CN102923806A - Method for processing formaldehyde wastewater through modified nanometer material - Google Patents
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Abstract
本发明涉及一种通过改性的纳米材料处理甲醛废水的方法,该方法通过改性的层状粘土纳米复合吸附材料来处理甲醛废水,处理好的甲醛废水完全能达到生化处理标准。本方法处理甲醛废水价格非常便宜,本方法在现实生活中处理甲醛废水非常方便,一般情况下甲醛废水都是酸性的,而且酸度很高,本发明的方法就是在酸性条件下进行的,但是在碱性条件下同样可以处理甲醛废水,本方法对废水的PH要求较低,在甲醛废水中,COD一般很高,还含有磷和氨氮等污染物,本方法使用的改性的层状粘土纳米复合吸附材料对这些污染物的去除都有很大的效果,所以本方法更加环保,更好的经济价值,本方法与其它去除甲醛的方法相比,工艺更加简单,而且快速,对环境的第二次污染基本为零,而且对病毒和细菌也有一定的去除效果。
The invention relates to a method for treating formaldehyde wastewater by using a modified nanometer material. The method uses a modified layered clay nanocomposite adsorption material to treat the formaldehyde wastewater, and the treated formaldehyde wastewater can fully meet the biochemical treatment standard. The price of this method for processing formaldehyde wastewater is very cheap, and this method is very convenient for processing formaldehyde wastewater in real life. Generally, formaldehyde wastewater is acidic, and the acidity is very high. The method of the present invention is carried out under acidic conditions, but in Formaldehyde wastewater can also be treated under alkaline conditions. This method has lower requirements on the pH of wastewater. In formaldehyde wastewater, COD is generally high, and it also contains pollutants such as phosphorus and ammonia nitrogen. The modified layered clay nanometer used in this method Composite adsorption materials have a great effect on the removal of these pollutants, so this method is more environmentally friendly and has better economic value. Compared with other methods for removing formaldehyde, this method has a simpler and faster process, and the first environmental protection The secondary pollution is basically zero, and it also has a certain removal effect on viruses and bacteria.
Description
技术领域 technical field
本发明涉及一种通过改性纳米材料处理甲醛废水的方法。 The invention relates to a method for treating formaldehyde wastewater by modifying nanomaterials.
背景技术 Background technique
甲醛(HCHO)是一种易溶于水、醇和醚的无色具有强烈刺激性气味的气体,是一种重要的有机原料,主要用于人工合成黏结剂。甲醛除可直接用作消毒、杀菌、防腐剂外,主要用于有机合成、合成材料、涂料、橡胶、农药等行业,其衍生产品主要有多聚甲醛、聚甲醛、酚醛树脂、脲醛树脂、氨基树脂、乌洛托产品及多元醇类等。甲醛的用途非常广泛,合成树脂、表面活性剂、塑料、橡胶、皮革、造纸、染料、制药、农药、照相胶片、炸药、建筑材料以及消毒、熏蒸和防腐过程中均要用到甲醛。虽然用途广泛,价格低廉,但是它的有毒有害性同样也在危害着人体和生物的健康,世界卫生组织2004年已经指出甲醛致癌。所以现在就有很多人研究出了去除甲醛废水的方法,但是其方法有很多局限性和不足的地方。 Formaldehyde (HCHO) is a colorless gas with a strong pungent odor that is easily soluble in water, alcohol and ether. It is an important organic raw material and is mainly used for artificial synthesis of binders. In addition to being directly used as a disinfection, sterilization and preservative, formaldehyde is mainly used in organic synthesis, synthetic materials, coatings, rubber, pesticides and other industries. Its derivative products are mainly polyformaldehyde, polyformaldehyde, phenolic resin, urea-formaldehyde resin, amino Resins, Uroto products and polyols, etc. Formaldehyde is widely used in synthetic resins, surfactants, plastics, rubber, leather, papermaking, dyes, pharmaceuticals, pesticides, photographic films, explosives, building materials, as well as in the processes of disinfection, fumigation and anticorrosion. Although it has a wide range of uses and low prices, its toxicity and harmfulness are also endangering the health of humans and organisms. The World Health Organization has pointed out that formaldehyde is carcinogenic in 2004. So now many people have studied the method of removing formaldehyde wastewater, but the method has many limitations and deficiencies.
