CN112452300B - Organic phosphorus composite material and preparation method and application thereof - Google Patents
Organic phosphorus composite material and preparation method and application thereof Download PDFInfo
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- CN112452300B CN112452300B CN202010958445.6A CN202010958445A CN112452300B CN 112452300 B CN112452300 B CN 112452300B CN 202010958445 A CN202010958445 A CN 202010958445A CN 112452300 B CN112452300 B CN 112452300B
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- 239000002131 composite material Substances 0.000 title claims abstract description 50
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 title claims description 14
- 239000011574 phosphorus Substances 0.000 title claims description 14
- 229910052698 phosphorus Inorganic materials 0.000 title claims description 14
- 238000002360 preparation method Methods 0.000 title abstract description 9
- 238000001179 sorption measurement Methods 0.000 claims abstract description 78
- IMQLKJBTEOYOSI-UHFFFAOYSA-N Phytic acid Natural products OP(O)(=O)OC1C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C1OP(O)(O)=O IMQLKJBTEOYOSI-UHFFFAOYSA-N 0.000 claims abstract description 42
- 239000000467 phytic acid Substances 0.000 claims abstract description 42
- 229940068041 phytic acid Drugs 0.000 claims abstract description 42
- IMQLKJBTEOYOSI-GPIVLXJGSA-N Inositol-hexakisphosphate Chemical compound OP(O)(=O)O[C@H]1[C@H](OP(O)(O)=O)[C@@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@@H]1OP(O)(O)=O IMQLKJBTEOYOSI-GPIVLXJGSA-N 0.000 claims abstract description 41
- 235000002949 phytic acid Nutrition 0.000 claims abstract description 41
- 239000000243 solution Substances 0.000 claims abstract description 22
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 19
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 18
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 5
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims description 4
- ZZCONUBOESKGOK-UHFFFAOYSA-N aluminum;trinitrate;hydrate Chemical compound O.[Al+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O ZZCONUBOESKGOK-UHFFFAOYSA-N 0.000 claims description 4
- 239000002244 precipitate Substances 0.000 claims description 4
- 238000004108 freeze drying Methods 0.000 claims description 3
- 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 claims description 2
- BUACSMWVFUNQET-UHFFFAOYSA-H dialuminum;trisulfate;hydrate Chemical compound O.[Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O BUACSMWVFUNQET-UHFFFAOYSA-H 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- CAYKLJBSARHIDI-UHFFFAOYSA-K trichloroalumane;hydrate Chemical compound O.Cl[Al](Cl)Cl CAYKLJBSARHIDI-UHFFFAOYSA-K 0.000 claims description 2
- 159000000013 aluminium salts Chemical class 0.000 claims 1
- 229910000329 aluminium sulfate Inorganic materials 0.000 claims 1
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- 239000000463 material Substances 0.000 abstract description 17
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- 239000002994 raw material Substances 0.000 abstract description 6
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- 229910052793 cadmium Inorganic materials 0.000 description 13
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 12
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 11
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- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 229910052624 sepiolite Inorganic materials 0.000 description 4
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 description 3
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- XNDZQQSKSQTQQD-UHFFFAOYSA-N 3-methylcyclohex-2-en-1-ol Chemical compound CC1=CC(O)CCC1 XNDZQQSKSQTQQD-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
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- 238000005481 NMR spectroscopy Methods 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
- B01J20/08—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04 comprising aluminium oxide or hydroxide; comprising bauxite
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- C—CHEMISTRY; METALLURGY
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Abstract
本发明属于重金属吸附技术领域,具体涉及一种高效吸附重金属Cd2+的有机磷–羟基铝复合吸附材料的制备方法及应用。其原料为铝盐和植酸,制备方法具体包括以下步骤:1)将铝盐溶于水中,在搅拌条件下加入植酸粉末,获得铝盐‑植酸混合溶液,并搅拌1 h左右,混合液中P:Al摩尔比为0.01~0.1;2)利用稀氢氧化钠溶液调节混合悬液pH 6.5左右,稳定0.5 h后,离心、过滤,冷冻干燥后即可制得有机磷负载羟基铝复合材料。通过水体吸附反应,复合材料对Cd2+的最大吸附量达205 mg/g,且在材料表面形成稳定的内圈络合物。该材料原料成本低廉、合成工艺简单,在治理Cd污染废水领域有广阔的前景。The invention belongs to the technical field of heavy metal adsorption, and in particular relates to a preparation method and application of an organophosphorus-hydroxyl aluminum composite adsorption material for efficiently adsorbing heavy metal Cd 2+ . The raw materials are aluminum salt and phytic acid. The preparation method specifically includes the following steps: 1) Dissolving the aluminum salt in water, adding phytic acid powder under stirring conditions to obtain a mixed solution of aluminum salt-phytic acid, and stirring for about 1 hour, mixing The molar ratio of P:Al in the solution is 0.01~0.1; 2) Use dilute sodium hydroxide solution to adjust the pH of the mixed suspension to about 6.5, stabilize it for 0.5 h, centrifuge, filter, and freeze-dry to prepare the organophosphorus-loaded hydroxyl aluminum compound Material. Through the water adsorption reaction, the maximum adsorption capacity of the composite material for Cd 2+ reaches 205 mg/g, and a stable inner ring complex is formed on the surface of the material. The raw material cost of the material is low, the synthesis process is simple, and the material has broad prospects in the field of treating Cd polluted wastewater.
Description
技术领域technical field
本发明属于重金属吸附技术领域,尤其是属于水体重金属去除治理技术领域,具体涉及一种高效吸附重金属Cd2+的有机磷–羟基铝复合吸附材料及其制备方法及应用。The invention belongs to the technical field of heavy metal adsorption, in particular to the technical field of removal and treatment of heavy metals in water, and specifically relates to an organophosphorus-hydroxyl aluminum composite adsorption material for efficiently adsorbing heavy metal Cd 2+ and its preparation method and application.
