CN100467397C - A kind of waste water treatment agent and preparation method thereof - Google Patents
A kind of waste water treatment agent and preparation method thereof Download PDFInfo
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- CN100467397C CN100467397C CNB2006100204786A CN200610020478A CN100467397C CN 100467397 C CN100467397 C CN 100467397C CN B2006100204786 A CNB2006100204786 A CN B2006100204786A CN 200610020478 A CN200610020478 A CN 200610020478A CN 100467397 C CN100467397 C CN 100467397C
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- 238000002360 preparation method Methods 0.000 title claims description 15
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- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 17
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- 239000004332 silver Substances 0.000 claims description 17
- 229910000278 bentonite Inorganic materials 0.000 claims description 11
- 239000000440 bentonite Substances 0.000 claims description 11
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 11
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- 238000012546 transfer Methods 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
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- 239000000047 product Substances 0.000 description 5
- 238000001179 sorption measurement Methods 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
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- 238000005553 drilling Methods 0.000 description 4
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- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000004043 dyeing Methods 0.000 description 3
- 238000005189 flocculation Methods 0.000 description 3
- 230000016615 flocculation Effects 0.000 description 3
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- -1 silver nitrate etc.) Chemical compound 0.000 description 3
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- 238000003911 water pollution Methods 0.000 description 3
- 241000083869 Polyommatus dorylas Species 0.000 description 2
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 2
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- 239000000463 material Substances 0.000 description 2
- STZCRXQWRGQSJD-GEEYTBSJSA-M methyl orange Chemical compound [Na+].C1=CC(N(C)C)=CC=C1\N=N\C1=CC=C(S([O-])(=O)=O)C=C1 STZCRXQWRGQSJD-GEEYTBSJSA-M 0.000 description 2
- 229940012189 methyl orange Drugs 0.000 description 2
- CXKWCBBOMKCUKX-UHFFFAOYSA-M methylene blue Chemical compound [Cl-].C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 CXKWCBBOMKCUKX-UHFFFAOYSA-M 0.000 description 2
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- OLSOUGWNONTDCK-UHFFFAOYSA-J tetrasodium 5-amino-3-[[4-[4-[(8-amino-1-hydroxy-3,6-disulfonatonaphthalen-2-yl)diazenyl]-3-methoxyphenyl]-2-methoxyphenyl]diazenyl]-4-hydroxynaphthalene-2,7-disulfonate Chemical compound [Na+].[Na+].[Na+].[Na+].C1=C(S([O-])(=O)=O)C=C2C=C(S([O-])(=O)=O)C(N=NC3=CC=C(C=C3OC)C=3C=C(C(=CC=3)N=NC=3C(=CC4=CC(=CC(N)=C4C=3O)S([O-])(=O)=O)S([O-])(=O)=O)OC)=C(O)C2=C1N OLSOUGWNONTDCK-UHFFFAOYSA-J 0.000 description 2
- YXZRCLVVNRLPTP-UHFFFAOYSA-J turquoise blue Chemical compound [Na+].[Na+].[Na+].[Na+].[Cu+2].NC1=NC(Cl)=NC(NC=2C=C(NS(=O)(=O)C3=CC=4C(=C5NC=4NC=4[N-]C(=C6C=CC(=CC6=4)S([O-])(=O)=O)NC=4NC(=C6C=C(C=CC6=4)S([O-])(=O)=O)NC=4[N-]C(=C6C=CC(=CC6=4)S([O-])(=O)=O)N5)C=C3)C(=CC=2)S([O-])(=O)=O)=N1 YXZRCLVVNRLPTP-UHFFFAOYSA-J 0.000 description 2
- FOGYNLXERPKEGN-UHFFFAOYSA-N 3-(2-hydroxy-3-methoxyphenyl)-2-[2-methoxy-4-(3-sulfopropyl)phenoxy]propane-1-sulfonic acid Chemical class COC1=CC=CC(CC(CS(O)(=O)=O)OC=2C(=CC(CCCS(O)(=O)=O)=CC=2)OC)=C1O FOGYNLXERPKEGN-UHFFFAOYSA-N 0.000 description 1
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- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 1
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Landscapes
- Water Treatment By Sorption (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