甲醛的处理有很多方法,由于甲醛具有强还原性,多数就是使用氧化法再加后续的处理方法。氧化法有很多种,比如Fenton法、光催化氧化法、湿式氧化法、二氧化氯氧化法、超声/H2O2法等氧化法去除甲醛废水,要么就是投资成本高运行费用高,要么就是出水达不到国家污水排放标准。还有A/O(缺/氧)、A-SBR(厌氧SBR)和Carrousel氧化沟法等都是传统的生化法,生化法的最大缺点就是处理甲醛的浓度很低,处理时间很长,而且对现场条件有所限值,对微生物的要求要较高,而且费用也较高。还有一种常见的处理方法就是石灰法,在石灰存在下,甲醛会聚合生成己糖,石灰处理甲醛废水的关键是废水的必须要是碱性,且PH越大越能够更彻底的处理甲醛废水中的甲醛,所以往往出水还要用盐酸调PH,且石灰法处理废水容易使管道堵塞,而且反应温度在90摄氏度左右时对甲醛的去除时间是最短的,所以反应温度对甲醛的去除也有限值,要通过加热装置才能更好的去除甲醛。所以石灰法去除甲醛对反应条件要求较高,对设备还有堵塞可能,所以在一般条件下用石灰去除甲醛废水得到的效果也不好。往往在我们处理的这些甲醛废水中并不止要去除甲醛,一般废水中还要处理COD,氨氮,总磷,色度等等,而这些方法往往不能满足我们处理废水的要求,针对以上处理甲醛废水我们研究出了一种处理甲醛废水的新方法,就是用一种新型纳米材料来处理甲醛废水。 There are many ways to deal with formaldehyde. Since formaldehyde has strong reducing properties, most of them use oxidation and subsequent treatment methods. There are many oxidation methods, such as Fenton method, photocatalytic oxidation method, wet oxidation method, chlorine dioxide oxidation method, ultrasonic/H 2 O 2 method and other oxidation methods to remove formaldehyde wastewater, either the investment cost is high and the operation cost is high, or the The effluent does not meet the national sewage discharge standards. There are also A/O (deficiency/oxygen), A-SBR (anaerobic SBR) and Carrousel oxidation ditch method, which are all traditional biochemical methods. The biggest disadvantage of biochemical methods is that the concentration of formaldehyde is very low and the treatment time is very long. Moreover, there are limits to on-site conditions, higher requirements on microorganisms, and higher costs. Another common treatment method is the lime method. In the presence of lime, formaldehyde will polymerize to form hexose. The key to lime treatment of formaldehyde wastewater is that the wastewater must be alkaline, and the greater the pH, the more thoroughly the formaldehyde in the wastewater can be treated. Formaldehyde, so it is often necessary to adjust the pH of the effluent with hydrochloric acid, and the lime method is easy to block the pipeline, and the removal time of formaldehyde is the shortest when the reaction temperature is around 90 degrees Celsius, so the reaction temperature has a limited value for the removal of formaldehyde. It is better to remove formaldehyde by heating device. Therefore, the removal of formaldehyde by the lime method has high requirements on the reaction conditions, and there is a possibility of clogging the equipment, so the effect of removing formaldehyde wastewater by lime is not good under general conditions. Often in the formaldehyde wastewater we treat, not only formaldehyde needs to be removed, but COD, ammonia nitrogen, total phosphorus, chroma, etc. are also treated in general wastewater, and these methods often cannot meet our wastewater treatment requirements. For the above treatment of formaldehyde wastewater We have developed a new method for treating formaldehyde wastewater, which is to use a new nanomaterial to treat formaldehyde wastewater.
发明内容 Contents of the invention
本发明的目的是提供一种便捷快速,工艺简单,处理成本低的通过改性纳米材料处理甲醛废水的方法,经本方法处理的甲醛废水得到了很好的去除效果。 The purpose of the present invention is to provide a method for treating formaldehyde wastewater through modified nano-materials which is convenient, fast, simple in process and low in treatment cost. The formaldehyde wastewater treated by the method has a good removal effect.