背景技术Background technique
镉是剧毒重金属,随着工农业的发展,不合理的农药化肥使用等使我国镉污染形势更加严峻。镉在环境中不易降解,移动性强,是动植物非必需元素,有一定的挥发性,可致畸、致癌、致突变,能通过空气和食物链在人类和动植物体内持续积累,直至产生严重危害。目前常用来修复环境中镉污染的方法有吸附、离子交换、膜过滤、生物法等,其中吸附法因材料来源广、经济高效、较少二次污染而被广泛应用。开发高效、清洁、低成本、易制备的新型吸附剂是水处理和净化领域的热门方向。Cadmium is a highly toxic heavy metal. With the development of industry and agriculture, the unreasonable use of pesticides and fertilizers has made the situation of cadmium pollution in my country more serious. Cadmium is not easy to degrade in the environment and has strong mobility. It is a non-essential element for animals and plants. It has certain volatility and can be teratogenic, carcinogenic, and mutagenic. harm. At present, the methods commonly used to repair cadmium pollution in the environment include adsorption, ion exchange, membrane filtration, biological methods, etc. Among them, the adsorption method is widely used because of its wide source of materials, cost-effectiveness, and less secondary pollution. The development of new adsorbents that are efficient, clean, low-cost, and easy to prepare is a hot direction in the field of water treatment and purification.
目前吸附剂多采用活性矿物、生物炭、耐性微生物等,但这些材料普遍存在一些缺点:例如生物炭制备条件复杂、成本较高;微生物培养复杂、存活性低;矿物质材料吸附效率低等,因此不适合大规模应用。铁/锰/铝羟基化合物,多采用碱沉淀方法制备,操作简单,且材料表面疏松多孔,具有较大的比表面积,并含有丰富的羟基,能通过静电吸附、络合、沉淀等物理化学反应有效去除重金属。尤其是铁/锰/铝氢氧化物经过有机改性,可以丰富吸附剂表面的官能团,提高其对重金属污染物的吸附能力。磷酸盐化合物可与重金属发生强螯合作用,因此多用来制备重金属吸附材料,但目前人们主要研究多集中在无机磷,对有机磷的研究较少。土壤中有机磷占总磷的30-65%,在高有机质土壤中有机磷高达90%,作物吸收后可在体内形成多种有机磷,如植酸等,因此该原料是一种低成本、易获得的材料。At present, active minerals, biochar, and resistant microorganisms are mostly used as adsorbents, but these materials generally have some disadvantages: for example, the preparation conditions of biochar are complicated and the cost is high; the cultivation of microorganisms is complicated and the viability is low; the adsorption efficiency of mineral materials is low, etc. Therefore, it is not suitable for large-scale application. Iron/manganese/aluminum hydroxyl compounds are mostly prepared by alkali precipitation method, which is easy to operate, and the surface of the material is loose and porous, has a large specific surface area, and is rich in hydroxyl groups, which can undergo physical and chemical reactions such as electrostatic adsorption, complexation, and precipitation. Effectively removes heavy metals. Especially the organic modification of iron/manganese/aluminum hydroxide can enrich the functional groups on the surface of the adsorbent and improve its adsorption capacity for heavy metal pollutants. Phosphate compounds can have a strong chelation effect with heavy metals, so they are often used to prepare heavy metal adsorption materials. However, most of the current research focuses on inorganic phosphorus, and less research on organic phosphorus. The organic phosphorus in the soil accounts for 30-65% of the total phosphorus, and the organic phosphorus in the soil with high organic matter is as high as 90%. After the crop absorbs it, it can form a variety of organic phosphorus in the body, such as phytic acid. Therefore, this raw material is a low-cost, readily available materials.
Huihui,Huang用无定形氢氧化铝-细菌复合材料吸附Cd2+,但研究发现细菌改性的无定形氢氧化铝材料在中性及碱性环境中对Cd2+的吸附促进效果不明显。粟燕等发现氢氧化铝-聚丙烯酰胺复合材料在温度为10℃、30℃和50℃条件下,对Cd2+的最大吸附量qmax的值分别是44.43mg/g、50.11mg/g和54.81mg/g。盛姣等发现植酸复合海泡石的吸附材料在30℃,吸附剂浓度为18g/L时,在pH 3.8具备最佳吸附性能,对Cd2+的最大吸附量为2.67mg/g。不难发现,这些材料对Cd2+的吸附均存在一定局限,故本研究研发一种新型高效吸附Cd2+的有机磷负载羟基铝复合材料。Huihui and Huang used amorphous aluminum hydroxide-bacteria composites to adsorb Cd 2+ , but found that the bacteria-modified amorphous aluminum hydroxide materials had no obvious effect on the adsorption of Cd 2+ in neutral and alkaline environments. Su Yan et al. found that the maximum adsorption capacity qmax of aluminum hydroxide-polyacrylamide composites at temperatures of 10°C, 30°C, and 50° C were 44.43mg/g, 50.11mg/g, respectively. and 54.81mg/g. Sheng Jiao et al. found that the adsorption material of phytic acid composite sepiolite had the best adsorption performance at pH 3.8 when the adsorbent concentration was 18g/L at 30°C, and the maximum adsorption capacity for Cd 2+ was 2.67mg/g. It is not difficult to find that these materials have certain limitations in the adsorption of Cd 2+ , so this study developed a new organophosphorus-supported hydroxyl aluminum composite material that can efficiently adsorb Cd 2+ .
参考文献:references:
1、Du HH,Huang,QY,Yang RJ,Tie BQ,Lei M Cd sequestration by bacteria–aluminum hydroxide composites[J].CHEMOSPHERE,2018,198,75-82.1. Du HH, Huang, QY, Yang RJ, Tie BQ, Lei M Cd sequestration by bacteria–aluminum hydroxide composites[J].CHEMOSPHERE,2018,198,75-82.
2、粟燕,刘人源,陈振玲.纳米氢氧化铝-聚丙烯酰胺复合絮凝剂对镉离子的吸附研究[J].离子交换与吸附,2016,32(04):324-332.2. Su Yan, Liu Renyuan, Chen Zhenling. Study on the adsorption of cadmium ions by nano-aluminum hydroxide-polyacrylamide composite flocculant[J]. Ion Exchange and Adsorption, 2016,32(04):324-332.
3、盛姣,曾桂华,闫淑梅,何爱翠,刘颖.植酸海泡石复合重金属吸附剂对Cd2+的吸附研究[J].安徽农业科学,2013,41(24):10087-10088.3. Sheng Jiao, Zeng Guihua, Yan Shumei, He Aicui, Liu Ying. Adsorption of Cd 2+ by Phytic Acid Sepiolite Composite Heavy Metal Adsorbent[J]. Anhui Agricultural Sciences, 2013,41(24):10087-10088.
