CN104209094A - Preparation method of sepiolite heavy metal absorbent modified with amino acid carboxylic acid - Google Patents
Preparation method of sepiolite heavy metal absorbent modified with amino acid carboxylic acid Download PDFInfo
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- 239000004113 Sepiolite Substances 0.000 title claims abstract description 56
- 229910052624 sepiolite Inorganic materials 0.000 title claims abstract description 56
- 235000019355 sepiolite Nutrition 0.000 title claims abstract description 55
- 229910001385 heavy metal Inorganic materials 0.000 title claims abstract description 14
- 238000002360 preparation method Methods 0.000 title claims description 8
- -1 amino acid carboxylic acid Chemical group 0.000 title claims description 4
- 230000002745 absorbent Effects 0.000 title 1
- 239000002250 absorbent Substances 0.000 title 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000012266 salt solution Substances 0.000 claims abstract description 16
- 238000003756 stirring Methods 0.000 claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- KXDHJXZQYSOELW-UHFFFAOYSA-N Carbamic acid Chemical compound NC(O)=O KXDHJXZQYSOELW-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000012065 filter cake Substances 0.000 claims abstract description 12
- 239000008367 deionised water Substances 0.000 claims abstract description 11
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 11
- 239000000725 suspension Substances 0.000 claims abstract description 11
- FRGBDYDAIWEXJX-UHFFFAOYSA-K trisodium;2-[2-[bis(carboxylatomethyl)amino]ethyl-(3-trimethoxysilylpropyl)amino]acetate Chemical compound [Na+].[Na+].[Na+].CO[Si](OC)(OC)CCCN(CC([O-])=O)CCN(CC([O-])=O)CC([O-])=O FRGBDYDAIWEXJX-UHFFFAOYSA-K 0.000 claims abstract description 9
- 239000003463 adsorbent Substances 0.000 claims abstract description 5
- 238000012546 transfer Methods 0.000 claims description 9
- 239000000243 solution Substances 0.000 claims description 8
- 239000000843 powder Substances 0.000 claims description 4
- PHQOGHDTIVQXHL-UHFFFAOYSA-N n'-(3-trimethoxysilylpropyl)ethane-1,2-diamine Chemical compound CO[Si](OC)(OC)CCCNCCN PHQOGHDTIVQXHL-UHFFFAOYSA-N 0.000 claims description 2
- 239000013535 sea water Substances 0.000 claims description 2
- XWNXEWLCHSLQOI-UHFFFAOYSA-K trisodium;triacetate Chemical compound [Na+].[Na+].[Na+].CC([O-])=O.CC([O-])=O.CC([O-])=O XWNXEWLCHSLQOI-UHFFFAOYSA-K 0.000 claims description 2
- OUDSFQBUEBFSPS-UHFFFAOYSA-N ethylenediaminetriacetic acid Chemical compound OC(=O)CNCCN(CC(O)=O)CC(O)=O OUDSFQBUEBFSPS-UHFFFAOYSA-N 0.000 claims 1
- 239000008262 pumice Substances 0.000 claims 1
- HRXKRNGNAMMEHJ-UHFFFAOYSA-K trisodium citrate Chemical compound [Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O HRXKRNGNAMMEHJ-UHFFFAOYSA-K 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 9
- 230000008569 process Effects 0.000 abstract description 4
- 238000000227 grinding Methods 0.000 abstract description 3
- 238000001035 drying Methods 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 238000001179 sorption measurement Methods 0.000 description 18
- 239000010949 copper Substances 0.000 description 11
- 239000000463 material Substances 0.000 description 7
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 5
- 229910052802 copper Inorganic materials 0.000 description 5
- 229910052793 cadmium Inorganic materials 0.000 description 4
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000011161 development Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000012224 working solution Substances 0.000 description 4
- 159000000000 sodium salts Chemical class 0.000 description 3
- 239000002689 soil Substances 0.000 description 3
