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CN1214995C - Decolouring method of printing and dyeing waste water - Google Patents

Decolouring method of printing and dyeing waste water Download PDF

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CN1214995C
CN1214995C CN 03100824 CN03100824A CN1214995C CN 1214995 C CN1214995 C CN 1214995C CN 03100824 CN03100824 CN 03100824 CN 03100824 A CN03100824 A CN 03100824A CN 1214995 C CN1214995 C CN 1214995C
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decolorization
reaction
printing
waste water
natural manganese
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CN1429775A (en
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鲁安怀
杨欣
李改云
高翔
李巧荣
王长秋
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Peking University
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Abstract

本发明提供了一种印染废水的脱色方法,包括以下步骤:调节废水的pH值至呈酸性;加入天然锰钾矿,搅拌反应几个小时即可。所述方法中,反应溶液酸度越大,反应进行得越快;天然锰钾矿用量越多、粒径越小,越有利于脱色反应;在废水中加入电解质硝酸钙有助于脱色反应;光照也有利于脱色反应的进行。本发明的脱色方法所采用的脱色剂天然锰钾矿原料易得,成本低,无二次污染,应用范围广泛,脱色效果明显。另外,天然锰钾矿处理印染废水后,还可以重复使用。

The invention provides a decolorization method of printing and dyeing wastewater, comprising the following steps: adjusting the pH value of the wastewater to be acidic; adding natural manganese potassium ore, and stirring for several hours. In the method, the greater the acidity of the reaction solution, the faster the reaction proceeds; the more the amount of natural manganese-potassium ore and the smaller the particle size, the more conducive to the decolorization reaction; adding electrolyte calcium nitrate to the waste water is helpful for the decolorization reaction; Illumination is also conducive to the decolorization reaction. The decolorizing agent used in the decolorizing method of the present invention has easy-to-obtain natural manganese-potassium ore raw materials, low cost, no secondary pollution, wide application range and obvious decolorizing effect. In addition, natural manganese and potassium ore can be reused after treating printing and dyeing wastewater.

Description

一种印染废水的脱色方法A kind of decolorization method of printing and dyeing wastewater

技术领域:Technical field:

本发明属于废水处理技术领域,尤其涉及印染废水的脱色方法。The invention belongs to the technical field of wastewater treatment, in particular to a decolorization method for printing and dyeing wastewater.

背景技术:Background technique:

当今,全球合成染料年产量约为100万吨,其中我国约占20%。染料生产投入的原料大部分是芳烃化合物和杂环化合物,因而使生产过程中所排放的废水绝大多数是以苯、萘、蒽、醌等芳香团作为母体的有机物,带有显色集团,颜色很深,色度达500-500000,有很强的污染感。如果直接排放,将会对水源造成严重污染,因此研究染料废水的处理对保护生态环境和人类健康有很重要的意义。目前,工业上常用的染料废水处理方法有絮凝沉淀法、电解法、氧化法、吸附法和生物降解法等。但是,这些方法普遍具有成本高,时效短且有二次污染等缺点。Today, the annual output of synthetic dyes in the world is about 1 million tons, of which my country accounts for about 20%. Most of the raw materials input into dye production are aromatic compounds and heterocyclic compounds, so that most of the wastewater discharged during the production process is organic matter with aromatic groups such as benzene, naphthalene, anthracene, and quinone as the parent, with chromogenic groups, The color is very dark, with a chroma of 500-500,000, and has a strong sense of pollution. If it is discharged directly, it will cause serious pollution to water sources. Therefore, it is of great significance to study the treatment of dye wastewater to protect the ecological environment and human health. At present, the commonly used dye wastewater treatment methods in industry include flocculation precipitation method, electrolysis method, oxidation method, adsorption method and biodegradation method. However, these methods generally have the disadvantages of high cost, short timeliness and secondary pollution.

目前,国内外关于锰的氧化物对印染废水的降解研究大都是人工合成产物,利用天然锰钾矿对印染废水的氧化降解研究未见报道。At present, most of the researches on the degradation of printing and dyeing wastewater by manganese oxides at home and abroad are artificially synthesized products, and there is no report on the oxidative degradation of printing and dyeing wastewater by using natural manganese potassium ore.

发明内容:Invention content:

本发明的目的是提供一种成本低、应用范围广泛、无二次污染的印染废水的脱色方法。The purpose of the present invention is to provide a method for decolorizing printing and dyeing wastewater with low cost, wide application range and no secondary pollution.

本发明的技术方案如下:Technical scheme of the present invention is as follows:

一种印染废水的脱色方法,包括以下步骤:A method for decolorizing printing and dyeing wastewater, comprising the following steps:

(1)调节废水的pH值至呈酸性(如果印染废水本身已是酸性,则可以省略本步骤);(1) Adjust the pH value of the wastewater to be acidic (if the printing and dyeing wastewater itself is already acidic, this step can be omitted);

(2)加入天然锰钾矿,搅拌反应几个小时即可。(2) Add natural manganese potassium ore, stir and react for several hours.

