WO2016187796A1 - Preparation method and use of heavy metal ion adsorbent - Google Patents

Preparation method and use of heavy metal ion adsorbent Download PDF

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WO2016187796A1
WO2016187796A1 PCT/CN2015/079757 CN2015079757W WO2016187796A1 WO 2016187796 A1 WO2016187796 A1 WO 2016187796A1 CN 2015079757 W CN2015079757 W CN 2015079757W WO 2016187796 A1 WO2016187796 A1 WO 2016187796A1
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heavy metal
metal ion
sodium alginate
reaction
ion adsorbent
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PCT/CN2015/079757
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French (fr)
Chinese (zh)
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倪才华
张丽萍
朱昌平
田贞乐
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江南大学
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/24Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/58Treatment of water, waste water, or sewage by removing specified dissolved compounds
    • C02F1/62Heavy metal compounds

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  • the invention relates to the technical field of polymer material modification, in particular to a preparation method of heavy metal ion adsorbent and application thereof.
  • Sodium alginate is a natural polymer composed of a linear copolymer of mannose and gulose, and is widely found in various brown seaweeds.
  • Sodium alginate has a very unique property, soluble in water and with many divalent metal cations in water such as: Pb 2+ , Cu 2+ , Hg 2+ , Cd 2+ , Co 2+ , Ni 2+ , Zn 2+ , Mn 2+ , Sr 2+ , Ba 2+ , and Ca 2+ react to form a gel which precipitates from water.
  • the mechanism is that the hydroxyl group in the molecular structural unit of sodium alginate acts synergistically with the carboxyl group to form a chelate structure like the "egg shell" with the metal ion. Even for very dilute concentrations of metal ions, such reactions can occur, which are not found in other natural polymeric flocculants and synthetic flocculants.
  • an object of the present invention is to provide a method for preparing a heavy metal ion adsorbent and an application thereof, and to modify a sodium alginate to introduce a chelating group having a strong adsorption capacity for heavy metal ions in a molecule. Further enhance the adsorption of heavy metal ions and improve the efficiency of removing heavy metal ions.
  • the preparation method of the heavy metal ion adsorbent proposed by the invention comprises the following steps:
  • the aldehyde-based sodium alginate is formulated into an aqueous solution, and the reaction with polyethene polyamine is added, followed by reduction with sodium borohydride, and the reaction is continued to obtain amino sodium alginate;
  • the mass percentage of the aldehyde-based sodium alginate in the aqueous solution is 5.8%.
  • polyethene polyamine includes any one or more of ethylenediamine, diethylenetriamine, triethylenetetramine, and tetraethylenepentamine.
  • the mass of the polyethene polyamine is 1-3 times the mass of the oxidized sodium alginate, and the mass of the sodium borohydride is 60% of the mass of the aldehyde-based alginate.
  • the reaction temperature of the aldehyde-based sodium alginate and the polyethene polyamine is 40 ° C, and the reaction time is 24 h.
  • a mixed solution of carbon disulfide and sodium hydroxide is formed by mixing an equal volume of carbon disulfide with a 30% by mass aqueous sodium hydroxide solution, and the mass ratio of the amino alginate to the carbon disulfide is 1. : 0.8 to 1.2.
  • the alcohol solvent comprises any one or more of methanol, absolute ethanol, and isopropanol in an amount of three times the volume of the reactant solution.
  • reaction temperature in the step (2) is 40 °C.
  • the preparation process of the aldehyde-based sodium alginate in the step (1) comprises the steps of dispersing sodium alginate in anhydrous ethanol, preparing a dispersion having a mass percentage of 15 to 20%, and then adding 0.8 mol / L sodium periodate aqueous solution, sodium periodate and sodium alginate mass ratio of 1:0.4 ⁇ 1, after the light-proof reaction, add ethylene glycol to terminate the reaction, the quality of ethylene glycol is sodium alginate 22.5% of the aldehyde-based sodium alginate was obtained after washing and drying.
  • the invention also provides an application of a heavy metal ion adsorbent for treating industrial sewage containing heavy metal ions and adsorbing heavy metal ions in the sewage.
  • the present invention has at least the following advantages: the raw material used in the present invention is derived from the natural product ammonium alginate, which is inexpensive and has few modification steps; the modified sodium alginate has a functional amino group and a thiocarboxylate group. Group, these two groups have strong capture ability for heavy metal ions, large adsorption capacity, high removal rate, high speed, and improved adsorption efficiency.
  • Fig. 1 is an infrared spectrum diagram of OSA-NH 4 -CS-1 in the first embodiment of the present invention.
  • a mixed solution of CS 2 and NaOH is added, and the mixed solution is prepared by mixing 4 g of CS 2 and 5 mL of 30% NaOH solution, and the reaction temperature is 40 ° C, and the reaction is continued until there is no CS 2 droplet in the solution. .