发明内容Contents of the invention
本发明的目的是提供一种有机磷复合材料,能高效吸附Cd2+,同时制备简单、不会造成二次污染。The purpose of the present invention is to provide an organophosphorus composite material, which can efficiently adsorb Cd 2+ , is simple to prepare and does not cause secondary pollution.
一种有机磷复合材料,其结构式如下所示:A kind of organophosphorus composite material, its structural formula is as follows:
所述有机磷复合材料的制备方法,包括以下步骤:The preparation method of described organophosphorus composite material, comprises the following steps:
S1、在铝盐中加入有机磷,混合均匀,调整pH值后离心、过滤,得到沉淀;S1, adding organophosphorus to the aluminum salt, mixing evenly, adjusting the pH value, centrifuging and filtering to obtain a precipitate;
S2、将沉淀冷冻干燥,得到有机磷复合材料。S2. Freeze-drying the precipitate to obtain an organophosphorus composite material.
优选的,所述铝盐为水溶性铝盐。Preferably, the aluminum salt is a water-soluble aluminum salt.
只有水溶性的铝盐才能通过溶解在水中调节水解平衡,然后把铝盐转化为无定形羟基铝,才能制备本发明需要的有机磷复合材料。Only water-soluble aluminum salts can be dissolved in water to adjust the hydrolysis balance, and then the aluminum salts can be converted into amorphous hydroxyaluminum to prepare the organophosphorus composite material required by the present invention.
优选的,所述水溶性铝盐为氯化铝、氯化铝水合物、硝酸铝、硝酸铝水合物、硫酸铝、硫酸铝水合物中的一种或几种。Preferably, the water-soluble aluminum salt is one or more of aluminum chloride, aluminum chloride hydrate, aluminum nitrate, aluminum nitrate hydrate, aluminum sulfate, and aluminum sulfate hydrate.
进一步优选的,所述铝盐为硝酸铝水合物。Further preferably, the aluminum salt is aluminum nitrate hydrate.
硝酸铝密度小、溶解性能好,易溶于水,乙醇,丙酮,硝酸。且硝酸根离子易于去除,对复合材料干扰小,九水硝酸铝是硝酸铝中最稳定的形态。Aluminum nitrate has low density, good solubility, and is easily soluble in water, ethanol, acetone, and nitric acid. Moreover, the nitrate ion is easy to remove and has little interference to the composite material. Aluminum nitrate nonahydrate is the most stable form of aluminum nitrate.
优选的,所述混合为磁力搅拌器在150~500rpm转速下搅拌混合。Preferably, the mixing is stirring and mixing with a magnetic stirrer at a rotational speed of 150-500 rpm.
优选的,所述有机磷为植酸。Preferably, the organic phosphorus is phytic acid.
植酸是大多数土壤和沉积物中含量最丰富的有机磷酸盐,含有大量磷酸基团,是一种少见的金属多齿螯合剂,有研究发现植酸可以提高重金属污染土壤中Cd2+的浸出速度与溶出量。且植酸低成本,易获得,在自然环境中大量存在。Phytic acid is the most abundant organophosphate in most soils and sediments. It contains a large number of phosphate groups and is a rare metal polydentate chelating agent. Some studies have found that phytic acid can increase the concentration of Cd 2+ in heavy metal-polluted soils. The leaching rate and the amount of leaching. Moreover, phytic acid is low-cost, easy to obtain, and exists in large quantities in the natural environment.
优选的,所述有机磷复合材料中P:Al摩尔比为1:(10~100)。Preferably, the molar ratio of P:Al in the organophosphorus composite material is 1:(10-100).
植酸分子量大,过高的P:Al摩尔比,提高了复合材料在实际应用中的施加量,进而提高成本,且羟基铝对植酸的有一定吸附上限;P:Al摩尔比过低,则对羟基铝的改性不明显。The molecular weight of phytic acid is large, and the molar ratio of P:Al is too high, which increases the application amount of composite materials in practical applications, thereby increasing the cost, and aluminum hydroxy has a certain upper limit for the adsorption of phytic acid; the molar ratio of P:Al is too low, The modification of hydroxyaluminum is not obvious.
进一步优选的,模拟自然环境中的矿物有机的复合比,同时从修复剂的实际应用方面考虑,所述有机磷复合材料中P:Al摩尔比为0.1。Further preferably, to simulate the mineral-organic composite ratio in the natural environment, and considering the practical application of the restoration agent, the molar ratio of P:Al in the organophosphorus composite material is 0.1.
优选的,所述步骤S1调整pH值至6.5±0.2,用稀碱溶液调节pH。Preferably, the step S1 adjusts the pH value to 6.5±0.2, and adjusts the pH with a dilute alkali solution.
所述pH需控制在6.5±0.2,在pH 5左右,铝离子开始产生沉淀,进一步保证转化完全,控制在6.5左右即无需再加碱,过量的碱易使氢氧化铝转变为偏铝酸盐。The pH needs to be controlled at 6.5±0.2. At a pH of about 5, aluminum ions begin to precipitate, further ensuring complete conversion. Controlling the pH at about 6.5 means that there is no need to add alkali. Excessive alkali can easily turn aluminum hydroxide into metaaluminate .
进一步优选的,碱溶液可以为NaOH溶液、KOH溶液。Further preferably, the alkaline solution may be NaOH solution or KOH solution.
优选的,所述步骤S1调整pH值后先稳定0.5h,期间pH微调,离心。Preferably, after adjusting the pH value in step S1, it is stabilized for 0.5 h, during which the pH is fine-tuned and centrifuged.
本发明还提供了所述有机磷复合材料吸附重金属Cd2+的应用,具体方法为:The present invention also provides the application of the organic phosphorus composite material to adsorb heavy metal Cd 2+ , the specific method is:
在离心管中加入有机磷复合材料,有机磷复合材料和重金属镉按100mg:(0~4)mg的比例进行试验,pH控制在6.5±0.05。样品在恒温摇床中(25℃)下震荡24h后过滤,用ICP(电感耦合等离子体质谱)测Cd2+浓度,根据吸附前后Cd2+浓度的差值计算吸附量。有机磷复合材料理论吸附量可达205mg/g,具有良好的重金属吸附效果。Add organophosphorus composite material into the centrifuge tube, test the ratio of organophosphorus composite material and heavy metal cadmium at 100 mg:(0-4) mg, and control the pH at 6.5±0.05. The sample was shaken in a constant temperature shaker (25°C) for 24 hours and then filtered. The Cd 2+ concentration was measured by ICP (Inductively Coupled Plasma Mass Spectrometry), and the adsorption amount was calculated according to the difference between the Cd 2+ concentration before and after adsorption. The theoretical adsorption capacity of organophosphorus composite materials can reach 205mg/g, which has good heavy metal adsorption effect.