所述方法中,反应溶液酸度越大,反应进行得越快,当废水的pH值调节为4以下时,效果最佳。In the method, the greater the acidity of the reaction solution, the faster the reaction will proceed, and the effect will be the best when the pH value of the wastewater is adjusted to be below 4.

所述天然锰钾矿用量越多、粒径越小,越有利于脱色反应,推荐粒径为160-200目。The more the natural manganese ore is used and the smaller the particle size is, the more favorable the decolorization reaction is, and the recommended particle size is 160-200 mesh.

所述方法中,在废水中加入电解质硝酸钙有助于脱色反应。光照也有利于脱色反应的进行。In the method, the electrolyte calcium nitrate is added to the waste water to facilitate the decolorization reaction. Illumination is also conducive to the decolorization reaction.

本发明脱色方法的主要机理为:天然锰钾矿因含有变价的Mn4+和Mn2+会表现出良好的氧化还原性,当锰钾矿与某些易被氧化或还原的分子或离子发生化学反应时,可表现为两种性质,一是Mn4+易获得电子被还原为低价的Mn3+或Mn2+,而与其相作用的离子或分子则失去电子被氧化。二是低价Mn2+可与某些高价阳离子反应,将其还原为低价离子。天然锰钾矿和染料发生了氧化还原反应,使其脱色。The main mechanism of the decolorization method of the present invention is: natural manganese ore will show good oxidation-reduction property because of containing the Mn 4+ and Mn 2+ of changing valence, when manganese ore reacts with some easily oxidized or reduced molecules or ions During the chemical reaction, there are two properties. One is that Mn 4+ easily obtains electrons and is reduced to low-priced Mn 3+ or Mn 2+ , while the ions or molecules interacting with it lose electrons and are oxidized. Second, low-valence Mn 2+ can react with certain high-valence cations and reduce them to low-valence ions. A redox reaction occurs between the natural manganite and the dye, which decolorizes it.

本发明的脱色方法应用十分广泛,对不同的染料废水均具有良好的脱色效果。利用本发明的方法,采用采自湘潭锰矿的天然锰钾矿样品,对天津新欣染料厂生产的X-3B、K-2BP、X-BR、X-R、K-BR、K-GN、X-8B、K-G、X-GN、M-3RE等十种工业常用染料形成的废水进行脱色试验,都有很好的效果。The decolorization method of the invention is widely used and has good decolorization effects on different dye wastewaters. Utilize the method of the present invention, adopt the natural manganese potassium ore sample that adopts from Xiangtan manganese ore, to the X-3B, K-2BP, X-BR, X-R, K-BR, K-GN, X- that Tianjin Xinxin dyestuff factory produces 8B, K-G, X-GN, M-3RE and other ten kinds of dyes commonly used in industry have been used in the decolorization test, and all of them have good results.

一、就X-3B染料进行了实验研究。1. Experimental research on X-3B dye was carried out.

所用天然锰钾矿样品采自湘潭锰矿,经自来水冲洗、自然干燥、破碎、筛分等预处理后备用。印染废水由500ppm染料储备液和去离子水配制,所用染料X-3B为天津新欣染料厂生产的工业常用染料。pH值由HNO3和NaOH调节。实验所用试剂均为分析纯,所用水为去离子水。实验所用仪器主要有HP-8453紫外可见分光光度计,80-2B离心机,PHS-2C数字式酸度计,HZS-H型水浴恒温振荡器等。The natural manganese and potassium ore samples used were collected from Xiangtan manganese ore, washed with tap water, dried naturally, crushed, sieved and other pretreatments before use. Printing and dyeing wastewater was prepared from 500ppm dye stock solution and deionized water. The dye X-3B used was a common industrial dye produced by Tianjin Xinxin Dye Factory. The pH was adjusted by HNO3 and NaOH. The reagents used in the experiments were of analytical grade, and the water used was deionized water. The instruments used in the experiment mainly include HP-8453 UV-Vis spectrophotometer, 80-2B centrifuge, PHS-2C digital acidity meter, HZS-H water bath constant temperature oscillator, etc.

实验过程:在100ml锥形瓶中加入一定量及一定粒度的矿样,再加入50ml,20mg/L的印染废水,溶液pH值由HNO3和NaOH调节。然后放入水浴恒温振荡器内,在25℃(误差不超过+1℃),200r/min条件下振荡一定时间,取出后立即用0.2微米微孔滤膜过滤,滤液于紫外分光光度计测定染料的浓度。计算染料的脱色率。Experimental process: Add a certain amount and a certain particle size of mineral samples into a 100ml Erlenmeyer flask, then add 50ml, 20mg/L printing and dyeing wastewater, and the pH of the solution is adjusted by HNO 3 and NaOH. Then put it into a constant temperature oscillator in a water bath, shake for a certain period of time at 25°C (the error does not exceed +1°C), and 200r/min. After taking it out, filter it with a 0.2 micron microporous membrane immediately, and measure the dye with a UV spectrophotometer. concentration. Calculate the decolorization rate of the dye.