  • the reaction was stopped, ethanol was added in an amount of 3 times the volume of the reactant solution, and the mixture was allowed to stand overnight.
  • the precipitate obtained by bottom chromatography was dried in an oven at 50 ° C for 24 hours to obtain a heavy metal ion adsorbent.
  • the product mass was 6.64 g, and it was named OSA-NH 4 . -CS-1.
  • Fig. 1 is an infrared analysis spectrum of the above heavy metal ion adsorbent.
  • the absorption peak at a wavenumber of 3350 cm -1 is a NH stretching vibration of an amino group in a polyethene polyamine; the absorption peak at 1601 cm -1 and 1422 cm -1 is thio
  • the characteristic peak of the carboxylic acid and the infrared spectrum confirmed the successful synthesis of the modified sodium alginate.
  • a mixed solution of CS 2 and NaOH is added, and the mixed solution is thoroughly stirred by mixing 6 g of CS 2 and 7.5 mL of a 30% NaOH solution, and the reaction temperature is 40 ° C, and the reaction is continued until there is no CS 2 liquid in the solution. drop.
  • the reaction was stopped, methanol was added in an amount of 3 times the volume of the reactant, and the mixture was allowed to stand overnight.
  • the precipitate obtained by bottom chromatography was dried in an oven at 50 ° C for 24 hours to obtain a heavy metal ion adsorbent.
  • the product mass was 5.21 g and was named OSA-NH 4 - CS-2.
  • a mixed solution of CS 2 and NaOH is added, and the mixed solution is prepared by mixing 5 g of CS 2 and 6.25 mL of 30% NaOH solution, and the reaction temperature is 40 ° C, and the reaction is continued until there is no CS 2 liquid in the solution. drop.
  • the reaction was stopped, isopropanol was added in an amount of 3 times the volume of the reactant solution, and the mixture was allowed to stand overnight.
  • the precipitate obtained by bottom chromatography was dried in an oven at 50 ° C for 24 hours to obtain a heavy metal ion adsorbent, and the product mass was 7.56 g, which was named OSA- NH 4 -CS-3.
  • the heavy metal ions commonly found in the sewage are adsorbed, and the adsorption capacity and adsorption conditions of the adsorbent are investigated.
  • OSA-NH 4 -CS-1, adsorbent reference sample and sodium alginate were used to adsorb Pb 2+ , and 1.0 g of the above three adsorbents were respectively taken and disposed as an aqueous solution of 1% by mass, respectively.
  • 5 mL, 10 mL, 15 mL, and 20 mL of the aqueous solution were added to 50 mL of a 5 mmol/L Pb(NO 3 ) 2 solution, shaken for 20 min (120 r/min), centrifuged for 15 min (4000 r/min), and 10 mL of the supernatant was taken.
  • OSA-NH 4 -CS-1 and sodium alginate were used to adsorb Cd 2+ , and Cd(NO 3 ) 2 was used instead of Pb(NO 3 ) 2 .
  • the procedure was the same as the step of adsorbing Pb 2+ , and the adsorbent was measured.
  • the adsorption performance of Cd 2+ it can be seen from Table 3 that compared with sodium alginate, the adsorption performance of OSA-NH 4 -CS-1 on Cd 2+ in solution is greatly improved.
  • Pb(NO 3 ) 2 solutions with concentrations of 5.0, 10.0, 20.0, 40.0, 50.0 (mmol/L) were prepared, each taking 50 mL, and 10 mL of OSA-NH 4 -CS-1 solution (1%, w/w) was added.
  • the saturated adsorption capacity of OSA-NH 4 -CS-1 is higher than that of SA, indicating that the adsorption performance of the modified adsorbent is better than that of sodium alginate.
  • the metal ion removal rate is low, the Pb 2+ concentration is lower. The effect is better.
  • the pH of the solution is very important for the adsorption effect.
  • the pH of the solution is adjusted, and the removal rate and adsorption capacity of the adsorbent for Pb 2+ ions are measured.
  • the results are shown in Table 5. As can be seen from the table, the adsorption performance of the adsorbent did not differ much between pH 5-6.
  • the present invention prepares a heavy metal ion adsorbent by modifying sodium alginate.
  • the source of sodium alginate is abundant, the price is cheap, the modification step is small, the product is convenient to use, and the post-treatment is easy, no secondary Contaminated, environmentally friendly;
  • the adsorbent has a large number of amino groups, thiocarboxylates and other groups, these two groups have strong capture ability for heavy metals, large adsorption capacity, high removal rate, fast speed, plus
  • the carboxyl group in the sodium alginate structure of Shanghai has synergistic effects to form a chelate with heavy metal ions.