下面对本发明进行进一步阐述:The present invention is further elaborated below:
本发明选取纯羟基铝、植酸为原料制备复合材料。铝羟基化合物广泛的存在于水生、地质环境中,具有较大的表面积和丰富的羟基官能团,能有效吸附金属,植酸是大多数土壤和沉积物中含量最丰富的有机磷酸盐,含有大量磷酸基团,是一种少见的金属多齿螯合剂,有研究发现植酸可以提高重金属污染土壤中Cd2+的浸出速度与溶出量。相对于其它铁/锰羟基化合物,铝(氢)氧化物吸附植酸通过表面的H2O和-OH基与磷酸基配位交换进行。因此,吸附过程释放OH-,同时吸附促进了磷酸基团的去质子化。红外光谱表明,植酸吸附在羟基铝上形成了Al–O–P键。纯羟基铝活性位点密度更大,对植酸有更好的结合能力,吸附量达到1.70mol/kg(34.3μmol/m2),而三水铝石和三羟铝石吸附植酸的量分别只有0.52μmol/m2和0.4μmol/m2。溶液化学分析、红外光谱表征和量子化学理论计算表明植酸通过3个磷酸基团吸附在羟基铝表面。The invention selects pure hydroxyl aluminum and phytic acid as raw materials to prepare composite materials. Aluminum hydroxy compounds are widely found in aquatic and geological environments. They have large surface areas and abundant hydroxyl functional groups, which can effectively adsorb metals. Phytic acid is the most abundant organophosphate in most soils and sediments. It contains a large amount of phosphoric acid Phytic acid is a rare metal polydentate chelating agent. Some studies have found that phytic acid can increase the leaching speed and amount of Cd 2+ in heavy metal polluted soil. Compared with other iron/manganese hydroxyl compounds, the adsorption of phytic acid by aluminum (hydr) oxide is carried out through the coordination exchange between H 2 O and -OH groups on the surface and phosphoric acid groups. Therefore, the adsorption process releases OH-, while the adsorption promotes the deprotonation of the phosphate group. Infrared spectroscopy showed that phytic acid was adsorbed on aluminum hydroxy to form Al–O–P bonds. Pure hydroxyaluminum has a higher density of active sites and better binding ability to phytic acid, with an adsorption capacity of 1.70 mol/kg (34.3 μmol/m 2 ), while gibbsite and bayerite adsorbed phytic acid respectively Only 0.52 μmol/m 2 and 0.4 μmol/m 2 . Solution chemical analysis, infrared spectrum characterization and quantum chemical theoretical calculations showed that phytic acid was adsorbed on the surface of hydroxyaluminum through three phosphoric acid groups.
本发明采用碱沉淀方法制备,操作简单。复合材料能显著吸附Cd2+,一方面是因为植酸的加入增加羟基铝表面负电荷,从而增强了对Cd2+的静电吸附能力,另一方面为纯羟基铝表面的羟基官能团以及纯羟基铝表面植酸的多重磷酸基团与Cd2+发生络合作用,形成Al-IHP-Cd三元络合物,从而增加对Cd2+的吸附量。The invention adopts the alkali precipitation method to prepare, and the operation is simple. The composite material can significantly adsorb Cd 2+ . On the one hand, the addition of phytic acid increases the negative charge on the surface of aluminum hydroxy, thereby enhancing the electrostatic adsorption capacity for Cd 2+ . The multiple phosphate groups of phytic acid on the aluminum surface complexed with Cd 2+ to form Al-IHP-Cd ternary complex, thereby increasing the adsorption amount of Cd 2+ .
本发明的优点如下:The advantages of the present invention are as follows:
1.本发明所述方法制备简单,在常温常压下进行,无特殊条件1. The method of the present invention is simple to prepare, and is carried out at normal temperature and pressure without special conditions
2.本发明所述植酸是一种低成本、易获得的有机磷类材料,在自然环境中常见且大量存在。2. The phytic acid described in the present invention is a low-cost, easy-to-obtain organophosphorus material, which is common and abundant in the natural environment.
3.本发明所述原料为自然环境中广泛存在的,模拟土壤环境中的矿物-有机复合体组成,对基质理化性质改变小,不易造成二次污染。3. The raw materials of the present invention are widely present in the natural environment, and are composed of mineral-organic complexes in simulated soil environments, which have little change in the physical and chemical properties of the matrix and are not easy to cause secondary pollution.
4.本发明将植酸负载于羟基铝表面,改善了其物理化学性质,提高了对镉的吸附性能。4. The present invention loads phytic acid on the surface of hydroxyaluminum, improves its physical and chemical properties, and improves the adsorption performance to cadmium.
5.本发明所述植酸-羟基铝-镉三元体系中,Cd既与水羟基铝的–OH反应,也与植酸的磷酸基团–PO4反应,并且生成Al-IHP-Cd稳定配位物,对Cd2+的最大吸附量高达205mg/g(~20wt.%),远远大于其它类型吸附剂。5. In the phytic acid-hydroxyaluminum-cadmium ternary system of the present invention, Cd not only reacts with the –OH of hydroxaluminum, but also reacts with the phosphoric acid group –PO of phytic acid, and generates Al-IHP-Cd stable The complex has a maximum adsorption capacity of 205mg/g (~20wt.%) for Cd 2+ , which is far greater than other types of adsorbents.
本发明提供的复合体亦可应用于水体其它性质相近的重金属(Pb2+、Cu2+、Ni2+、Zn2 +)吸附去除。The complex provided by the invention can also be applied to adsorb and remove other heavy metals (Pb 2+ , Cu 2+ , Ni 2+ , Zn 2 + ) with similar properties in water bodies.