本发明涉及一种废水处理剂及其制备方法,该处理剂各组分及其质量比为改性膨润土∶三氧化二铝∶银=100∶11~30∶0.2~0.8,该废水处理剂的制备方法为:(1)按膨润土∶细炭粉=100∶3~7的质量比称量,用焙烧法制备改性膨润土;(2)按改性膨润土∶铝=100∶3~8的质量比称取铝盐,将改性膨润土浸入铝盐水溶液中,并通过化学反应和高温焙烧使铝盐转化为三氧化二铝;(3)按改性膨润土∶银=100∶0.2~0.8的质量比称取银盐,将上步产物浸入银盐水溶液中,烘干后高温焙烧。该处理剂对废水中的有机污染物、悬浮物具有良好的吸附、絮凝和催化降解作用,适用于多种有机污染废水的处理,水处理成本低,且易于回收再用。The invention relates to a waste water treatment agent and a preparation method thereof. The components of the treatment agent and their mass ratios are modified bentonite: aluminum oxide: silver = 100: 11-30: 0.2-0.8, the waste water treatment agent The preparation method is: (1) weighing according to the mass ratio of bentonite: fine carbon powder = 100: 3-7, and preparing modified bentonite by roasting method; (2) weighing according to the mass ratio of modified bentonite: aluminum = 100: 3-8 The aluminum salt is weighed, the modified bentonite is immersed in the aluminum salt aqueous solution, and the aluminum salt is converted into aluminum oxide by chemical reaction and high-temperature roasting; (3) according to the quality of modified bentonite: silver=100:0.2~0.8 Weigh the silver salt, immerse the product of the previous step in the silver salt aqueous solution, dry it and roast it at high temperature. The treatment agent has good adsorption, flocculation and catalytic degradation effects on organic pollutants and suspended matter in wastewater, is suitable for the treatment of various organic polluted wastewater, has low water treatment cost, and is easy to recycle and reuse.
Description
技术领域 technical field
本发明涉及一种废水处理剂及其制备方法。The invention relates to a waste water treatment agent and a preparation method thereof.
背景技术 Background technique
日益突出的水污染破坏了生态环境,危害了动植物的生存,影响了人们的健康,制约了工农业生产的发展,已引起了全社会的广泛关注。研制和使用新的高效、低毒、价廉的废水处理剂,已成为解决水污染问题的关键之一,其重要性是显而易见的。为此国内外均进行了大量的研究,提出了一系列新的水处理剂及其制备方法。中国专利CN1046315公开了“膨润土复合净水剂(一型)的制备方法”,CN1055528公开了“复合高效钻井泥浆废水处理剂”,CN1081160公开了“高效吸附水处理”,CN1222603公开了“印染污水脱色和净化的方法及其制剂”,CN1257839公开了“一种氧化絮凝固液分离的水净化方法”,CN1319564公开了“一种天然复合型水处理剂,”CN1341568公开了“改性木素磺酸盐多功能水处理剂及其制备方法”,CN135627公开了“一种天然膨润土污水处理材料的制备方法”,CN1428301公开了“一种水处理剂”,CN1535925公开了“高铁酸盐多功能水处理剂的制备及除污染技术”,CN1539756公开了“一种用锌、钼、镁盐类做水处理剂的方法”,CN1559930公开了“水处理剂的制备及其应用”,CN156966公开了“一种无机—有机复合膨润土废水处材料的制备方法”等等。这些专利技术各有其特点和应用方向。但是,由于水污染的复杂性和多变性,现有的水处理剂还远远不能满足环境保护的需要。The increasingly prominent water pollution has destroyed the ecological environment, endangered the survival of animals and plants, affected people's health, and restricted the development of industrial and agricultural production, which has aroused widespread concern from the whole society. The development and use of new high-efficiency, low-toxicity, and cheap wastewater treatment agents has become one of the keys to solving water pollution problems, and its importance is obvious. For this reason, a large number of researches have been carried out at home and abroad, and a series of new water treatment agents and their preparation methods have been proposed. Chinese patent CN1046315 discloses "preparation method of bentonite composite water purifying agent (type I)", CN1055528 discloses "composite high-efficiency drilling mud wastewater treatment agent", CN1081160 discloses "high-efficiency adsorption water treatment", and CN1222603 discloses "printing and dyeing sewage decolorization and purification method and preparation thereof", CN1257839 discloses "a water purification method for oxidative flocculation solid-liquid separation", CN1319564 discloses "a natural composite water treatment agent", and CN1341568 discloses "modified lignosulfonic acid Salt multifunctional water treatment agent and preparation method thereof”, CN135627 discloses “a preparation method of natural bentonite sewage treatment material”, CN1428301 discloses “a kind of water treatment agent”, CN1535925 discloses “ferrate multifunctional water treatment Preparation of water treatment agent and decontamination technology", CN1539756 discloses "a method of using zinc, molybdenum and magnesium salts as water treatment agent", CN1559930 discloses "preparation and application of water treatment agent", CN156966 discloses "a A preparation method of an inorganic-organic composite bentonite wastewater treatment material" and so on. Each of these patented technologies has its own characteristics and application directions. However, due to the complexity and variability of water pollution, the existing water treatment agents are far from meeting the needs of environmental protection.