本方法中用到了一种新型纳米材料,纳米材料就是指在三维空间中至少有一维处于纳米尺度范围(1-100nm)或由它们作为基本单元构成的材料,这种新型纳米材料是由纳米级颗粒(1-100nm)组成的粘土矿物,是由两个硅氧四面体夹一层铝氧四面体组成的2:1型晶体结构,而本发明中使用的是改性的层状粘土纳米复合吸附材料做原料,先经过高温改性,然后粉碎为一百目左右,然后加水浸泡制浆,通过沉降除去粗渣,再加盐酸酸化,用蒸馏水洗涤,烘干,就可以制造改性的层状粘土纳米复合吸附材料,酸活化可以增加该纳米材料的比表面积及表面酸位浓度,除去孔道中的杂质,进而提高其活性。该材料的比表面积大,可达600-800平方米/克,巨大的表面积产生巨大的表面能,还有其层状结构以及结构中元素的类型与分布共同决定了其具有了很强的吸附性能,在改性过程中层状粘土纳米复合吸附材料层间金属阳离子溶解于酸,层间键能削弱,层间距变大,表面活性增加,金属阳离子被酸中氢离子置换后,一部分氢离子又被溶液中的铝离子取代,可以形成吸附能力更强的铝离子,从而大大提高改性的层状粘土纳米复合吸附材料的吸附性能。这种改性的层状粘土纳米复合吸附材料主要通过吸附甲醛的方式去除甲醛。 A new type of nanomaterial is used in this method. Nanomaterials refer to materials that have at least one dimension in the nanoscale range (1-100nm) in three-dimensional space or are made of them as basic units. This new type of nanomaterial is composed of nanoscale The clay mineral of particle (1-100nm) is made up of two silicon-oxygen tetrahedrons sandwiching a layer of aluminum-oxygen tetrahedron with a 2:1 type crystal structure, and what is used in the present invention is a modified layered clay nanocomposite Adsorption materials are used as raw materials, which are firstly modified at high temperature, then crushed into about 100 meshes, then soaked in water to make pulp, and the coarse residue is removed by sedimentation, then acidified with hydrochloric acid, washed with distilled water, and dried, and the modified layer can be produced Clay nanocomposite adsorption material, acid activation can increase the specific surface area and surface acid site concentration of the nanomaterial, remove impurities in the pores, and then improve its activity. The specific surface area of the material is large, up to 600-800 square meters per gram. The huge surface area produces huge surface energy, as well as its layered structure and the type and distribution of elements in the structure determine its strong adsorption. Performance, during the modification process, the interlayer metal cations of the layered clay nanocomposite adsorption material are dissolved in the acid, the interlayer bond energy is weakened, the interlayer distance becomes larger, and the surface activity increases. After the metal cations are replaced by hydrogen ions in the acid, a part of the hydrogen ions Replaced by aluminum ions in the solution, aluminum ions with stronger adsorption capacity can be formed, thereby greatly improving the adsorption performance of the modified layered clay nanocomposite adsorption material. The modified layered clay nanocomposite adsorption material mainly removes formaldehyde by adsorbing formaldehyde.