在一定浓度范围内,X-3B的浓度与它的吸光度符合朗伯—比耳定律:Within a certain concentration range, the concentration of X-3B and its absorbance conform to the Lambert-Beer law:

                  A=εbcA=εbc

ε为摩尔吸光系数,其单位为L.mol-1.cm-1,b为液层厚度(以cm为单位),c表示摩尔浓度用mol.L-1表示。本实验利用此原理在一定的浓度范围内用HP-8453紫外可见分光光度计于559纳米处测量溶液的吸光度从而得到不同X-3B溶液的浓度。根据以下公式计算染料脱色率,t时刻染料的脱色率表示为:ε is the molar absorptivity, and its unit is L.mol -1 .cm -1 , b is the thickness of the liquid layer (in cm), and c is the molar concentration expressed in mol.L -1 . This experiment uses this principle to measure the absorbance of the solution at 559 nanometers with a HP-8453 UV-Vis spectrophotometer within a certain concentration range to obtain the concentration of different X-3B solutions. Calculate the dye decolorization rate according to the following formula, and the decolorization rate of the dye at time t is expressed as:

                  st=((c0-ct)/c0)×100%      st = ((c0-ct)/c0) × 100%

其中st代表某时刻X-3B的脱色率;c0、ct分别代表初始时刻和中间t时刻染料的浓度。Among them, st represents the decolorization rate of X-3B at a certain moment; c0 and ct represent the concentration of the dye at the initial moment and the middle t moment, respectively.

实验结果:Experimental results:

当160-200目锰钾矿用量为0.2g,反应pH值为3,反应温度为25℃,振荡速度为200r/min,反应半小时,对初始浓度为20mg/l的X-3B印染废水的脱色率几乎达到100%。同时,我们发现,介质pH值、样品用量与粒径大小、共存电解质、反应时间、光照对染料脱色反应有影响。介质pH值是最重要的影响因素,其与X-3B脱色率之间的关系见附图1,由图1可见,反应溶液酸度越大,反应进行得越快;当pH>3时,pH值微小的改变对X-3B脱色率影响很大,脱色率随pH的降低而增大;PH=3时,反应20分钟,脱色率就可达到99.48%;pH<3时,pH值的变化对脱色率的影响不大。样品用量越多、粒径越小,越有利于脱色反应;共存电解质硝酸钙有助于脱色反应,而磷酸钠的存在则不利于脱色反应。光照也有利于脱色反应的进行。锰钾矿还可以重复使用,表一所示为锰钾矿重复使用时的脱色结果。When the dosage of 160-200 mesh manganese potassium ore is 0.2g, the reaction pH value is 3, the reaction temperature is 25°C, the oscillation speed is 200r/min, and the reaction is half an hour, the X-3B printing and dyeing wastewater with an initial concentration of 20mg/l The decolorization rate is almost 100%. At the same time, we found that the pH value of the medium, sample amount and particle size, coexisting electrolyte, reaction time, and light had an impact on the dye decolorization reaction. The pH value of the medium is the most important influencing factor, and the relationship between it and the X-3B decolorization rate is shown in Figure 1, as can be seen from Figure 1, the greater the acidity of the reaction solution, the faster the reaction; when pH>3, the pH The small change of the value has a great influence on the decolorization rate of X-3B, and the decolorization rate increases with the decrease of pH; when PH=3, the decolorization rate can reach 99.48% after 20 minutes of reaction; when pH<3, the change of pH value Little effect on decolorization rate. The more samples used and the smaller the particle size, the more favorable the decolorization reaction; the coexistence of electrolyte calcium nitrate is conducive to the decolorization reaction, while the presence of sodium phosphate is not conducive to the decolorization reaction. Illumination is also conducive to the decolorization reaction. Manganese ore can also be reused, and Table 1 shows the decolorization results of manganese ore when it is reused.