附图说明Description of drawings
图1为本发明实施例中纯羟基铝(AAH)、低浓度有机磷负载羟基铝复合材料(AAH-OP_low)、高浓度有机磷负载羟基铝复合材料(AAH-OP_high)的TEM图谱。Figure 1 is the TEM spectrum of pure hydroxyaluminum (AAH), low-concentration organophosphorus-supported hydroxyaluminum composite material (AAH-OP_low), and high-concentration organophosphorus-supported hydroxyaluminum composite material (AAH-OP_high) in the examples of the present invention.
图2为实施案例中纯羟基铝(AAH)、低浓度有机磷负载羟基铝复合材料(AAH-OP_low)、高浓度有机磷负载羟基铝复合材料(AAH-OP_high)的XRD图谱。Fig. 2 is the XRD patterns of pure aluminum hydroxy (AAH), low-concentration organophosphorus-supported aluminum hydroxy composite material (AAH-OP_low), and high-concentration organophosphorus-supported aluminum hydroxy composite material (AAH-OP_high) in the implementation case.
图3为实施案例中纯羟基铝(AAH)、低浓度有机磷负载羟基铝复合材料(AAH-OP_low)、高浓度有机磷负载羟基铝复合材料(AAH-OP_high)的FTIR图谱。Fig. 3 is the FTIR spectra of pure aluminum hydroxy (AAH), low-concentration organophosphorus-supported aluminum hydroxy composite material (AAH-OP_low), and high-concentration organophosphorus-supported aluminum hydroxy composite material (AAH-OP_high) in the implementation case.
图4为植酸负载羟基铝的结构示意图Figure 4 is a schematic diagram of the structure of phytic acid supported aluminum hydroxy
图5为吸附性能测试中纯羟基铝(AAH)、低浓度有机磷负载羟基铝复合材料(AAH-OP_low)、高浓度有机磷负载羟基铝复合材料(AAH-OP_high)对Cd2+的吸附等温线。Figure 5 shows the adsorption isotherms of pure hydroxyaluminum (AAH), low-concentration organophosphorus-supported hydroxyaluminum composite (AAH-OP_low), and high-concentration organophosphorus-supported hydroxyaluminum composite (AAH-OP_high) on Cd 2+ in the adsorption performance test Wire.
图6为吸附性能测试中纯羟基铝(AAH)、有机磷负载羟基铝复合材料吸附Cd2+前后的NMR图谱对比。Figure 6 is a comparison of the NMR spectra of pure aluminum hydroxy (AAH) and organophosphorus-supported aluminum hydroxy composites before and after adsorption of Cd 2+ in the adsorption performance test.
图7为吸附性能测试中纯羟基铝(AAH)、有机磷负载羟基铝复合材料吸附Cd2+前后的FTIR图谱对比。Fig. 7 is a comparison of FTIR spectra before and after adsorption of Cd 2+ by pure aluminum hydroxy (AAH) and organophosphorus-supported aluminum hydroxy composites in the adsorption performance test.
图8为高浓度有机磷负载羟基铝复合材料(AAH-OP_high)对Cd2+的pH吸附实验图谱。Fig. 8 is a pH adsorption experiment spectrum of Cd 2+ on a high-concentration organophosphorus-supported aluminum hydroxy composite material (AAH-OP_high).
具体实施方式Detailed ways
以下结合具体优选的实施例对本发明作进一步描述,但并不因此而限制本发明的保护范围。The present invention will be further described below in conjunction with specific preferred embodiments, but the protection scope of the present invention is not limited thereby.
实施例1Example 1
两种浓度有机磷负载羟基铝复合材料的制备,纯羟基铝作为参照,探究复合材料的表面形貌、官能团电位及空间结构。步骤如下:Two concentrations of organophosphorus-supported hydroxyl aluminum composites were prepared, and pure hydroxyl aluminum was used as a reference to explore the surface morphology, functional group potential and spatial structure of the composites. Proceed as follows:
有机磷负载羟基铝复合材料的合成步骤如下:准确称量0.05mol九水硝酸铝(Al(NO3)3·9H2O)溶于500mL去离子水,用磁力搅拌器搅拌溶,任意取其中两份分别加入0.33g、3.3g植酸,反应1h,向溶液缓慢加入1mol/L NaOH溶液,将溶液pH调节为6.5,稳定0.5h后停止搅拌,将合成的有机磷负载羟基铝复合物悬液离心去除上清液,此步骤重复3次,经冷冻干燥后即制备完成。The synthesis steps of organophosphorus-loaded hydroxyl aluminum composite materials are as follows: accurately weigh 0.05mol aluminum nitrate nonahydrate (Al(NO 3 ) 3 9H 2 O) and dissolve it in 500mL deionized water, stir the solution with a magnetic stirrer, and take any of them Add 0.33g and 3.3g phytic acid respectively to the two parts, react for 1h, slowly add 1mol/L NaOH solution to the solution, adjust the pH of the solution to 6.5, stop stirring after 0.5h of stabilization, and suspend the synthesized organophosphorus-loaded hydroxyaluminum complex The liquid was centrifuged to remove the supernatant, this step was repeated 3 times, and the preparation was completed after freeze-drying.
吸附剂表面ξ电位由Zeta电位分析仪(Zetaplus90,Brookhaven)测定,测试前将每种吸附剂分散于0.1mol/L KNO3溶液,每种吸附剂设置3个平行样,调节pH至6.5,放入25℃恒温振荡器平衡24h。结果如表1所示,植酸的加入使矿物表面电位由正变为负,且复合材料中P:Al摩尔比越高,降低程度越大。表面负电性的减少使吸附剂对Cd2+的静电吸引增加,从而促进其吸附。The surface ξ potential of the adsorbent was measured by a Zeta potential analyzer (Zetaplus90, Brookhaven). Before the test, each adsorbent was dispersed in a 0.1mol/L KNO3 solution, and three parallel samples were set for each adsorbent, and the pH was adjusted to 6.5. Put into 25 ℃ constant temperature shaker and balance for 24h. The results are shown in Table 1. The addition of phytic acid changed the surface potential of minerals from positive to negative, and the higher the molar ratio of P:Al in the composite material, the greater the degree of reduction. The reduction of surface negativity increases the electrostatic attraction of the adsorbent to Cd 2+ , thereby facilitating its adsorption.