  • the heavy metal ion adsorbent has higher adsorption capacity, larger adsorption capacity, and wider pH range than the existing sodium alginate, so it is suitable for a wide range of applications.

Abstract

The present invention relates to the technical field of high-molecular material modification, and especially relates to a preparation method and a use of a heavy metal ion adsorbent. The preparation method for the adsorbent comprises the following steps: (1) formulating an aqueous solution of aldehyde group sodium alginate, adding a polyethylene polyamine for reaction, then adding sodium borohydride for reduction, and continuing the reaction so as to obtain amino sodium alginate; and (2) adding a mixed solution of carbon disulfide and sodium hydroxide to the solution obtained after the reaction in step (1), continuing the reaction until carbon disulfide droplets in the solution have disappeared, stopping the reaction, adding an alcohol solvent for precipitating a product, standing and layering, separating the precipitate precipitated at the bottom layer, and drying same so as to obtain the heavy metal ion adsorbent. The adsorbent has a strong adsorptivity to heavy metal ions, and desorption efficiency is improved.

Description

一种重金属离子吸附剂的制备方法及其应用Preparation method of heavy metal ion adsorbent and application thereof
本申请要求了申请日为2015年05月22日,申请号为201510262299.2,发明名称为“一种重金属离子吸附剂的制备方法及其应用”的中国专利申请的优先权,其全部内容通过引用结合在本申请中。The present application claims priority from Chinese Patent Application No. 201510262299.2, entitled "Preparation of a Heavy Metal Ion Adsorbent and Its Application", the entire contents of which are incorporated by reference. In this application.
技术领域Technical field
本发明涉及高分子材料改性技术领域,尤其涉及一种重金属离子吸附剂的制备方法及其应用。The invention relates to the technical field of polymer material modification, in particular to a preparation method of heavy metal ion adsorbent and application thereof.
背景技术Background technique
在水里的多种污染物中,重金属离子的危害最大。现代医学研究表明,一些重金属离子进入人体会使人致癌、致畸、致染色体突变,潜伏期可达数十年。我国有上万家电镀企业,废水中重金属离子产出量巨大,重金属离子污染事件在我国时有发生,还有很多企业对重金属离子治理不力,超标排放,因此存在巨大的环境破坏隐患。Of the many pollutants in the water, heavy metal ions are the most harmful. Modern medical research has shown that some heavy metal ions can cause cancer, teratogenicity and chromosomal mutations in humans, and the incubation period can reach several decades. There are tens of thousands of electroplating enterprises in China. The output of heavy metal ions in wastewater is huge. The incident of heavy metal ion pollution has occurred in China. Many enterprises have weak treatment of heavy metal ions and exceeded the standards. Therefore, there are huge hidden dangers of environmental damage.
目前治理重金属离子废水用的方法包括离子交换法、膜分离法、电化学法、化学法以及生物法。这些方法虽然能够不同程度地脱除重金属离子,但是却各有利弊。其主要问题是设备复杂,运行成本高。化学法药剂费高、一级排放达标困难,废物难处理,造成二次污染。使用金属絮凝剂来吸附重金属离子,该方法简单有效,处理的效果比较理想,有机纳米絮凝剂的絮凝效果比传统的无机盐类絮凝剂大十几甚至几十倍,具有使用简便、沉降速度快、用量少、处理成本低、效率高、等优点。Current methods for treating heavy metal ion wastewater include ion exchange, membrane separation, electrochemical, chemical, and biological methods. Although these methods can remove heavy metal ions to varying degrees, they have their own advantages and disadvantages. The main problem is that the equipment is complicated and the running cost is high. The chemical law has high drug costs, the first-level discharge is difficult to meet the standard, and the waste is difficult to handle, causing secondary pollution. The use of metal flocculant to adsorb heavy metal ions is simple and effective, and the treatment effect is ideal. The flocculation effect of organic nanoflocculant is ten or even dozens larger than that of traditional inorganic salt flocculant, and it has the advantages of simple use and fast sedimentation speed. , low dosage, low processing cost, high efficiency, and so on.