表一:     使用次数     1     2     3     X-3B反应后浓度(mg/l)     0.21     0.36     0.45     脱色率(%)     98.94     98.19     97.75 Table I: usage count 1 2 3 Concentration of X-3B after reaction (mg/l) 0.21 0.36 0.45 Decolorization rate (%) 98.94 98.19 97.75

二、锰钾矿对其余九种染料的脱色效果2. The decolorization effect of manganese potassium ore on the remaining nine dyes

pH=2.5,160-200目锰钾矿用量0.5g,废水用量50ml,染料浓度20ppm,振荡反应5小时,结果如表二所示:pH=2.5, 160-200 mesh manganese potassium ore dosage 0.5g, waste water dosage 50ml, dye concentration 20ppm, shaking reaction for 5 hours, the results are shown in Table 2:

表二: 染料 K-2BP  X-BR  X-R  K-BR  K-GN  X-8B  K-G  X-GN  M-3RE 脱色率(%) 93.15  98.94  84.14  89.11  100.00  99.46  100.0  97.54  99.02 Table II: dye K-2BP X-BR XR K-BR K-GN X-8B KG X-GN M-3RE Decolorization rate (%) 93.15 98.94 84.14 89.11 100.00 99.46 100.0 97.54 99.02

本发明的优点和积极效果:本发明的脱色方法所采用的脱色剂天然锰钾矿原料易得,成本低,无二次污染,应用范围广泛,脱色效果明显。在我国南方沿北纬23°带东西长1500km、南北宽220km、氧化深度50-60m范围分布着十分丰富的氧化锰矿资源。另外,天然锰钾矿处理印染废水后,还可以重复使用。Advantages and positive effects of the present invention: the decolorizing agent used in the decolorizing method of the present invention is easy to obtain natural manganese-potassium ore raw materials, has low cost, no secondary pollution, wide application range, and obvious decolorizing effect. In the south of my country, there are very rich manganese oxide ore resources distributed along the north latitude 23° belt, which is 1500km long from east to west, 220km wide from north to south, and has an oxidation depth of 50-60m. In addition, natural manganese and potassium ore can be reused after treating printing and dyeing wastewater.

附图说明:Description of drawings:

图1废水的pH值与X-3B脱色率的关系图。Figure 1 The relationship between the pH value of wastewater and the decolorization rate of X-3B.

具体实施方式:Detailed ways:

初始浓度为20mg/l的X-3B(天津新欣染料厂生产的工业常用染料)印染废水50ml,盛放于100ml锥形瓶,将其pH值用HNO3和NaOH调节至3。天然锰钾矿采自湘潭锰矿,经自来水冲洗、自然干燥、破碎、筛分得到160-200目的锰钾矿,用量为0.2g。将锥形瓶放入水浴恒温振荡器内,在25℃条件下,200r/min振荡半小时,对X-3B的脱色率几乎达到100%。50ml of printing and dyeing wastewater of X-3B (a common industrial dye produced by Tianjin Xinxin Dye Factory) with an initial concentration of 20mg/l was placed in a 100ml Erlenmeyer flask, and its pH value was adjusted to 3 with HNO3 and NaOH. The natural manganese and potassium ore is collected from Xiangtan manganese ore, washed with tap water, naturally dried, crushed and sieved to obtain 160-200 mesh manganese and potassium ore, and the dosage is 0.2g. Put the Erlenmeyer flask into a constant temperature shaker in a water bath, shake at 200r/min for half an hour at 25°C, and the decolorization rate of X-3B is almost 100%.

Claims (9)

1. decolorization of dyeing method may further comprise the steps in order:
(1) regulates the pH value of waste water to being acid;
(2) add natural cryptomelane, the stirring reaction several hrs gets final product.
2. decoloring method as claimed in claim 1, the pH value that it is characterized in that described waste water is below 4.
3. decoloring method as claimed in claim 1 or 2, the particle diameter that it is characterized in that described natural cryptomelane is the 160-200 order.
4. decoloring method as claimed in claim 1 or 2 is characterized in that also adding ionogen nitrocalcite in waste water.
5. decoloring method as claimed in claim 3 is characterized in that also adding ionogen nitrocalcite in waste water.
6. decoloring method as claimed in claim 1 or 2 is characterized in that decolouring and carries out under illumination condition.
7. decoloring method as claimed in claim 3 is characterized in that decolouring and carries out under illumination condition.
8. decoloring method as claimed in claim 4 is characterized in that decolouring and carries out under illumination condition.
9. decoloring method as claimed in claim 5 is characterized in that decolouring and carries out under illumination condition.
CN 03100824 2003-01-23 2003-01-23 Decolouring method of printing and dyeing waste water Expired - Fee Related CN1214995C (en)

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WO2010101867A1 (en) * 2009-03-03 2010-09-10 Danisco Us Inc. Oxidative decolorization of dyes with enzymatically generated peracid - method, composition and kit of parts
CN101781012B (en) * 2009-12-31 2011-08-17 陕西师范大学 Chloroperoxidase Catalyzed H2O2 Oxidation Method for Decolorization and Degradation of Water-Soluble Azo Dyes
CN107698693B (en) * 2017-11-17 2020-02-18 湖南农业大学 A kind of fruit polysaccharide decolorization method
CN118002066A (en) * 2024-03-07 2024-05-10 重庆化工职业学院 Application of natural manganese mineral powder in adsorption of methylene blue

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