表1三种吸附剂在pH 6.5、0.1mol/L KNO3条件下的ξ电位表Table 1 The ξ potential table of three kinds of adsorbents under the conditions of pH 6.5 and 0.1mol/L KNO 3
复合体样本经真空冷冻干燥处理后,用玛瑙研钵磨成细粉末,其表面形貌由Tecnai G2 F20 S-TWIN透射电子显微镜(TEM,美国FEI公司)分析测定,结果如图1所示,合成的纯羟基铝为不规则纳米颗粒,质地松散,属于无定形氢氧化铝(AAH),制备复合物时植酸的加入对纯羟基铝的表面形貌影响并不显著。After the composite sample was vacuum freeze-dried, it was ground into a fine powder with an agate mortar, and its surface morphology was analyzed and determined by a Tecnai G2 F20 S-TWIN transmission electron microscope (TEM, FEI, USA). The results are shown in Figure 1. The synthesized pure aluminum hydroxide is irregular nanoparticles with loose texture, which belongs to amorphous aluminum hydroxide (AAH). The addition of phytic acid in the preparation of the composite has no significant effect on the surface morphology of pure aluminum hydroxide.
布鲁克D8 ADVANCE粉末衍射仪(XRD,德国Bruker公司)分析测定复合体样本晶体结构。结果如图2所示,植酸的加入可以缓解纯羟基铝结晶度增高的趋势,AAH上的植酸处于表面络合向表面沉淀过渡的阶段。The Bruker D8 ADVANCE powder diffractometer (XRD, Bruker, Germany) analyzed and determined the crystal structure of the composite sample. The results are shown in Figure 2. The addition of phytic acid can alleviate the trend of increasing the crystallinity of pure hydroxyaluminum, and the phytic acid on AAH is in the transition stage from surface complexation to surface precipitation.
用NICOLET 5700傅立叶红外光谱仪(ATR-FTIR,美国热电尼高力仪器公司)测定其FTIR图,结果如图3所示,根据ATR-FTIR图,负载植酸后,Al-O-H的化学环境发生了改变,其中AAH-OP_high的FTIR光谱变化更加明显,在946cm-1处Al-OH峰发生蓝移,在883cm-1、1065cm-1、1176cm-1、1724cm-1出现新峰。1065cm-1、1176cm-1对应吸附在AAH表面植酸的P-O-Al的对称和非对称伸缩振动。1724cm-1处的峰为植酸中的C-C,883cm-1处峰可能为P-OH的拉伸振动产生,2428cm-1峰强减弱,猜测为结晶度高的纯羟基铝杂质中Al-OH的吸收峰。在pH 6~7,植酸中的四个磷酸基团质子化,因此与AAH发生表面络合的磷酸基团不超过四个,主要发生在1、3、5位的三个磷酸基团。故本发明提供的这有机磷负载羟基铝复合材料具体结构式如图4。Use NICOLET 5700 Fourier transform infrared spectrometer (ATR-FTIR, American Thermoelectric Nicolis Instrument Company) to measure its FTIR figure, the result is shown in Figure 3, according to the ATR-FTIR figure, after loading phytic acid, the chemical environment of Al-OH occurred The FTIR spectrum of AAH-OP_high changes more obviously, the Al-OH peak at 946cm -1 has a blue shift, and new peaks appear at 883cm -1 , 1065cm -1 , 1176cm -1 and 1724cm -1 . 1065cm -1 and 1176cm -1 correspond to the symmetric and asymmetric stretching vibrations of PO-Al adsorbed on the surface of AAH with phytic acid. The peak at 1724cm -1 is CC in phytic acid, the peak at 883cm -1 may be generated by the stretching vibration of P-OH, and the peak at 2428cm -1 is weakened, which is guessed to be Al-OH in pure hydroxyaluminum impurities with high crystallinity the absorption peak. At pH 6-7, the four phosphate groups in phytic acid are protonated, so no more than four phosphate groups can be complexed with AAH on the surface, mainly three phosphate groups at
实施例2Example 2
吸附性能测试一Adsorption performance test one
有机磷负载羟基铝复合材料对Cd2+的等温吸附实验,纯羟基铝吸附Cd2+作为参照,测试吸附剂在25℃、pH 6.5的条件下最大吸附量。The isothermal adsorption experiment of Cd 2+ on organophosphorus-supported hydroxyl-aluminum composites, pure hydroxyl-aluminum adsorption of Cd 2+ was used as a reference, and the maximum adsorption capacity of the adsorbent was tested at 25°C and pH 6.5.
实验在50mL离心管中进行,用实施案例1中制备的复合体作为吸附剂,在离心管中加入一定体积的吸附剂、Cd2+母液,用0.1mol/L KNO3定容到等体积并控制最终吸附剂浓度为0.1g/L,Cd2+浓度为0~40mg/L,调节体系pH为6.5。每个浓度设三个平行,以不加吸附剂的作对照。将离心管置于25℃恒温振荡器中反应24h,5000g离心15min,离心管中的上清液过0.45μm尼龙滤膜,随后用ICP(电感耦合等离子体质谱)测量滤液中Cd2+浓度。测量数据用Langmuir模型进行拟合。The experiment was carried out in a 50mL centrifuge tube. The complex prepared in Example 1 was used as the adsorbent. A certain volume of adsorbent and Cd 2+ mother liquor were added to the centrifuge tube, and 0.1mol/L KNO 3 was used to make the volume equal to that of the adsorbent. The final adsorbent concentration is controlled to be 0.1g/L, the Cd 2+ concentration is 0-40mg/L, and the pH of the system is adjusted to 6.5. Three parallels were set up for each concentration, and no adsorbent was used as the control. The centrifuge tube was placed in a constant temperature oscillator at 25°C for 24h, centrifuged at 5000g for 15min, the supernatant in the centrifuge tube was passed through a 0.45μm nylon filter membrane, and then the Cd 2+ concentration in the filtrate was measured by ICP (Inductively Coupled Plasma Mass Spectrometry). The measured data were fitted with a Langmuir model.