海藻酸钠是一种由甘露糖酸盐和古罗糖酸盐连接而成的线性共聚物组成的天然高分子,广泛存在于各类棕色海藻中。海藻酸钠具有一种非常独特的性能,能够溶于水并与水中多数二价金属阳离子如:Pb2+、 Cu2+、Hg2+、Cd2+、Co2+、Ni2+、Zn2+、Mn2+、Sr2+、Ba2+、Ca2+发生反应生成凝胶,从水中析出。其机理是海藻酸钠分子结构单元中的羟基与羧基协同作用,与金属离子形成象“鸡蛋壳”一样的螯合结构。即使对于很稀浓度的金属离子,此类反应也可以发生,这种特性是其他天然高分子絮凝剂以及合成絮凝剂所不具有的。Sodium alginate is a natural polymer composed of a linear copolymer of mannose and gulose, and is widely found in various brown seaweeds. Sodium alginate has a very unique property, soluble in water and with many divalent metal cations in water such as: Pb 2+ , Cu 2+ , Hg 2+ , Cd 2+ , Co 2+ , Ni 2+ , Zn 2+ , Mn 2+ , Sr 2+ , Ba 2+ , and Ca 2+ react to form a gel which precipitates from water. The mechanism is that the hydroxyl group in the molecular structural unit of sodium alginate acts synergistically with the carboxyl group to form a chelate structure like the "egg shell" with the metal ion. Even for very dilute concentrations of metal ions, such reactions can occur, which are not found in other natural polymeric flocculants and synthetic flocculants.
为了提高海藻酸钠的吸附性能,需要对其进行结构改性,以最大程度的提高其吸附重金属离子的性能,提高其处理污水废水的能力。In order to improve the adsorption performance of sodium alginate, it needs to be structurally modified to maximize the adsorption of heavy metal ions and improve its ability to treat wastewater.
发明内容Summary of the invention
为解决上述技术问题,本发明的目的是提供一种重金属离子吸附剂的制备方法及其应用,发明对海藻酸钠进行改性,在分子中引入对重金属离子吸附能力强的螯合基团,进一步增强对重金属离子的吸附作用,提高去除重金属离子的效率。In order to solve the above technical problems, an object of the present invention is to provide a method for preparing a heavy metal ion adsorbent and an application thereof, and to modify a sodium alginate to introduce a chelating group having a strong adsorption capacity for heavy metal ions in a molecule. Further enhance the adsorption of heavy metal ions and improve the efficiency of removing heavy metal ions.
本发明提出的一种重金属离子吸附剂的制备方法,包括以下步骤:The preparation method of the heavy metal ion adsorbent proposed by the invention comprises the following steps:
(1)将醛基海藻酸钠配成水溶液,加入多乙烯多胺反应,然后加入硼氢化钠还原,继续反应,得到氨基海藻酸钠;(1) The aldehyde-based sodium alginate is formulated into an aqueous solution, and the reaction with polyethene polyamine is added, followed by reduction with sodium borohydride, and the reaction is continued to obtain amino sodium alginate;
(2)在所述步骤(1)中反应后的溶液中加入二硫化碳与氢氧化钠的混合溶液,继续反应至溶液中二硫化碳液滴消失,停止反应,加入醇类溶剂使产物沉淀,静置,分层,分离底层析出的沉淀,干燥后,得到重金属离子吸附剂。(2) adding a mixed solution of carbon disulfide and sodium hydroxide to the solution in the step (1), continuing the reaction until the carbon disulfide droplets disappear in the solution, stopping the reaction, adding an alcohol solvent to precipitate the product, and allowing to stand. The layers were separated, and the precipitate obtained by the bottom chromatography was separated, and after drying, a heavy metal ion adsorbent was obtained.
进一步的,所述步骤(1)中,醛基海藻酸钠在水溶液中的质量百分含量为5.8%。Further, in the step (1), the mass percentage of the aldehyde-based sodium alginate in the aqueous solution is 5.8%.
进一步的,所述多乙烯多胺包括乙二胺、二乙烯三胺、三乙烯四胺、四乙烯五胺中的任意一种或多种。Further, the polyethene polyamine includes any one or more of ethylenediamine, diethylenetriamine, triethylenetetramine, and tetraethylenepentamine.
进一步的,所述步骤(1)中,所述多乙烯多胺的质量是氧化海藻酸钠质量的1~3倍,所述硼氢化钠的质量是醛基海藻酸钠质量的60%。 Further, in the step (1), the mass of the polyethene polyamine is 1-3 times the mass of the oxidized sodium alginate, and the mass of the sodium borohydride is 60% of the mass of the aldehyde-based alginate.
进一步的,所述步骤(1)中,醛基海藻酸钠与多乙烯多胺的反应温度为40℃,反应时间为24h。Further, in the step (1), the reaction temperature of the aldehyde-based sodium alginate and the polyethene polyamine is 40 ° C, and the reaction time is 24 h.
进一步的,所述步骤(2)中,二硫化碳与氢氧化钠的混合溶液由等体积的二硫化碳与质量百分含量为30%的氢氧化钠水溶液混合形成,氨基海藻酸钠与二硫化碳质量比为1∶0.8~1.2。Further, in the step (2), a mixed solution of carbon disulfide and sodium hydroxide is formed by mixing an equal volume of carbon disulfide with a 30% by mass aqueous sodium hydroxide solution, and the mass ratio of the amino alginate to the carbon disulfide is 1. : 0.8 to 1.2.
