compound, the CH bond in the mineral oil molecule will be temporarily broken and quickly recombined into a CC bond or a CH bond , and the CH bond will be broken again, and the CC bond will not be broken again due to the limited catalytic effect of the π-allyl nickel compound, so mineral oil molecules with shorter carbon chains can be gradually synthesized into longer carbon chains. heavy oil molecules. At the same time, heavy oil molecules will be desorbed from the π-allyl nickel compound-containing modified diatomite adsorption membrane 42 at high temperature, and after converging, they will be discharged from the heavy oil outlet 45 on the right side of the bottom of the reactor, which can be collected and reused .
原果胶-重金属旋转吸附池5采用硬质玻璃钢材质,外层涂刷有防水材料,吸附池左侧上方装有进水阀门55,左侧下方装有电动伸缩杆推泥装置57,右侧上方装有电动钩爪59,右侧中部装有出水阀门56,右侧下方设有污泥排口58,吸附池中部依靠转轴连杆52固定有V型网状滚筒53,V型网状滚筒53上方装有提钩54;经过pH值调节处理后(处理后pH值为7.5~8.5)的工业废水通过原果胶-重金属旋转吸附池5左侧的进水阀门55进入吸附池内部,V型网状滚筒53在转轴连杆52的驱动下充分转动,使废水与南瓜皮充分接触,通过南瓜皮细胞中的非水溶性原果胶的吸附作用使废水中的重金属离子被吸附,经过吸附处理后的废水经出水阀门56排出吸附池,V型网状滚筒53在吸附近饱和后,可操作电动钩爪59抓取V型网状滚筒53上方的提钩54,将V型网状滚筒53提离吸附池,进而完成南瓜皮的更换操作,同时,部分南瓜皮残渣在吸附池底部沉淀,逐渐形成污泥物质,可使用电动伸缩杆推泥装置57通过污泥排口58排出吸附池,V型网状滚筒53更换下的南瓜皮残渣与在吸附池底部沉淀的污泥物质合并后外运处理。The original pectin-heavy metal rotary adsorption tank 5 is made of hard fiberglass, and the outer layer is painted with waterproof material. The upper left side of the adsorption tank is equipped with a water inlet valve 55, and the lower left side is equipped with an electric telescopic rod pushing mud device 57. An electric hook 59 is installed on the top, a water outlet valve 56 is installed in the middle of the right side, and a sludge discharge port 58 is arranged on the lower right side. A lifting hook 54 is installed above the 53; the industrial waste water after the pH adjustment treatment (the pH value after treatment is 7.5~8.5) enters the interior of the adsorption pool through the water inlet valve 55 on the left side of the protopectin-heavy metal rotary adsorption pool 5, V The type mesh drum 53 is fully rotated under the drive of the rotating shaft connecting rod 52, so that the wastewater is fully contacted with the pumpkin skin, and the heavy metal ions in the wastewater are adsorbed through the adsorption of the non-water-soluble protopectin in the pumpkin skin cells. The treated wastewater is discharged from the adsorption pool through the water outlet valve 56. After the V-shaped mesh drum 53 is saturated near the suction, the electric hook 59 can be operated to grab the lifting hook 54 above the V-shaped mesh drum 53, and the V-shaped mesh drum 53 53 lifts away from the adsorption tank, and then completes the replacement operation of the pumpkin skin. At the same time, part of the pumpkin skin residue settles at the bottom of the adsorption tank and gradually forms sludge. The electric telescopic rod pusher 57 can be used to discharge the adsorption tank through the sludge discharge port 58 , the pumpkin peel residue replaced by the V-shaped mesh drum 53 is combined with the sludge material deposited at the bottom of the adsorption tank and then transported outside for treatment.
通过本系统处理后的工业废水,其重金属去除效率可达97.9%。The industrial wastewater treated by this system has a heavy metal removal efficiency of 97.9%.
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