- UUEWCQRISZBELL-UHFFFAOYSA-N 3-trimethoxysilylpropane-1-thiol Chemical compound CO[Si](OC)(OC)CCCS UUEWCQRISZBELL-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000009388 chemical precipitation Methods 0.000 description 2
- 229960000935 dehydrated alcohol Drugs 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000010668 complexation reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000009775 high-speed stirring Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000013500 performance material Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
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- 150000003839 salts Chemical class 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052604 silicate mineral Inorganic materials 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
本发明提供了一种胺基羧酸修饰海泡石重金属吸附剂的制备方法,属于环保技术领域。按照海泡石∶去离子水∶无水乙醇=2.5~5∶40~70∶35~55(w/v/v/)的比例制备海泡石悬浊液,并搅拌形成凝胶;在7000~10000rpm搅拌条件下加入质量浓度为10~20%的N-(三甲氧基甲硅烷基丙基)乙二胺三乙酸三钠盐溶液,其与海泡石的比例为4.5~9:2~3(v/w);加入无水乙醇,继续搅拌形成凝胶体系后,用无水乙醇抽滤并收集凝胶滤饼;将滤饼置于烘箱中恒温70~80℃,持续18h后烘干,研磨后即得到胺基羧酸修饰海泡石。本发明工艺简单、成本低、适用范围广、无二次污染。The invention provides a method for preparing an aminocarboxylic acid-modified sepiolite heavy metal adsorbent, which belongs to the technical field of environmental protection. Prepare sepiolite suspension according to the ratio of sepiolite: deionized water: absolute ethanol = 2.5~5:40~70:35~55 (w/v/v/), and stir to form a gel; at 7000 Add the N-(trimethoxysilylpropyl) ethylenediaminetriacetic acid trisodium salt solution with a mass concentration of 10-20% under the stirring condition of ~10000rpm, and the ratio of it to sepiolite is 4.5~9:2~ 3 (v/w); Add absolute ethanol, continue to stir to form a gel system, then use absolute ethanol to filter and collect the gel filter cake; place the filter cake in an oven at a constant temperature of 70-80°C for 18 hours and then bake After drying, the aminocarboxylic acid modified sepiolite can be obtained after grinding. The invention has simple process, low cost, wide application range and no secondary pollution.
Description
技术领域technical field
本发明涉及重金属吸附材料的制备技术,特别是一种胺基羧酸修饰海泡石重金属吸附剂的制备方法,属于环保技术领域。The invention relates to a preparation technology of a heavy metal adsorption material, in particular to a preparation method of an aminocarboxylic acid-modified sepiolite heavy metal adsorbent, which belongs to the technical field of environmental protection.
背景技术Background technique
工业作为我国经济的重要支撑,高速发展的同时带来了日益严重的环境污染问题,尤其是随着频繁的开矿、金属冶炼以及加工,大量含铅、汞、镉、钴、铜等废气、废水和固体废物排放到环境中,造成严重危害。据不完全统计,目前全世界平均每年排放汞约1.5万吨,铜约340万吨,铅约500万吨,锰约1500万吨,镍约100万吨等,排放的废弃物使很多区域的土壤重金属浓度明显高于背景值。重金属污染会不仅会严重影响和改变水体、土壤等的生态功能,还会导致农作物产量和品质的下降,重金属在食物链中的过量富集会对自然环境和人体健康造成很大的危害,影响社会经济可持续发展。As an important support for my country's economy, industry has brought about increasingly serious environmental pollution problems with its rapid development, especially with frequent mining, metal smelting and processing, a large amount of waste gas and waste water containing lead, mercury, cadmium, cobalt, copper, etc. and solid waste discharged into the environment, causing serious harm. According to incomplete statistics, the world currently discharges an average of 15,000 tons of mercury, 3.4 million tons of copper, 5 million tons of lead, 15 million tons of manganese, and 1 million tons of nickel, etc. The concentration of heavy metals in the soil was significantly higher than the background value. Heavy metal pollution will not only seriously affect and change the ecological functions of water bodies and soils, but also lead to a decline in crop yield and quality. Excessive accumulation of heavy metals in the food chain will cause great harm to the natural environment and human health, affecting society. sustainable economic development.