表2实施例对镉的等温吸附线拟合参数Table 2 embodiment is to the isotherm adsorption line fitting parameter of cadmium
注释:K表示吸附亲和力常数(L/g),Qmax表示Langmuir模型拟合得出最大吸附量(mg/g)是以单位质量吸附的Cd2+的质量来计Note: K represents the adsorption affinity constant (L/g), and Q max represents the maximum adsorption amount (mg/g) obtained by fitting the Langmuir model, which is calculated by the mass of Cd 2+ adsorbed per unit mass
根据图5及表2,AAH、AAH-OP_low、AAH-OP_high对Cd2+的吸附行为属于单分子层吸附,可以用Langmuir模型很好的拟合,对Cd2+的吸附能力大小排序为AAH-OP_high>AAH-OP_low>AAH,其中AAH-OP_high的最大吸附量为205mg/g,高浓度的植酸加入可以提高对Cd2+的吸附性能。According to Figure 5 and Table 2, the adsorption behavior of AAH, AAH-OP_low, and AAH-OP_high on Cd 2+ belongs to the monolayer adsorption, which can be well fitted by the Langmuir model, and the adsorption capacity of Cd 2+ is ranked as AAH -OP_high>AAH-OP_low>AAH, where the maximum adsorption capacity of AAH-OP_high is 205mg/g, adding high concentration of phytic acid can improve the adsorption performance of Cd 2+ .
用Bruker 600兆宽腔固体核磁共振波谱仪(NMR,德国Bruker公司)测定1H NMR谱图,分析官能团及结构信息。根据图6AAH-OP_high的1H NMR谱图,植酸中P-O-H中的H与水铝矿的Al-O-H中的H的化学环境极其相似。与AAH吸附Cd2+前后的H特征峰的变化相比,AAH-OP_high吸附Cd2+前后H特征峰的峰面积变化幅度变小。这说明Cd2+主要与植酸的磷酸基团包含的–OH发生络合作用,而只有一小部分的Cd2+仍与AAH的–OH发生络合作用。A Bruker 600M wide-cavity solid-state nuclear magnetic resonance spectrometer (NMR, Bruker, Germany) was used to measure 1 H NMR spectra, and analyze functional groups and structural information. According to the 1 H NMR spectrum of Figure 6AAH-OP_high, the chemical environment of H in POH in phytic acid is very similar to that in Al-OH in gibbsite. Compared with the change of H characteristic peak before and after AAH adsorption of Cd 2+ , the peak area change range of H characteristic peak before and after AAH-OP_high adsorption of Cd 2+ is smaller. This shows that Cd 2+ mainly complexes with the –OH contained in the phosphate group of phytic acid, while only a small part of Cd 2+ still complexes with the –OH of AAH.
吸附剂吸附Cd2+前后的样本经真空冷冻干燥处理后,用玛瑙研钵磨成细粉末,用NICOLET 5700傅立叶红外光谱仪(ATR-FTIR,美国热电尼高力仪器公司)测定其FTIR图。从图7可知,Cd2+既与AAH的–OH反应,也与植酸的磷酸基团的–OH反应,与前面实验数据一致,植酸的加入提高了羟基铝吸附Cd2+的能力。The samples before and after adsorption of Cd 2+ on the adsorbent were vacuum freeze-dried, ground into fine powder with an agate mortar, and their FTIR patterns were measured with a NICOLET 5700 Fourier transform infrared spectrometer (ATR-FTIR, American Thermo-Nicole Instruments Inc.). It can be seen from Figure 7 that Cd 2+ reacts with both the –OH of AAH and the –OH of the phosphoric acid group of phytic acid. Consistent with the previous experimental data, the addition of phytic acid improves the ability of hydroxyaluminum to adsorb Cd 2+ .
吸附性能测试二Adsorption performance test two
有机磷负载羟基铝复合材料对Cd2+的pH吸附实验,测试吸附剂在25℃、pH4~8的条件下对Cd2+吸附的影响。The pH adsorption experiment of organophosphorus-supported hydroxyl aluminum composite materials on Cd 2+ was tested to test the effect of adsorbent on the adsorption of Cd 2+ under the conditions of 25°C and pH 4-8.
该实验均在50mL离心管中进行。配制一系列Cd2+浓度为20mg/L的溶液,选高浓度有机磷负载羟基铝复合材料(AAH-OP_high)为吸附剂,吸附剂投加量为1.0g/L,加入0.1mol/L的KNO3溶液定容至30mL,使用1mol/L NaOH、1mol/L HCl调节溶液pH,用恒温振荡机在25℃恒温下振荡24h,然后离心15min。离心管中的上清液用0.45μm尼龙膜过滤,然后用ICP(电感耦合等离子体质谱)分析上清液中残余Cd2+浓度。All experiments were carried out in 50mL centrifuge tubes. A series of solutions with a Cd 2+ concentration of 20 mg/L were prepared, and a high-concentration organophosphorus-supported aluminum hydroxy composite material (AAH-OP_high) was selected as the adsorbent. The dosage of the adsorbent was 1.0 g/L, and 0.1 mol/L of The volume of KNO 3 solution was adjusted to 30 mL, and the pH of the solution was adjusted with 1 mol/L NaOH and 1 mol/L HCl, shaken at a constant temperature of 25 °C for 24 h with a constant temperature shaker, and then centrifuged for 15 min. The supernatant in the centrifuge tube was filtered with a 0.45 μm nylon membrane, and then the residual Cd 2+ concentration in the supernatant was analyzed by ICP (inductively coupled plasma mass spectrometry).
根据图8复合材料在pH 4~8的范围内对Cd2+的吸附量均随pH的升高而升高,由图可以发现在中性至碱性环境下,复合材料对Cd2+具备优异的吸附性能。According to Figure 8, the adsorption capacity of the composite material to Cd 2+ increases with the increase of pH in the range of pH 4-8. From the figure, it can be found that the composite material has the ability to adsorb Cd 2+ in a neutral to alkaline environment. Excellent adsorption properties.
对比案例1Comparative case 1
氢氧化铝与细菌的复合体对镉的pH吸附pH Adsorption of Cadmium by the Complex of Aluminum Hydroxide and Bacteria
用Cd(NO3)3·4H2O制备镉母液,反应体系中Cd2+浓度为0.1mM,吸附剂(无定形氢氧化铝、不同比例的氢氧化铝-细菌复合体)浓度为1g/L,用0.1mol/L的KNO3溶液定容至30mL,对照组不添加吸附剂。使用1mol/L NaOH、1mol/L HNO3调整悬浮液的pH 4~7,用恒温振荡机在25℃恒温下振荡24h待吸附平衡,然后离心。上清液用0.45μm尼龙膜过滤,原子吸收光谱法分析上清液中残余Cd2+浓度。Use Cd(NO 3 ) 3 4H 2 O to prepare cadmium mother liquor, the concentration of Cd 2+ in the reaction system is 0.1mM, and the concentration of adsorbent (amorphous aluminum hydroxide, aluminum hydroxide-bacteria complex in different proportions) is 1g/ L, with 0.1mol/L KNO3 solution to make the volume to 30mL, no adsorbent was added to the control group. Use 1 mol/L NaOH, 1 mol/L HNO 3 to adjust the pH of the suspension to 4-7, shake it at a constant temperature of 25°C for 24 hours with a constant temperature shaker to allow adsorption to balance, and then centrifuge. The supernatant was filtered with a 0.45 μm nylon membrane, and the concentration of residual Cd 2+ in the supernatant was analyzed by atomic absorption spectrometry.