发明内容 Contents of the invention
本发明的目的在于提供一种废水处理剂及其制备方法,该处理剂对印染废水、油气田废水和其他有机污染废水中的污染物有较好的吸附、絮凝和催化降解作用,从而产生明显的处理效果,并且其制备方法简单,水处理成本低,易于回收再用。The object of the present invention is to provide a kind of waste water treatment agent and preparation method thereof, and this treatment agent has better adsorption, flocculation and catalytic degradation to the pollutant in printing and dyeing waste water, oil and gas field waste water and other organic polluted waste water, thereby produces obvious The treatment effect is simple, the preparation method is simple, the water treatment cost is low, and it is easy to recycle and reuse.
本发明利用加炭焙烧法对膨润土改性,使其具有较大的孔隙率和表面积,从而增强其吸附能力。然后通过化学反应和高温焙烧,在改性膨润土表面负载高吸附性高催化活性的三氧化二铝和金属银微粒,制备成一种废水处理剂。In the invention, the bentonite is modified by a charcoal-added roasting method to make it have larger porosity and surface area, thereby enhancing its adsorption capacity. Then, through chemical reaction and high-temperature roasting, the surface of the modified bentonite is loaded with aluminum oxide and metal silver particles with high adsorption capacity and high catalytic activity to prepare a waste water treatment agent.
一种废水处理剂,由改性膨润土、三氧化二铝、银组成,各组分的质量比为:A kind of waste water treatment agent, is made up of modified bentonite, aluminum oxide, silver, and the mass ratio of each component is:
改性膨润土 100Modified bentonite 100
三氧化二铝 11~30Aluminum oxide 11~30
银 0.2~0.8Silver 0.2~0.8
一种废水处理剂的制备方法,依次包括以下步骤:A preparation method for wastewater treatment agent, comprising the following steps in turn:
(1)按膨润土:细炭粉=100:3~7的质量比称量,将二者充分研磨混匀,在温度为550~600℃的马弗炉内焙烧2~3小时,得改性膨润土;(1) Weigh according to the mass ratio of bentonite: fine carbon powder = 100:3-7, fully grind and mix the two, and roast in a muffle furnace at a temperature of 550-600°C for 2-3 hours to obtain modified Bentonite;
(2)按改性膨润土:铝=100:3~8的质量比,称取上述改性膨润土和铝盐,先配制浓度为10%~30%的铝盐水溶液,再将上述改性膨润土倒入其中,摇匀后静置1~2小时,在搅拌下滴加NH3·H2O,调节pH值为10左右,在100℃下烘干,再逐渐升温至400~500℃保温焙烧1~2小时;(2) According to the mass ratio of modified bentonite: aluminum=100:3~8, weigh the above-mentioned modified bentonite and aluminum salt, first prepare an aqueous solution of aluminum salt with a concentration of 10%~30%, then pour the above-mentioned modified bentonite Put it into it, shake it up and let it stand for 1-2 hours, add NH 3 ·H 2 O dropwise under stirring, adjust the pH value to about 10, dry it at 100°C, and then gradually raise the temperature to 400-500°C and heat-preserve and roast for 1 ~2 hours;
(3)按改性膨润土:银=100:0.2~0.8的质量比称取银盐,先配制浓度为1%~2.5%的银盐水溶液,再将上步焙烧产物浸入其中,在90℃下烘干,然后转入马弗炉内升温至450~500℃,保温2小时,使银盐转化为银,即得本发明一种废水处理剂。(3) Weigh the silver salt according to the mass ratio of modified bentonite: silver=100:0.2~0.8, first prepare a silver salt aqueous solution with a concentration of 1%~2.5%, and then immerse the roasted product of the previous step in it. drying, and then transfer to a muffle furnace to raise the temperature to 450-500° C., and keep it warm for 2 hours, so that the silver salt is converted into silver, and a waste water treatment agent of the present invention is obtained.