目前,人们利用多种方法,如:化学沉淀法、吸附法、气浮法、氧化还原法等,处理废水中的重金属离子,其中,以化学沉淀法和吸附法应用最为广泛。At present, people use a variety of methods, such as: chemical precipitation, adsorption, air flotation, redox, etc., to treat heavy metal ions in wastewater, among which chemical precipitation and adsorption are the most widely used.
海泡石(Sepiolite)化学式为Mg8Si12O30(OH)4(OH2)4·8H2O,是一种2:1型链式层状结构的纤维状富镁硅酸盐矿物,通常呈白、浅灰、浅黄等颜色,不透明也没有光泽,硬度2~3,密度2~2.5g/cm3,具有收缩率低,可塑性好,比表面大,吸附性强以及热稳定等优点。我国是世界上少数几个富产海泡石的国家之一,在湖南、江西、河北均有广泛分布,但开发利用却十分落后,目前仍以出口原料为主。海泡石理论比表面积为900m2/g,接近活性炭,但价格仅为其十几分之一。近年来,通过表面修饰方法来提高材料性能,制备功能先进、性能突出的材料以及复合材料成为研究的热点。因此加强对海泡石的开发利用,特别是通过表面修饰来提高海泡石的吸附性能有极其重要的意义。The chemical formula of sepiolite is Mg 8 Si 12 O 30 (OH) 4 (OH 2 ) 4 8H 2 O, which is a fibrous magnesium-rich silicate mineral with a 2:1 chain layer structure. Usually white, light gray, light yellow and other colors, opaque and dull, hardness 2-3, density 2-2.5g/cm 3 , has the advantages of low shrinkage, good plasticity, large specific surface, strong adsorption and thermal stability, etc. . my country is one of the few countries rich in sepiolite in the world. It is widely distributed in Hunan, Jiangxi and Hebei, but its development and utilization are very backward, and the raw materials are still mainly exported. The theoretical specific surface area of sepiolite is 900m 2 /g, which is close to that of activated carbon, but its price is only one tenth of that. In recent years, improving material performance through surface modification methods, preparing materials with advanced functions and outstanding performance, and composite materials have become research hotspots. Therefore, it is extremely important to strengthen the development and utilization of sepiolite, especially to improve the adsorption performance of sepiolite through surface modification.
2000年,学者Mercier在甲苯溶液中利用3-巯丙基三甲氧基硅烷(3-mercapto-pro-pyltrimethoxysilane)对海泡石进行表面修饰,修饰后的材料对Pb2+和Cd2+的最大吸附量分别为0.31mmol/g和0.21mmol/g。但由于该反应是在有机溶液甲苯中进行,不可避免会造成一定的污染和危害。因此亟需开发一种快速、低成本、绿色环保的合成工艺对海泡石进行表面修饰以提高其吸附性能。In 2000, scholar Mercier used 3-mercapto-pro-pyltrimethoxysilane (3-mercapto-pro-pyltrimethoxysilane) to modify the surface of sepiolite in toluene solution, and the modified material had the maximum resistance to Pb 2+ and Cd 2+ The adsorption amounts were 0.31 mmol/g and 0.21 mmol/g, respectively. But because this reaction is carried out in the organic solution toluene, it will inevitably cause certain pollution and harm. Therefore, it is urgent to develop a fast, low-cost, green and environmentally friendly synthesis process to modify the surface of sepiolite to improve its adsorption performance.
发明内容Contents of the invention
本发明的目的是提供一种工艺简单、成本低、适用范围广、无二次污染的胺基羧酸修饰海泡石作为重金属吸附剂的制备方法。The purpose of the present invention is to provide a method for preparing aminocarboxylic acid-modified sepiolite as a heavy metal adsorbent with simple process, low cost, wide application range and no secondary pollution.