进一步的,所述步骤(2)中,所述醇类溶剂包括甲醇、无水乙醇、异丙醇中的任意一种或多种,用量为反应物溶液体积的3倍。Further, in the step (2), the alcohol solvent comprises any one or more of methanol, absolute ethanol, and isopropanol in an amount of three times the volume of the reactant solution.
进一步的,所述步骤(2)中反应温度为40℃。Further, the reaction temperature in the step (2) is 40 °C.
进一步的,所述步骤(1)中醛基海藻酸钠的制备过程包括以下步骤:将海藻酸钠分散在无水乙醇中,配成质量百分含量为15~20%的分散液,然后加入0.8mol/L的高碘酸钠水溶液,高碘酸钠与海藻酸钠的质量比为1∶0.4~1,避光反应后,加入乙二醇终止反应,乙二醇的质量为海藻酸钠的22.5%,洗涤、烘干后得到醛基海藻酸钠。Further, the preparation process of the aldehyde-based sodium alginate in the step (1) comprises the steps of dispersing sodium alginate in anhydrous ethanol, preparing a dispersion having a mass percentage of 15 to 20%, and then adding 0.8 mol / L sodium periodate aqueous solution, sodium periodate and sodium alginate mass ratio of 1:0.4 ~ 1, after the light-proof reaction, add ethylene glycol to terminate the reaction, the quality of ethylene glycol is sodium alginate 22.5% of the aldehyde-based sodium alginate was obtained after washing and drying.
本发明还提供一种重金属离子吸附剂的应用,将所述的重金属离子吸附剂用于含有重金属离子的工业污水的处理,吸附污水中的重金属离子。The invention also provides an application of a heavy metal ion adsorbent for treating industrial sewage containing heavy metal ions and adsorbing heavy metal ions in the sewage.
借由上述方案,本发明至少具有以下优点:本发明使用的原料来自天然产物海藻酸铵,价格便宜,改性步骤少;改性后的海藻酸钠带有功能性氨基和硫代羧酸根基团,这两类基团对于重金属离子的捕捉能力极强,吸附容量大、脱除率高、速度快,提高了吸附效率。By the above scheme, the present invention has at least the following advantages: the raw material used in the present invention is derived from the natural product ammonium alginate, which is inexpensive and has few modification steps; the modified sodium alginate has a functional amino group and a thiocarboxylate group. Group, these two groups have strong capture ability for heavy metal ions, large adsorption capacity, high removal rate, high speed, and improved adsorption efficiency.
上述说明仅是本发明技术方案的概述,为了能够更清楚了解本发明的技术手段,并可依照说明书的内容予以实施,以下以本发明的较佳实施例并配合附图详细说明如后。The above description is only an overview of the technical solutions of the present invention, and the technical means of the present invention can be more clearly understood and can be implemented in accordance with the contents of the specification. Hereinafter, the preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.
附图说明DRAWINGS
此处所说明的附图用来提供对本发明的进一步理解,构成本申请 的一部分,本发明的示意性实施例及其说明用于解释本发明,并不构成对本发明的不当限定。在附图中:The drawings described herein are provided to provide a further understanding of the invention and constitute the application. In part, the illustrative embodiments of the invention and the description thereof are intended to be illustrative of the invention and are not intended to limit the invention. In the drawing:
图1是本发明实施例一中OSA-NH4-CS-1的红外谱图。BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is an infrared spectrum diagram of OSA-NH 4 -CS-1 in the first embodiment of the present invention.
具体实施方式detailed description
下面将参考附图并结合实施例,来详细说明本发明。The invention will be described in detail below with reference to the drawings in conjunction with the embodiments.
实施例1Example 1
吸附剂OSA-NH4-CS-1的制备Preparation of adsorbent OSA-NH 4 -CS-1
用100mL无水乙醇加入到20g海藻酸钠(SA)粉末中,磁力搅拌分散均匀,加入100mL浓度为0.8mol/L的高碘酸钠(NaIO4)溶液,室温避光反应12h,加入4.5mL乙二醇,继续反应2h。对溶液进行抽滤,将产物用50%的乙醇充分搅拌清洗,抽滤,重复两次。得到的产物在55℃烘箱中干燥24h,得到醛基海藻酸钠(OSA)。Add 100 mL of absolute ethanol to 20 g of sodium alginate (SA) powder, stir evenly with magnetic stirring, add 100 mL of sodium periodate (NaIO 4 ) solution with a concentration of 0.8 mol/L, and react at room temperature for 12 h in the dark, add 4.5 mL. Ethylene glycol, continue to react for 2h. The solution was suction filtered, and the product was washed thoroughly with 50% ethanol, suction filtered, and twice. The obtained product was dried in an oven at 55 ° C for 24 h to give an aldehyde-based sodium alginate (OSA).