本发明废水处理剂的制备方法中,第(1)步按膨润土:细炭粉=100:3~7的质量比称量,将二者充分研磨混匀,调水制成细小颗粒,烘干后转入温度为550~600℃的马弗炉内焙烧2~3小时,得改性膨润土;第(2)步按改性膨润土:铝=100:3~8的质量比,称取改性膨润土和铝盐(如硫酸铝、三氯化铝等),先配制浓度为10%~30%的铝盐水溶液,再将改性膨润土倒入其中,摇匀,静置1~2小时,然后在搅拌下滴加NH3·H2O,调节pH值为10左右,使铝盐转化为氢氧化铝,于100℃下烘干,再逐渐升温至400~500℃保温焙烧1~2小时,使氢氧化铝转化为三氧化二铝,所得焙烧产物中二组分的质量比为改性膨润土:三氧化二铝=100:11~30;第(3)步按改性膨润土:银=100:0.2~0.8的质量比称取银盐(如硝酸银等),先配制成浓度为1%~2.5%的银盐水溶液,再将上步焙烧产物浸入其中,在90℃下烘干,然后转入马弗炉内升温至450~500℃,保温2小时,使银盐转化为银,即制得本发明一种废水处理剂,其中各组分的质量比为改性膨润土:三氧化二铝:银=100:11~30:0.2~0.8。In the preparation method of the wastewater treatment agent of the present invention, the (1) step is weighed according to the mass ratio of bentonite: fine carbon powder=100:3~7, the two are fully ground and mixed, and the water is adjusted to make fine particles, and dried Then transfer to a muffle furnace with a temperature of 550-600°C and roast for 2-3 hours to obtain modified bentonite; in the second step, the modified bentonite: aluminum = 100:3-8 mass ratio, weigh the modified bentonite Bentonite and aluminum salts (such as aluminum sulfate, aluminum trichloride, etc.), first prepare an aluminum salt solution with a concentration of 10% to 30%, then pour the modified bentonite into it, shake well, and let it stand for 1 to 2 hours, then Add NH 3 ·H 2 O dropwise under stirring, adjust the pH value to about 10, convert the aluminum salt into aluminum hydroxide, dry it at 100°C, then gradually raise the temperature to 400-500°C and heat-preserve for 1-2 hours. Aluminum hydroxide is converted into aluminum oxide, and the mass ratio of the two components in the resulting calcined product is modified bentonite: aluminum oxide=100:11~30; step (3) presses modified bentonite: silver=100 : The mass ratio of 0.2~0.8 takes by weighing silver salt (such as silver nitrate etc.), is first prepared into the silver salt aqueous solution that concentration is 1%~2.5%, then immerses the roasting product of last step wherein, dries at 90 ℃, then Put it into a muffle furnace and heat up to 450-500°C, keep it warm for 2 hours, and convert the silver salt into silver, and then a kind of waste water treatment agent of the present invention is obtained, wherein the mass ratio of each component is modified bentonite:dioxide trioxide Aluminum: silver = 100: 11-30: 0.2-0.8.
本发明一种废水处理剂可用于印染废水、油气田废水、生活污水以及其他多种有机污染废水的处理。The waste water treatment agent of the invention can be used for the treatment of printing and dyeing waste water, oil and gas field waste water, domestic sewage and other various organic polluted waste water.