为了把甲醛废水处理到能按照国家排放标准排放的状况下,本发明提出的通过改性纳米材料处理处理甲醛废水的方法,具体步骤如下: In order to treat formaldehyde waste water to the situation that can be discharged according to national discharge standards, the method proposed by the present invention for processing formaldehyde waste water by modified nanomaterials, the specific steps are as follows:
(1)先把层状粘土纳米复合吸附材料在390-410℃温度下煅烧,使其失去表面水、水化水结构骨架中的结合水,减少水膜对甲醛、磷和氨氮的吸附阻力;然后冷却和碾磨过筛,粉碎为90-110目,再经过酸化法对其改性,加水浸泡制浆,通过沉降除去粗渣,再加盐酸酸化,用蒸馏水洗涤,烘干,就可以制造改性的层状粘土纳米复合吸附材料; (1) Calcining the layered clay nanocomposite adsorption material at a temperature of 390-410°C to make it lose surface water and bound water in the hydration water structure skeleton, and reduce the adsorption resistance of the water film to formaldehyde, phosphorus and ammonia nitrogen; Then cool, grind and sieve, pulverize into 90-110 mesh, then modify it by acidification method, soak it in water to make pulp, remove the coarse residue by sedimentation, acidify it with hydrochloric acid, wash it with distilled water, and dry it to produce Modified layered clay nanocomposite adsorption material;
(2)向废水中加入步骤(1)所得层状粘土纳米复合吸附材料,反应温度为10~80℃,反应时间为0.5~24小时,搅拌速度为每分钟115-125转,搅拌8-15分钟后,静置时间18-25分钟,过滤,每毫克甲醛中加入3.8-4.2克层状粘土纳米复合吸附材料,处理好的甲醛废水排放,排放时控制甲醛废水的PH值为6~9,经本方法处理的甲醛废水可以达到国家一级排放标准。在多次实验中我们使用的甲醛废水中甲醛的浓度是120.48毫克每升。 (2) Add the layered clay nanocomposite adsorption material obtained in step (1) to the wastewater, the reaction temperature is 10-80°C, the reaction time is 0.5-24 hours, the stirring speed is 115-125 revolutions per minute, and the stirring time is 8-15 hours. After 10 minutes, let it stand for 18-25 minutes, filter, add 3.8-4.2 grams of layered clay nanocomposite adsorption materials per milligram of formaldehyde, and discharge the treated formaldehyde wastewater. When discharging, control the pH value of the formaldehyde wastewater to 6-9. The formaldehyde wastewater treated by the method can reach the national first-class discharge standard. The concentration of formaldehyde in the formaldehyde wastewater we used in many experiments was 120.48 mg per liter.
本发明中,所述步骤(1)中所述层状粘土纳米复合吸附材料为蒙脱石、沸石或硅藻土等中任一种,由1-100nm纳米级颗粒组成的粘土矿物,是由两个硅氧四面体夹一层铝氧四面体组成的2:1型晶体结构。 In the present invention, the layered clay nanocomposite adsorption material described in the step (1) is any one of montmorillonite, zeolite or diatomaceous earth, etc., and is composed of 1-100nm nanoscale particles of clay minerals, which are composed of A 2:1 crystal structure consisting of two silicon-oxygen tetrahedrons sandwiching a layer of aluminum-oxygen tetrahedrons.
影响本发明处理甲醛废水的效果主要因素有:甲醛初始浓度、反应温度、改性的层状粘土纳米复合吸附材料的加入量、废水PH值等。一般情况下,改性的层状粘土纳米复合吸附材料加入越多越能够彻底的去除甲醛,甲醛的处理效果越好,但是当甲醛浓度在50微克每升左右时继续加入改性的层状粘土纳米复合吸附材料就没有效果。 The main factors affecting the effect of the present invention on treating formaldehyde wastewater include: initial concentration of formaldehyde, reaction temperature, addition of modified layered clay nanocomposite adsorption material, pH value of wastewater, and the like. In general, the more the modified layered clay nanocomposite adsorption material is added, the more formaldehyde can be completely removed, and the treatment effect of formaldehyde is better, but when the formaldehyde concentration is about 50 micrograms per liter, continue to add modified layered clay Nanocomposite adsorbent materials are not effective.
本发明的优点如下: The advantages of the present invention are as follows:
一、本方法处理甲醛废水价格非常便宜,改性的层状粘土纳米复合吸附材料在我国储量非常丰富,而且分布非常广泛,所以在资源上为甲醛废水处理奠定了物质基础; 1. The price of this method to treat formaldehyde wastewater is very cheap. The modified layered clay nanocomposite adsorption material is very abundant in my country and widely distributed, so it has laid a material foundation for the treatment of formaldehyde wastewater in terms of resources;
二、本方法在我们现实生活中处理甲醛废水非常方便,一般情况下甲醛废水都是酸性的,而且酸度很高,本发明的方法就是在酸性条件下进行的,但是在碱性条件下同样可以处理甲醛废水,本方法对废水的PH要求较低,所以所花成本更低; Two, this method is very convenient in our real life to process formaldehyde waste water, and formaldehyde waste water is all acidic under normal circumstances, and acidity is very high, and the method of the present invention is exactly carried out under acidic conditions, but can be equally possible under alkaline conditions For the treatment of formaldehyde wastewater, this method has lower requirements on the pH of the wastewater, so the cost is lower;
三、在甲醛废水中,COD一般很高,还含有磷和氨氮等污染物,本方法使用的氢改性的层状粘土纳米复合吸附材料对这些污染物的去除都有很大的效果,所以本方法更加环保,更好的经济价值; Three, in formaldehyde waste water, COD is generally very high, also contains pollutants such as phosphorus and ammonia nitrogen, the layered clay nanocomposite adsorption material of hydrogen modification that this method uses all has very big effect to the removal of these pollutants, so This method is more environmentally friendly and has better economic value;
四、本方法与其它去除甲醛的方法相比,工艺更加简单,而且快速,对环境的第二次污染基本为零。 4. Compared with other methods for removing formaldehyde, this method has a simpler and faster process, and the second pollution to the environment is basically zero.