取5g OSA于80mL水中配成均匀溶液,加入80mL浓度为1mol/L的四乙烯五胺水溶液,于40℃水浴中磁力搅拌反应24h后,冷却至室温。分批加入3.02g NaBH4,继续反应24h,得到氨基海藻酸钠。5 g of OSA was mixed into 80 mL of water to form a homogeneous solution, 80 mL of a 1 mol/L tetraethylenepentamine aqueous solution was added, and the reaction was magnetically stirred in a 40 ° C water bath for 24 hours, and then cooled to room temperature. 3.02 g of NaBH 4 was added in portions, and the reaction was continued for 24 hours to obtain amino sodium alginate.
在上述反应后的溶液中,加入CS2与NaOH混合溶液,混合溶液由4g CS2与5mL 30%NaOH溶液混合充分搅拌而成,反应温度为40℃,继续反应至溶液中没有CS2液滴。停止反应,按反应物溶液体积3倍的量加入乙醇,静置过夜,取底层析出的沉淀,50℃烘箱中干燥24h即得重金属离子吸附剂,产物质量为6.64g,命名为OSA-NH4-CS-1。In the solution after the above reaction, a mixed solution of CS 2 and NaOH is added, and the mixed solution is prepared by mixing 4 g of CS 2 and 5 mL of 30% NaOH solution, and the reaction temperature is 40 ° C, and the reaction is continued until there is no CS 2 droplet in the solution. . The reaction was stopped, ethanol was added in an amount of 3 times the volume of the reactant solution, and the mixture was allowed to stand overnight. The precipitate obtained by bottom chromatography was dried in an oven at 50 ° C for 24 hours to obtain a heavy metal ion adsorbent. The product mass was 6.64 g, and it was named OSA-NH 4 . -CS-1.
图1为上述重金属离子吸附剂的红外分析谱图,在波数为3350cm-1处的吸收峰是多乙烯多胺中氨基的N-H伸缩振动;在1601cm-1和 1422cm-1的吸收峰是硫代羧酸的特征峰,红外光谱图证实了改性海藻酸钠的成功合成。Fig. 1 is an infrared analysis spectrum of the above heavy metal ion adsorbent. The absorption peak at a wavenumber of 3350 cm -1 is a NH stretching vibration of an amino group in a polyethene polyamine; the absorption peak at 1601 cm -1 and 1422 cm -1 is thio The characteristic peak of the carboxylic acid and the infrared spectrum confirmed the successful synthesis of the modified sodium alginate.
化学反应方程式如下所示。The chemical reaction equation is as follows.
Figure PCTCN2015079757-appb-000001
Figure PCTCN2015079757-appb-000001
实施例2Example 2
吸附剂OSA-NH4-CS-2的制备Preparation of adsorbent OSA-NH 4 -CS-2
用100mL无水乙醇加入到18g海藻酸钠(SA)粉末中,磁力搅 拌分散均匀,加入263mL浓度为0.8mol/L的高碘酸钠(NaIO4)溶液,室温避光反应12h,加入4.1mL乙二醇,继续反应2h。对溶液进行抽滤,将产物用50%的乙醇充分搅拌清洗,抽滤,重复两次。得到的产物在55℃烘箱中干燥24h,得到醛基海藻酸钠(OSA)。100 mL of absolute ethanol was added to 18 g of sodium alginate (SA) powder, and the mixture was uniformly dispersed by magnetic stirring. 263 mL of a sodium periodate (NaIO 4 ) solution having a concentration of 0.8 mol/L was added, and the reaction was carried out at room temperature for 12 hours in the dark, and 4.1 mL was added. Ethylene glycol, continue to react for 2h. The solution was suction filtered, and the product was washed thoroughly with 50% ethanol, suction filtered, and twice. The obtained product was dried in an oven at 55 ° C for 24 h to give an aldehyde-based sodium alginate (OSA).
取5g OSA于80mL水中配成均匀溶液,加入34mL浓度为1mol/L的三乙烯四胺水溶液,于40℃水浴中磁力搅拌反应24h后,冷却至室温。分批加入3.02g NaBH4,继续反应24h,得到氨基海藻酸钠。5 g of OSA was mixed into 80 mL of water to form a homogeneous solution. 34 mL of a 1 mol/L aqueous solution of triethylenetetramine was added, and the reaction was magnetically stirred in a 40 ° C water bath for 24 hours, and then cooled to room temperature. 3.02 g of NaBH 4 was added in portions, and the reaction was continued for 24 hours to obtain amino sodium alginate.