各吸附剂对Cd2+的吸附量均随着pH的升高而升高,在pH小于6时,复合体的对Cd2+的吸附性能优于纯氢氧化铝,在pH 6~7,细菌对氢氧化铝材料的改性未显著提高氢氧化铝材料的吸附性能,吸附量约为7.9mg/g。The adsorption capacity of each adsorbent for Cd 2+ increases with the increase of pH. When the pH is less than 6, the adsorption performance of the complex for Cd 2+ is better than that of pure aluminum hydroxide. At pH 6-7, The modification of aluminum hydroxide material by bacteria did not significantly improve the adsorption performance of aluminum hydroxide material, and the adsorption capacity was about 7.9mg/g.
对比案例2Comparative case 2
氢氧化铝-聚丙烯酰胺对Cd2+的吸附等温线Adsorption Isotherm of Aluminum Hydroxide-Polyacrylamide for Cd 2+
镉储备液(1.000g/L),将220mg氢氧化铝-聚丙烯酰胺溶液加入盛有400mL镉溶液的锥形瓶中,将锥形瓶置于旋转摇床中反应4h,摇床转速为180r/min。然后将溶液离心分离,取上清液采用原子吸收分光光度计测量Cd2+浓度。For cadmium stock solution (1.000g/L), add 220mg of aluminum hydroxide-polyacrylamide solution into an Erlenmeyer flask filled with 400mL of cadmium solution, place the Erlenmeyer flask in a rotary shaker for 4 hours, and the shaker speed is 180r /min. Then the solution was centrifuged, and the supernatant was taken to measure the Cd 2+ concentration by an atomic absorption spectrophotometer.
在研究的温度范围内,Langmuir等温吸附模型更加符合氢氧化铝-聚丙烯酰胺对Cd2+的吸附等温线数据。这表明Cd2+在氢氧化铝-聚丙烯酰胺表面形成单层吸附层。在温度为10℃、30℃和50℃条件下,氢氧化铝-聚丙烯酰胺对Cd2+的最大吸附量qmax的值分别是44.43mg/g、50.11mg/g和54.81mg/g。In the studied temperature range, the Langmuir isotherm adsorption model is more consistent with the adsorption isotherm data of aluminum hydroxide-polyacrylamide on Cd 2+ . This indicates that Cd 2+ forms a monolayer adsorption layer on the surface of aluminum hydroxide-polyacrylamide. At 10°C, 30°C, and 50°C, the maximum adsorption capacity q max of aluminum hydroxide-polyacrylamide to Cd 2+ is 44.43mg/g, 50.11mg/g, and 54.81mg/g, respectively.
对比案例3Comparative case 3
植酸海泡石复合重金属吸附剂对Cd2+的吸附研究Adsorption of Cd 2+ by Phytic Acid Sepiolite Composite Heavy Metal Adsorbent
以植酸与海泡石为原料,制备出植酸海泡石复合吸附材料,温度为30℃,吸附剂浓度18g/L,Cd2+浓度100mg/L,调节pH 1~6,进行pH吸附实验;温度为30℃,吸附剂浓度18g/L,pH 3.8处理不同镉浓度的溶液探讨重金属浓度对吸附性能的影响;Using phytic acid and sepiolite as raw materials, a phytic acid-sepiolite composite adsorption material was prepared. The temperature was 30°C, the concentration of the adsorbent was 18g/L, the concentration of Cd 2+ was 100mg/L, and the pH was adjusted from 1 to 6 for pH adsorption. Experiment; the temperature is 30°C, the adsorbent concentration is 18g/L, and the pH is 3.8 to treat solutions with different cadmium concentrations to explore the influence of heavy metal concentration on adsorption performance;
研究结果表明植酸海泡石复合重金属吸附剂在30℃,吸附剂浓度为18g/L时,在pH=3.8具备最佳吸附性能,最大吸附量为2.67mg/g。The research results show that the phytic acid sepiolite composite heavy metal adsorbent has the best adsorption performance at pH=3.8 when the adsorbent concentration is 18g/L at 30°C, and the maximum adsorption capacity is 2.67mg/g.
由性能测试及对比案例可以发现有机磷负载羟基铝对Cd2+具有很好的吸附效果,均高于现有技术正常吸附量(~50mg/g),高浓度有机磷的添加可以显著增强吸附性能,对Cd2+的最大吸附量可达205mg/g以上,超过现有技术正常吸附量的四倍。本发明制备简单,成本低,吸附量较其它发明较高,具有较高的工农业推广价值。From performance tests and comparison cases, it can be found that organophosphorus-supported hydroxyaluminum has a good adsorption effect on Cd 2+ , which is higher than the normal adsorption capacity (~50mg/g) of the existing technology. The addition of high-concentration organophosphorus can significantly enhance the adsorption Performance, the maximum adsorption capacity of Cd 2+ can reach more than 205mg/g, more than four times the normal adsorption capacity of the existing technology. The invention has the advantages of simple preparation, low cost, higher adsorption capacity than other inventions, and high industrial and agricultural popularization value.
以上所述,仅是本申请的较佳实施例,并非对本申请做任何形式的限制,虽然本申请以较佳实施例揭示如上,然而并非用以限制本申请,任何熟悉本专业的技术人员,在不脱离本申请技术方案的范围内,利用上述揭示的技术内容做出些许的变动或修饰均等同于等效实施案例,均属于技术方案范围内。The above is only a preferred embodiment of the application, and does not limit the application in any form. Although the application is disclosed as above with the preferred embodiment, it is not intended to limit the application. Any skilled person familiar with this field, Without departing from the scope of the technical solution of the present application, any changes or modifications made using the technical content disclosed above are equivalent to equivalent implementation cases, and all belong to the scope of the technical solution.
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