为实现上述目的,本发明提供了一种纳米织构化方法制备胺基羧酸海泡石,该胺基羧酸海泡石可作为重金属吸附剂,制备方法如下:In order to achieve the above object, the present invention provides a nano-textured method for preparing aminocarboxylate sepiolite, which can be used as a heavy metal adsorbent, and the preparation method is as follows:
(1)取海泡石粉末,分散于去离子水中,加入无水乙醇,形成海泡石悬浊液,其中,海泡石:去离子水:无水乙醇=2.5~5:40~70:35~55(w/v/v/);(1) Take sepiolite powder, disperse it in deionized water, add absolute ethanol to form sepiolite suspension, wherein, sepiolite: deionized water: absolute ethanol=2.5~5:40~70: 35~55(w/v/v/);
(2)制备质量浓度为10~20%的N-(三甲氧基甲硅烷基丙基)乙二胺三乙酸三钠盐溶液,备用;(2) preparing N-(trimethoxysilylpropyl) ethylenediaminetriacetic acid trisodium salt solution with a mass concentration of 10-20%, for subsequent use;
(3)将海泡石悬浊液在分散机上搅拌形成凝胶后,在7000~10000rpm搅拌条件下加入步骤(2)中制备好的N-(三甲氧基甲硅烷基丙基)乙二胺三乙酸三钠盐溶液,质量浓度为10~20%的N-(三甲氧基甲硅烷基丙基)乙二胺三乙酸三钠盐溶液与海泡石的比例为4.5~9:2~3(v/w);(3) Stir the sepiolite suspension on a disperser to form a gel, then add N-(trimethoxysilylpropyl)ethylenediamine prepared in step (2) under the stirring condition of 7000~10000rpm Trisodium triacetate solution, the ratio of N-(trimethoxysilylpropyl) ethylenediamine trisodium trisodium salt solution to sepiolite with a mass concentration of 10-20% is 4.5-9:2-3 (v/w);
(4)加入无水乙醇,继续搅拌形成胺基羧酸修饰海泡石凝胶体系,将该凝胶体系转移至布氏漏斗,用无水乙醇抽滤并收集凝胶滤饼;(4) Add absolute ethanol, continue stirring to form an aminocarboxylic acid modified sepiolite gel system, transfer the gel system to a Buchner funnel, suction filter with absolute ethanol and collect the gel filter cake;
(5)将上述凝胶滤饼转移至广口瓶,置于烘箱中恒温70~80℃,持续18h后将广口瓶中凝胶取出,烘干,研磨后即得到胺基羧酸修饰海泡石(TMS-EDTA-海泡石)。(5) Transfer the above-mentioned gel filter cake to a jar, place it in an oven at a constant temperature of 70-80°C, and after 18 hours, take out the gel in the jar, dry it, and grind it to obtain aminocarboxylic acid-modified seawater. Sepiolite (TMS-EDTA-Sepiolite).
本发明具有如下优点:The present invention has the following advantages:
(1)适用范围广:本发明制备的吸附材料主要用于含重金属离子的废水处理、水体的修复,以及重金属污染土壤的修复等,对于由铅、镉、铜等多种重金属元素引起的复合污染也有显著的效果。(1) Wide range of application: the adsorption material prepared by the present invention is mainly used for wastewater treatment containing heavy metal ions, water body restoration, and heavy metal-contaminated soil restoration, etc. Pollution also has a significant effect.
(2)吸附效果好:本发明制备的重金属吸附分离材料胺基羧酸修饰海泡石,含有大量的活性功能基团,可通过化学吸附等表面络合反应吸附重金属,经试验证明胺基羧酸修饰海泡石对铅(Pb)、镉(Cd)和铜(Cu)均具有较好的吸附效果。(2) Good adsorption effect: The heavy metal adsorption and separation material prepared by the present invention is aminocarboxylic acid modified sepiolite, which contains a large number of active functional groups, and can adsorb heavy metals through surface complexation reactions such as chemical adsorption. Acid-modified sepiolite has good adsorption effect on lead (Pb), cadmium (Cd) and copper (Cu).
(3)用量少、易推广:本发明的材料在投加量较少的情况下即可取得较好的效果,成本较低,不会产生二次污染,易被社会接受,同时使用方法简单,可以大规模推广应用。(3) less dosage, easy to popularize: the material of the present invention can achieve better results when the dosage is less, the cost is low, no secondary pollution will occur, and it is easily accepted by the society. It is simple and can be used on a large scale.