附图说明 Description of drawings
图1为本发明的工艺流程图。 Fig. 1 is a process flow diagram of the present invention.
图2为本发明实施例1的甲醛、氨氮和总磷的去除率图。 Fig. 2 is the removal rate diagram of formaldehyde, ammonia nitrogen and total phosphorus in Example 1 of the present invention.
图3为本发明实施例2的不同PH下所测得的甲醛、氨氮和总磷的去除率图。 Figure 3 is a graph showing the removal rates of formaldehyde, ammonia nitrogen and total phosphorus measured at different pHs in Example 2 of the present invention.
图4为本发明实施例3的不同加药量的去除率图。 Fig. 4 is a removal rate diagram of different dosages of Example 3 of the present invention.
图中标号:1为干式投加仪器,2为搅拌机,3为反应池,4为沉淀池,5为过滤池。 Numbers in the figure: 1 is a dry dosing instrument, 2 is a mixer, 3 is a reaction tank, 4 is a sedimentation tank, and 5 is a filter tank.
具体实施方式 Detailed ways
下面通过实施例进一步说明本发明。 The present invention is further illustrated below by way of examples.
本发明以某地的封闭河道污水为例,该河道水周围有大量的化工厂,使得该河道水中含有大量的甲醛、磷和氨氮,通过本例来进一步说明甲醛废水的处理过程和效果。 The present invention takes closed river sewage in a certain place as an example. There are a large number of chemical plants around the river water, which makes the river water contain a large amount of formaldehyde, phosphorus and ammonia nitrogen. This example further illustrates the treatment process and effect of formaldehyde wastewater.
本发明方法,具体步骤如下: The inventive method, concrete steps are as follows:
第一步:通过物理方法和化学方法对层状粘土纳米复合吸附材料进行改性 Step 1: Modification of layered clay nanocomposite adsorption materials by physical and chemical methods
先把层状粘土纳米复合吸附材料在高温下煅烧一段时间,然后冷却和碾磨过筛,在400℃下煅烧层状粘土纳米复合吸附材料,使其失去表面水、水化水结构骨架中的结合水,减少水膜对甲醛、磷和氨氮的吸附阻力。经过高温改性后的层状粘土纳米复合吸附材料,然后粉碎为一百目左右,再经过酸化法对其改性,加水浸泡制浆,通过沉降除去粗渣,再加盐酸酸化,用蒸馏水洗涤,烘干,就可以制造改性的层状粘土纳米复合吸附材料。 First, the layered clay nanocomposite adsorption material is calcined at high temperature for a period of time, then cooled, ground and sieved, and the layered clay nanocomposite adsorption material is calcined at 400°C to lose surface water and hydration water in the structural skeleton. Combine water to reduce the adsorption resistance of water film to formaldehyde, phosphorus and ammonia nitrogen. The layered clay nanocomposite adsorption material modified by high temperature is then crushed into about 100 meshes, then modified by acidification method, soaked in water to make pulp, and the coarse residue is removed by sedimentation, then acidified with hydrochloric acid and washed with distilled water , and dried, the modified layered clay nanocomposite adsorption material can be manufactured.