与现有技术相比,本发明具有以下优点:(1)对废水中的有机污染物、悬浮物具有良好的吸附、絮凝和催化降解作用;(2)处理废水工艺简单,用量少,沉降速度较快,效果较好;(3)水处理成本低;(4)易于回收再用。Compared with the prior art, the present invention has the following advantages: (1) It has good adsorption, flocculation and catalytic degradation effects on organic pollutants and suspended solids in wastewater; The speed is faster and the effect is better; (3) the cost of water treatment is low; (4) it is easy to recycle and reuse.
具体实施方式 Detailed ways
下面根据实施例具体说明本发明。The present invention will be specifically described below based on examples.
实施例1Example 1
按下述步骤制备本发明废水处理剂:Prepare wastewater treatment agent of the present invention according to the following steps:
(1)按膨润土:细炭粉=100:4的质量比,称取膨润土和细炭粉,将二者充分研磨混匀,调水制成细小颗粒,在100℃下烘干,转入温度为550℃的马弗炉内焙烧2小时,得改性膨润土;(1) According to the mass ratio of bentonite: fine charcoal powder = 100:4, weigh bentonite and fine charcoal powder, fully grind and mix the two, adjust water to make fine particles, dry at 100°C, and transfer to temperature Roasting in a muffle furnace at 550°C for 2 hours to obtain modified bentonite;
(2)按改性膨润土:铝=100:6.6的质量比,称取上述改性膨润土和硫酸铝,配制成浓度为20%的铝盐水溶液,将上述改性膨润土倒入其中,摇匀,静置2小时,然后在搅拌下滴加NH3·H2O,调节pH值为10左右,使铝盐转化为氢氧化铝,于100℃下烘干,再逐渐升温至450℃保温焙烧1小时,使氢氧化铝转化为三氧化二铝,所得焙烧产物中二组分的质量比为改性膨润土:三氧化二铝=100:25;(2) According to the mass ratio of modified bentonite: aluminum=100:6.6, take the above-mentioned modified bentonite and aluminum sulfate, and prepare the aluminum salt solution with a concentration of 20%, pour the above-mentioned modified bentonite into it, shake well, Stand still for 2 hours, then add NH 3 ·H 2 O dropwise under stirring, adjust the pH value to about 10, convert the aluminum salt into aluminum hydroxide, dry at 100°C, and then gradually heat up to 450°C for 1 hour, aluminum hydroxide is converted into aluminum oxide, and the mass ratio of the two components in the resulting roasted product is modified bentonite: aluminum oxide=100:25;
(3)按改性膨润土:银=100:0.5的质量比称取硝酸银,配制成浓度为1.5%的银盐水溶液,将上步焙烧产物浸入其中,在90℃下烘干,然后转入马弗炉内升温至500℃,保温2小时,使银盐转化为银,即制得废水处理剂(A),其各组分的质量比为改性膨润土:三氧化二铝:银=100:25:0.5。(3) Take silver nitrate according to the mass ratio of modified bentonite: silver=100:0.5, and prepare it into a silver salt aqueous solution with a concentration of 1.5%, immerse the roasted product in the previous step, dry it at 90°C, and then transfer it to In the muffle furnace, the temperature is raised to 500° C. and kept for 2 hours, so that the silver salt is converted into silver, and the waste water treatment agent (A) is obtained, and the mass ratio of its components is modified bentonite: aluminum oxide: silver=100 :25:0.5.
取浓度为250mg.L-1的工业染料直接毛蓝和直接桃红12B水溶液100mL,分别置于两个250mL烧杯中,投加一定量的上述废水处理剂(A),搅拌5~10分钟,静置4小时或高速离心分离,取上层清液在分光光度计上测定其吸光度,计算脱色率;用密封管法测定其CODCr,计算COD去除率,结果如表1所示。Take 100mL of industrial dyes direct wool blue and direct pink 12B aqueous solutions with a concentration of 250mg.L -1 , put them in two 250mL beakers respectively, add a certain amount of the above-mentioned wastewater treatment agent (A), stir for 5-10 minutes, and let Place it for 4 hours or centrifuge at high speed, take the supernatant and measure its absorbance on a spectrophotometer to calculate the decolorization rate; measure its COD Cr by the sealed tube method and calculate the COD removal rate, the results are shown in Table 1.