(4)本发明采用快速、低成本的一步法合成工艺,利用水做反应介质,绿色环保;产品的吸附性能得到进一步提升,对Pb2+、Cd2+和Cu2+的最大吸附量分别为0.338、0.357和0.469mmol/g;操作简单,产率高,有利于推进规模化生产。(4) The present invention adopts a fast and low-cost one-step synthesis process, uses water as the reaction medium, and is environmentally friendly; the adsorption performance of the product is further improved, and the maximum adsorption capacity for Pb 2+ , Cd 2+ and Cu 2+ is respectively 0.338, 0.357 and 0.469mmol/g; the operation is simple, the yield is high, and it is beneficial to promote large-scale production.
具体实施方式Detailed ways
实施例1Example 1
称取海泡石粉末3g,加入50ml去离子水,40ml无水乙醇,形成海泡石悬浊液;将海泡石悬浊液在分散机上以8000rpm的速度高速搅拌8min形成凝胶,备用(I);将购买的质量浓度为45%的N-(三甲氧基甲硅烷基丙基)乙二胺三乙酸三钠盐溶液2ml溶于去离子水中,制备质量浓度为10%的盐溶液备用(II);继续在8000rpm搅拌条件下将质量浓度为10%的N-(三甲氧基甲硅烷基丙基)乙二胺三乙酸三钠盐溶液用量9ml(II)倾倒入(I)中,加入1ml无水乙醇,继续8000rpm搅拌25min,形成胺基羧酸修饰海泡石凝胶体系,其中钠盐溶液和海泡石的比例为9:3(v/w);将该反应凝胶体系转移至布氏漏斗,用无水乙醇抽滤并收集凝胶滤饼,将凝胶滤饼转移至广口瓶,置于烘箱中恒温70℃,持续18h后,将广口瓶中凝胶取出,80℃烘干,研磨后即得到胺基羧酸修饰海泡石3.17g。Take by weighing sepiolite powder 3g, add 50ml deionized water, 40ml dehydrated alcohol, form sepiolite suspension; The sepiolite suspension is stirred at a high speed of 8000rpm on the disperser for 8min to form a gel, for subsequent use ( 1); the mass concentration purchased is that 45% N-(trimethoxysilylpropyl) ethylenediaminetriacetic acid trisodium salt solution 2ml is dissolved in deionized water, and the preparation mass concentration is that 10% salt solution is standby (II); Continue to pour 9ml (II) of N-(trimethoxysilylpropyl) ethylenediaminetriacetic acid trisodium salt solution consumption amount of 10% under the stirring condition of 8000rpm into (I), Add 1ml of absolute ethanol and continue to stir at 8000rpm for 25min to form an aminocarboxylic acid modified sepiolite gel system, wherein the ratio of sodium salt solution to sepiolite is 9:3 (v/w); the reaction gel system Transfer to a Buchner funnel, filter with absolute ethanol and collect the gel filter cake, transfer the gel filter cake to a jar, place in an oven at a constant temperature of 70°C for 18 hours, then take out the gel in the jar , dried at 80°C, and after grinding, 3.17 g of aminocarboxylic acid-modified sepiolite was obtained.