第二步:在废水中投加改性的层状粘土纳米复合吸附材料 Step 2: Dosing modified layered clay nanocomposite adsorption materials in wastewater
经过多次实验得出的结果显示,在废水中投加的药剂并不是越多越好,在3.8-4.2克药剂每毫克甲醛情况下甲醛废水的处理情况是最好的。在多次实验中我们使用的甲醛废水中甲醛的浓度是120.48毫克每升。 The results obtained after many experiments show that the more chemicals added to the wastewater is not the better, and the treatment of formaldehyde wastewater is the best under the condition of 3.8-4.2 grams of chemicals per mg of formaldehyde. The concentration of formaldehyde in the formaldehyde wastewater we used in many experiments was 120.48 mg per liter.
第三步:搅拌 Step 3: Stir
把改性的层状粘土纳米复合吸附材料跟甲醛废水按照一定的比例进行混合,通过搅拌机搅拌,使改性的层状粘土纳米复合吸附材料跟甲醛废水充分混合。 The modified layered clay nanocomposite adsorption material is mixed with the formaldehyde wastewater according to a certain ratio, and stirred by a mixer to fully mix the modified layered clay nanocomposite adsorption material with the formaldehyde wastewater.
第四步:沉淀 Step Four: Precipitation
搅拌一定时间以后,因为层状粘土纳米复合吸附材料是不溶于水的,在自然状态下,让改性的层状粘土纳米复合吸附材料自然沉降,通过排泥装置把沉淀物排除。 After stirring for a certain period of time, because the layered clay nanocomposite adsorption material is insoluble in water, in the natural state, the modified layered clay nanocomposite adsorption material is allowed to settle naturally, and the sediment is removed through the mud discharge device.
第五步:过滤 Step Five: Filter
改性的层状粘土纳米复合吸附材料沉淀以后,剩下的甲醛废水中还有一部分悬浮物,通过过滤装置把悬浮物过滤掉。 After the modified layered clay nanocomposite adsorption material is precipitated, there is still a part of suspended matter in the remaining formaldehyde wastewater, and the suspended matter is filtered out by a filter device.
第六步:调PH值 Step 6: Adjust the PH value
在实际操作中,甲醛废水一般都是呈现酸性的,把处理好的甲醛废水排出去必须要调回PH值(6~9)。 In actual operation, formaldehyde wastewater is generally acidic, and the pH value (6-9) must be adjusted to discharge the treated formaldehyde wastewater.
第七步:排放 Step Seven: Drain
根据相关法律法规,把处理好的甲醛废水排除或进入当地的污水管网中。 According to relevant laws and regulations, the treated formaldehyde wastewater should be discharged or entered into the local sewage pipe network.
实施例1 Example 1
反应温度20℃,改性的层状粘土纳米复合吸附材料和甲醛的质量比为4g:1mg,取浓度为120.48mg.L-1 的甲醛废水溶液其中氨氮为15.6mg.L-1 、总磷为3.1mg.L-1放入容器,分别在30、45、60、75和90分钟所测得的甲醛、氨氮和总磷的去除率如图2所示,对甲醛的去除在60分钟的时候几乎可以达到100%,对氨氮的去除效果不好,在60分钟的时候去除率也只有42%,对磷的去除效果比氨氮要好,去除率可以达到62%。虽然对氨氮和磷的去除率达到了42%和62%,但是它们的初始量很低,该材料对氨氮和磷的吸附量不高。总之,该纳米材料对甲醛的吸附效果非常好,但是对氨氮和磷的吸附量不高。 The reaction temperature is 20°C, the mass ratio of the modified layered clay nanocomposite adsorption material to formaldehyde is 4g:1mg, and the formaldehyde wastewater solution with a concentration of 120.48mg.L -1 is taken, in which ammonia nitrogen is 15.6mg.L -1 and total phosphorus 3.1mg.L -1 was put into the container, and the removal rates of formaldehyde, ammonia nitrogen and total phosphorus measured in 30, 45, 60, 75 and 90 minutes were shown in Figure 2, and the removal of formaldehyde in 60 minutes It can almost reach 100% in time, and the removal effect on ammonia nitrogen is not good, and the removal rate is only 42% in 60 minutes. The removal effect on phosphorus is better than that of ammonia nitrogen, and the removal rate can reach 62%. Although the removal efficiencies of ammonia nitrogen and phosphorus reached 42% and 62%, but their initial amounts were very low, and the adsorption capacity of the material for ammonia nitrogen and phosphorus was not high. In short, the nanomaterials have a very good adsorption effect on formaldehyde, but the adsorption capacity on ammonia nitrogen and phosphorus is not high.