在上述反应后的溶液中,加入CS2与NaOH混合溶液,混合溶液由6g CS2与7.5mL 30%NaOH溶液混合充分搅拌而成,反应温度为40℃,继续反应至溶液中没有CS2液滴。停止反应,按反应物体积3倍的量加入甲醇,静置过夜,取底层析出的沉淀,50℃烘箱中干燥24h即得重金属离子吸附剂,产物质量为5.21g,命名为OSA-NH4-CS-2。In the solution after the above reaction, a mixed solution of CS 2 and NaOH is added, and the mixed solution is thoroughly stirred by mixing 6 g of CS 2 and 7.5 mL of a 30% NaOH solution, and the reaction temperature is 40 ° C, and the reaction is continued until there is no CS 2 liquid in the solution. drop. The reaction was stopped, methanol was added in an amount of 3 times the volume of the reactant, and the mixture was allowed to stand overnight. The precipitate obtained by bottom chromatography was dried in an oven at 50 ° C for 24 hours to obtain a heavy metal ion adsorbent. The product mass was 5.21 g and was named OSA-NH 4 - CS-2.
实施例3Example 3
吸附剂OSA-NH4-CS-3的制备Preparation of adsorbent OSA-NH 4 -CS-3
用100mL无水乙醇加入到25g海藻酸钠(SA)粉末中,磁力搅拌分散均匀,加入183mL浓度为0.8mol/L的高碘酸钠(NaIO4)溶液,室温避光反应12h,加入5.6mL乙二醇,继续反应2h。对溶液进行抽滤,将产物用50%的乙醇充分搅拌清洗,抽滤,重复两次。得到的产物在55℃烘箱中干燥24h,得到醛基海藻酸钠(OSA)。Add 100 mL of absolute ethanol to 25 g of sodium alginate (SA) powder, stir evenly under magnetic stirring, add 183 mL of sodium periodate (NaIO 4 ) solution with a concentration of 0.8 mol/L, and react at room temperature for 12 h in the dark, add 5.6 mL. Ethylene glycol, continue to react for 2h. The solution was suction filtered, and the product was washed thoroughly with 50% ethanol, suction filtered, and twice. The obtained product was dried in an oven at 55 ° C for 24 h to give an aldehyde-based sodium alginate (OSA).
取5g OSA于80mL水中配成均匀溶液,加入53mL浓度为1mol/L的四乙烯五胺水溶液,于40℃水浴中磁力搅拌反应24h后,冷却至室 温。分批加入3.02g NaBH4,继续反应24h,得到氨基海藻酸钠。5 g of OSA was mixed into 80 mL of water to form a homogeneous solution. 53 mL of a 1 mol/L tetraethylenepentamine aqueous solution was added, and the reaction was magnetically stirred in a 40 ° C water bath for 24 hours, and then cooled to room temperature. 3.02 g of NaBH 4 was added in portions, and the reaction was continued for 24 hours to obtain amino sodium alginate.
在上述反应后的溶液中,加入CS2与NaOH混合溶液,混合溶液由5g CS2与6.25mL 30%NaOH溶液混合充分搅拌而成,反应温度为40℃,继续反应至溶液中没有CS2液滴。停止反应,按反应物溶液体积3倍的量加入异丙醇,静置过夜,取底层析出的沉淀,50℃烘箱中干燥24h即得重金属离子吸附剂,产物质量为7.56g,命名为OSA-NH4-CS-3。In the solution after the above reaction, a mixed solution of CS 2 and NaOH is added, and the mixed solution is prepared by mixing 5 g of CS 2 and 6.25 mL of 30% NaOH solution, and the reaction temperature is 40 ° C, and the reaction is continued until there is no CS 2 liquid in the solution. drop. The reaction was stopped, isopropanol was added in an amount of 3 times the volume of the reactant solution, and the mixture was allowed to stand overnight. The precipitate obtained by bottom chromatography was dried in an oven at 50 ° C for 24 hours to obtain a heavy metal ion adsorbent, and the product mass was 7.56 g, which was named OSA- NH 4 -CS-3.
以实施例一中得到的吸附剂(OSA-NH4-CS-1)为例,对污水中常见的重金属离子进行吸附,考察吸附剂的吸附能力和吸附条件。Taking the adsorbent (OSA-NH 4 -CS-1) obtained in the first embodiment as an example, the heavy metal ions commonly found in the sewage are adsorbed, and the adsorption capacity and adsorption conditions of the adsorbent are investigated.