实施例2Example 2
称取海泡石粉末2.5g,加入70ml去离子水,55ml无水乙醇,形成海泡石悬浊液;将海泡石悬浊液在分散机上以7000rpm的速度高速搅拌8min形成凝胶,备用(I);将购买的质量浓度为45%的N-(三甲氧基甲硅烷基丙基)乙二胺三乙酸三钠盐溶液2.5ml溶于去离子水中,制备质量浓度为15%的盐溶液备用(II);10000rpm搅拌条件下将质量浓度为15%的N-(三甲氧基甲硅烷基丙基)乙二胺三乙酸三钠盐溶液用量7.5ml(II)倾倒入(I)中,加入3ml无水乙醇,继续8000rpm搅拌25min,形成胺基羧酸修饰海泡石凝胶体系,其中钠盐溶液和海泡石的比例为7.5:2.5(v/w);将该反应凝胶体系转移至布氏漏斗,用无水乙醇抽滤并收集凝胶滤饼,将凝胶滤饼转移至广口瓶,置于烘箱中恒温80℃,持续18h后,将广口瓶中凝胶取出,80℃烘干,研磨后即得到胺基羧酸修饰海泡石2.55g。Weigh 2.5g of sepiolite powder, add 70ml of deionized water and 55ml of absolute ethanol to form a sepiolite suspension; stir the sepiolite suspension on a disperser at a speed of 7000rpm for 8min to form a gel, and set aside (1); 45% N-(trimethoxysilylpropyl) ethylenediaminetriacetic acid trisodium salt solution 2.5ml is dissolved in deionized water by the mass concentration purchased, and the preparation mass concentration is 15% salt The solution is ready for use (II); under the stirring condition of 10000 rpm, the mass concentration of 15% N-(trimethoxysilylpropyl) ethylenediaminetriacetic acid trisodium salt solution consumption 7.5ml (II) is poured into (I) , add 3ml of absolute ethanol, and continue to stir at 8000rpm for 25min to form an aminocarboxylic acid modified sepiolite gel system, wherein the ratio of sodium salt solution to sepiolite is 7.5:2.5 (v/w); the reaction gel Transfer the system to a Buchner funnel, filter with absolute ethanol and collect the gel filter cake, transfer the gel filter cake to a jar, place it in an oven at a constant temperature of 80°C for 18 hours, and put the gel in the jar Take it out, dry at 80°C, and grind to obtain 2.55 g of aminocarboxylic acid-modified sepiolite.
实施例3Example 3
称取海泡石4g,加入40ml去离子水,35ml无水乙醇,形成海泡石悬浊液;将海泡石悬浊液在分散机上以9000rpm的速度高速搅拌7min形成凝胶,备用(I);将购买的质量浓度为45%的N-(三甲氧基甲硅烷基丙基)乙二胺三乙酸三钠盐溶液4ml溶于去离子水中,制备质量浓度为20%的盐溶液备用(II);9000rpm搅拌条件下将质量浓度为20%的N-(三甲氧基甲硅烷基丙基)乙二胺三乙酸三钠盐溶液用量9ml(II)倾倒入(I)中,加入2ml无水乙醇,继续9000rpm搅拌25min,形成胺基羧酸修饰海泡石凝胶体系,其中钠盐溶液和海泡石的比例为4.5:2(v/w);将该反应凝胶体系转移至布氏漏斗,用无水乙醇抽滤并收集凝胶滤饼,将凝胶滤饼转移至广口瓶,置于烘箱中恒温80℃,持续18h后,将广口瓶中凝胶取出,65℃烘干,研磨后即得到胺基羧酸修饰海泡石4.20g。Take by weighing sepiolite 4g, add 40ml deionized water, 35ml dehydrated alcohol, form sepiolite suspension; The sepiolite suspension is formed gel with the speed of 9000rpm high-speed stirring 7min on disperser, standby (1 ); the purchased mass concentration is 45% N-(trimethoxysilylpropyl) ethylenediaminetriacetic acid trisodium salt solution 4ml is dissolved in deionized water, and the preparation mass concentration is 20% salt solution for subsequent use ( II); under the stirring condition of 9000rpm, the mass concentration is 20% N-(trimethoxysilylpropyl) ethylenediaminetriacetic acid trisodium salt solution consumption 9ml (II) is poured into (I), add 2ml without Water ethanol, continue stirring at 9000rpm for 25min to form aminocarboxylic acid modified sepiolite gel system, wherein the ratio of sodium salt solution and sepiolite is 4.5:2 (v/w); the reaction gel system is transferred to cloth filter with absolute ethanol to collect the gel filter cake, transfer the gel filter cake to a jar, and place it in an oven at a constant temperature of 80°C for 18 hours, then take out the gel in the jar and heat it at 65°C After drying and grinding, 4.20 g of aminocarboxylic acid-modified sepiolite was obtained.
实施例4Example 4
胺基羧酸修饰海泡石吸附水溶液Pb2+、Cd2+和Cu2+的应用。Amino carboxylic acid modified sepiolite for adsorption of Pb 2+ , Cd 2+ and Cu 2+ in aqueous solution.