表1Table 1
取难以脱色的指示剂甲基橙和亚甲基蓝水溶液100mL,分别置于250mL烧杯中,各投加一定量的上述废水处理剂(A),搅拌5~10分钟,静置4小时或高速离心分离,取上层清液测定其脱色率,结果见表2。Take 100mL aqueous solution of methyl orange and methylene blue, indicators that are difficult to decolorize, put them in 250mL beakers respectively, add a certain amount of the above-mentioned wastewater treatment agent (A), stir for 5-10 minutes, let stand for 4 hours or centrifuge at a high speed, The supernatant was taken to measure its decolorization rate, and the results are shown in Table 2.
表2Table 2
实施例2Example 2
按膨润土:细炭粉=100:5的质量比,依照上述实施例1(1)的方法和步骤进行操作,制得改性膨润土颗粒;按改性膨润土:铝=100:4的质量比,依照上述实施例1(2)的方法和步骤进行操作;按改性膨润土:银=100:0.75的质量比,依照上述实施例1(3)的方法和步骤进行操作,即制得废水处理剂(B),其各组分的质量比为改性膨润土:三氧化二铝:银=100:15:0.75。Press bentonite: the mass ratio of fine carbon powder=100:5, operate according to the method and the step of above-mentioned embodiment 1 (1), make modified bentonite particle; Press modified bentonite: the mass ratio of aluminum=100:4, Operate according to the method and steps of above-mentioned embodiment 1 (2); operate according to the method and steps of above-mentioned embodiment 1 (3) according to the mass ratio of modified bentonite: silver=100:0.75, promptly make wastewater treatment agent (B), the mass ratio of each component is modified bentonite: aluminum oxide: silver=100:15:0.75.
取浓度为500mg.L-1的工业染料直接耐晒翠蓝、直接耐酸大红、直接深蓝、直接天蓝、直接深烟、直接耐酸枣红等水溶液各100mL,分别置于6个烧杯中,投加一定量的废水处理剂(B),搅拌5~10分钟,静置4小时或高速离心分离,取上层清液测定脱色率和COD去除率,结果见表3。Take 100mL of industrial dyes with a concentration of 500mg.L -1 , such as direct sun-fast turquoise blue, direct acid-resistant bright red, direct dark blue, direct sky blue, direct dark smoke, direct acid-resistant bordeaux, etc., and put them in 6 beakers respectively. Amount of wastewater treatment agent (B), stirred for 5 to 10 minutes, left to stand for 4 hours or high-speed centrifuged, took the supernatant to measure the decolorization rate and COD removal rate, the results are shown in Table 3.
表3table 3
分别取两种成分复杂、色度高、COD高的钻井废水100mL,各加入少量高分子絮凝剂,搅拌3分钟,静置10分钟,然后再加入0.50g废水处理剂(B),搅拌5分钟,静置4小时或高速离心分离,取上层清液测定其COD去除率。结果见表4。Take 100mL of two kinds of drilling wastewater with complex components, high chroma and high COD, respectively, add a small amount of polymer flocculant, stir for 3 minutes, let stand for 10 minutes, then add 0.50g of wastewater treatment agent (B), and stir for 5 minutes , stand for 4 hours or high-speed centrifugation, take the supernatant to measure its COD removal rate. The results are shown in Table 4.
表4Table 4
取0.5g废水处理剂(B)处理浓度为250mg.L-1的直接桃红12B染料溶液,将分离出的沉淀物放入马弗炉内,于500℃保温1小时,冷却后即得回收废水处理剂。使用该回收废水处理剂重复处理上述染料溶液,回收次数与脱色率的关系如表5。Take 0.5g of wastewater treatment agent (B) to treat the direct pink 12B dye solution with a concentration of 250mg.L -1 , put the separated precipitate into a muffle furnace, keep it warm at 500°C for 1 hour, and obtain recovered wastewater after cooling treatment agent. The above-mentioned dye solution was repeatedly treated with the recovered wastewater treatment agent, and the relationship between the number of recovery times and the decolorization rate is shown in Table 5.
表5table 5
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