实施例2 Example 2
反应温度40℃,改性的层状粘土纳米复合吸附材料和甲醛的质量比为4g:1mg,取浓度为120.48mg.L-1 的甲醛废水溶液其中氨氮为15.6mg.L-1 、总磷为3.1mg.L-1放入容器,不同PH下所测得的甲醛、氨氮和总磷的去除率如图3所示,在PH=6的时候对甲醛的处理效果是最好的,在其他情况下处理效果都要差很多,只能达到85%左右,氨氮和磷的处理效果跟甲醛的处理效果显示差不多,都是在PH=6的时候最好,但是氨氮和磷的最好处理率只有43%和64%。总之,该纳米材料对对甲醛的吸附效果非常好,但是对氨氮和磷的吸附量不高。 The reaction temperature is 40°C, the mass ratio of the modified layered clay nanocomposite adsorption material to formaldehyde is 4g:1mg, and the formaldehyde wastewater solution with a concentration of 120.48mg.L -1 is taken, in which ammonia nitrogen is 15.6mg.L -1 and total phosphorus 3.1mg.L -1 was placed in the container, and the removal rates of formaldehyde, ammonia nitrogen and total phosphorus measured at different pH are shown in Figure 3. The treatment effect on formaldehyde is the best when the pH is 6. In other cases, the treatment effect is much worse, and can only reach about 85%. The treatment effect of ammonia nitrogen and phosphorus is similar to that of formaldehyde. It is best when PH=6, but the treatment of ammonia nitrogen and phosphorus is the best. The rate is only 43% and 64%. In short, the nanomaterial has a very good adsorption effect on formaldehyde, but the adsorption amount on ammonia nitrogen and phosphorus is not high.
实施例3 Example 3
反应温度20℃,调节改性的层状粘土纳米复合吸附材料土和甲醛的质量比,取浓度为120.48mg.L-1 的甲醛废水溶液其中氨氮为15.6mg.L-1 、总磷为3.1mg.L-1放入容器,分别加入1g、2g、4g、8g和12g的吸附材料,处理一个小时以后,测得的甲醛浓度数据如图4所示,甲醛、氨氮和磷的去除率都随着加药量的增加而增加,但是到一定程度去除率就不再增加了。 The reaction temperature is 20°C, the mass ratio of the modified layered clay nanocomposite adsorption material soil to formaldehyde is adjusted, and the formaldehyde wastewater solution with a concentration of 120.48 mg.L -1 is taken, wherein the ammonia nitrogen is 15.6 mg.L -1 and the total phosphorus is 3.1 mg.L -1 was put into the container, and 1g, 2g, 4g, 8g and 12g of adsorption materials were added respectively. After one hour of treatment, the measured formaldehyde concentration data was shown in Figure 4. The removal rates of formaldehyde, ammonia nitrogen and phosphorus were all It increases with the increase of dosage, but the removal rate does not increase to a certain extent.
通过以上实施例可以说明通过本发明处理甲醛废水有非常好的处理效果,通过本方法处理的甲醛废水最后的甲醛的浓度为0.52mg.L-1 ,氨氮为7.39mg.L-1 和磷为0.85mg.L-1 。通过中华人民共和国国家标准城镇污水处理厂污染物排放标准(见表一和表二)可知,该污水完全符合一级排放A级排放标准,所以该方法切实可行,是有效的处理甲醛废水的方法。 It can be illustrated by the above examples that the treatment of formaldehyde wastewater by the present invention has a very good treatment effect. The final concentration of formaldehyde in the formaldehyde wastewater treated by this method is 0.52 mg.L -1 , ammonia nitrogen is 7.39 mg.L -1 and phosphorus is 0.85 mg.L -1 . According to the National Standards of the People's Republic of China on the pollutant discharge standards of urban sewage treatment plants (see Table 1 and Table 2), it can be seen that the sewage fully meets the first-level discharge A-level discharge standards, so this method is feasible and effective for the treatment of formaldehyde wastewater. .
表1: Table 1:
表2: Table 2:
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