配置浓度均为100mg/L的Pb2+、Cd2+和Cu2+溶液作为工作液,各量取25ml置于50ml离心管中,分别称取实施例1制备的胺基羧酸修饰海泡石0.025g加入已经添加Pb2+、Cd2+和Cu2+污染工作液的离心管中,胺基羧酸修饰海泡石与污染工作液的比例为1g/L,25℃恒温震荡6h,3800rpm离心后取上层清液,用原子吸收分光光度计测定溶液中Pb2+、Cd2+和Cu2+浓度,根据工作液中Pb2+和Cd2+浓度前后浓度差计算胺基羧酸修饰海泡石的吸附量。Prepare Pb 2+ , Cd 2+ , and Cu 2+ solutions with a concentration of 100mg/L as the working solution, measure 25ml each and place them in a 50ml centrifuge tube, and weigh the aminocarboxylic acid-modified seafoam prepared in Example 1 Add 0.025g of sepiolite to the centrifuge tube that has been added with Pb 2+ , Cd 2+ and Cu 2+ contaminated working solution, the ratio of aminocarboxylic acid modified sepiolite to contaminated working solution is 1g/L, shake at 25°C for 6h, After centrifuging at 3800rpm, take the supernatant, measure the concentration of Pb 2+ , Cd 2+ and Cu 2+ in the solution with an atomic absorption spectrophotometer, and calculate the concentration difference of Pb 2+ and Cd 2+ in the working solution before and after the concentration of amino carboxylic acid Modifies the adsorption amount of sepiolite.
结果显示:胺基羧酸修饰海泡石对溶液中铅、镉和铜污染均具有良好的吸附效果,其饱和吸附量为:铅0.338mmol/g,镉0.357mmol/g和铜0.469mmol/g。The results show that aminocarboxylic acid modified sepiolite has good adsorption effect on lead, cadmium and copper pollution in solution, and its saturated adsorption capacity is: lead 0.338mmol/g, cadmium 0.357mmol/g and copper 0.469mmol/g .
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CN105195085A (en) * | 2015-09-24 | 2015-12-30 | 北京新源环境有限公司 | Preparation method of dopamine modified sepiolite adsorbent |
CN106902745A (en) * | 2017-03-08 | 2017-06-30 | 江苏大学 | A kind of preparation method and applications of lithium/rubidium ion synchronization adsorbent |
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US20130095025A1 (en) * | 2011-10-12 | 2013-04-18 | Gwangju Institute Of Science And Technology | Granular mesoporous silica and preparation method thereof |
CN104041362A (en) * | 2014-05-13 | 2014-09-17 | 农业部环境保护科研监测所 | Method for safely producing rice in rice field with serious Cd pollution |
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US20130095025A1 (en) * | 2011-10-12 | 2013-04-18 | Gwangju Institute Of Science And Technology | Granular mesoporous silica and preparation method thereof |
CN104041362A (en) * | 2014-05-13 | 2014-09-17 | 农业部环境保护科研监测所 | Method for safely producing rice in rice field with serious Cd pollution |
Cited By (6)
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CN105195085A (en) * | 2015-09-24 | 2015-12-30 | 北京新源环境有限公司 | Preparation method of dopamine modified sepiolite adsorbent |
CN106902745A (en) * | 2017-03-08 | 2017-06-30 | 江苏大学 | A kind of preparation method and applications of lithium/rubidium ion synchronization adsorbent |
CN106902745B (en) * | 2017-03-08 | 2019-06-28 | 江苏大学 | A kind of lithium/rubidium ion synchronizes the preparation method and applications of adsorbent |
CN111167409A (en) * | 2019-12-04 | 2020-05-19 | 甘肃省科学院传感技术研究所 | Preparation method and application of Ni-NTA modified silicon dioxide coated ferroferric oxide magnetic nano functional assembly |
CN111167409B (en) * | 2019-12-04 | 2021-01-08 | 甘肃省科学院传感技术研究所 | Preparation method and application of Ni-NTA modified silicon dioxide coated ferroferric oxide magnetic nano functional assembly |
CN111186874A (en) * | 2020-01-17 | 2020-05-22 | 厦门大学 | Silanization reduction graphene oxide titanium dioxide composite material and preparation method and application thereof |
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