为了比较吸附效果,合成了一种不含硫代羧酸根的吸附剂,命名为吸附剂参比样,该吸附剂参比样的合成过程中不加入CS2与NaOH混合溶液,其他合成条件与实施例一相同。表1是吸附剂参比样与实施例一中OSA-NH4-CS-1制备结果的比较。In order to compare the adsorption effect, an adsorbent containing no thiocarboxylate was synthesized and named as the adsorbent reference sample. The mixed solution of CS 2 and NaOH was not added during the synthesis of the adsorbent. The other synthetic conditions were The first embodiment is the same. Table 1 is a comparison of the sorbent reference sample with the results of the preparation of OSA-NH 4 -CS-1 in Example 1.
表1 两种吸附剂的合成结果比较Table 1 Comparison of the synthesis results of two adsorbents
Figure PCTCN2015079757-appb-000002
Figure PCTCN2015079757-appb-000002
将OSA-NH4-CS-1、吸附剂参比样和海藻酸钠用于吸附Pb2+,分别 取上述三种吸附剂1.0g,配置成质量百分含量1%的水溶液,分别取它们的水溶液5mL、10mL、15mL、20mL加入到50mL浓度为5mmol/L Pb(NO3)2溶液中,震荡20min(120r/min)后,离心分离15min(4000r/min),取上层清液10mL,加入1mL六亚甲基四胺-盐酸缓冲溶液(pH=6.11),以0.2%二甲酚橙溶液做指示剂,用9.97mmol/L EDTA溶液进行滴定,测试溶液中Pb2+浓度,计算对Pb2+的去除率和吸附率。OSA-NH 4 -CS-1, adsorbent reference sample and sodium alginate were used to adsorb Pb 2+ , and 1.0 g of the above three adsorbents were respectively taken and disposed as an aqueous solution of 1% by mass, respectively. 5 mL, 10 mL, 15 mL, and 20 mL of the aqueous solution were added to 50 mL of a 5 mmol/L Pb(NO 3 ) 2 solution, shaken for 20 min (120 r/min), centrifuged for 15 min (4000 r/min), and 10 mL of the supernatant was taken. Add 1 mL of hexamethylenetetramine-hydrochloric acid buffer solution (pH=6.11), use 0.2% xylenol orange solution as indicator, titrate with 9.97mmol/L EDTA solution, test the concentration of Pb 2+ in the solution, calculate the pair Pb 2+ removal rate and adsorption rate.
从表2可以看出,经过改性后的吸附剂OSA-NH4-CS-1比改性前的海藻酸钠,对铅离子吸附容量和去除率(表2括号内为去除率)都有了明显提高,而OSA-NH4-CS-1与吸附剂参比样相比,其吸附容量增加,说明硫代羧酸根的引入是提高吸附率的关键因素。It can be seen from Table 2 that the modified adsorbent OSA-NH 4 -CS-1 has higher adsorption capacity and removal rate for lead ions than the sodium alginate before modification (Table 2 shows the removal rate in parentheses). The apparent increase is improved, and the adsorption capacity of OSA-NH 4 -CS-1 is higher than that of the adsorbent reference sample, indicating that the introduction of thiocarboxylate is a key factor for increasing the adsorption rate.
表2 不同吸附剂对Pb2+吸附容量的影响(mmol/g)Table 2 Effect of different adsorbents on Pb 2+ adsorption capacity (mmol/g)
Figure PCTCN2015079757-appb-000003
Figure PCTCN2015079757-appb-000003
又将OSA-NH4-CS-1和海藻酸钠用于吸附Cd2+,用Cd(NO3)2代替Pb(NO3)2,操作步骤与吸附Pb2+的步骤相同,测定吸附剂对Cd2+的吸附性能,从表3可以看出,对比海藻酸钠,OSA-NH4-CS-1对溶液中Cd2+的吸附性能有较大提高。 Further, OSA-NH 4 -CS-1 and sodium alginate were used to adsorb Cd 2+ , and Cd(NO 3 ) 2 was used instead of Pb(NO 3 ) 2 . The procedure was the same as the step of adsorbing Pb 2+ , and the adsorbent was measured. As for the adsorption performance of Cd 2+ , it can be seen from Table 3 that compared with sodium alginate, the adsorption performance of OSA-NH 4 -CS-1 on Cd 2+ in solution is greatly improved.
表3 不同吸附剂对Cd2+吸附容量的影响(mmol/g)Table 3 Effect of different adsorbents on Cd 2+ adsorption capacity (mmol/g)
Figure PCTCN2015079757-appb-000004
Figure PCTCN2015079757-appb-000004
R:去除率;Q:吸附容量R: removal rate; Q: adsorption capacity
溶液中金属离子的初始浓度会影响吸附剂的吸附效果,因此,我们考察了不同浓度的Pb2+溶液对不同吸附剂的吸附效果的影响。配置浓度分别为5.0、10.0、20.0、40.0、50.0(mmol/L)的Pb(NO3)2溶液,各取50mL,加入10mL OSA-NH4-CS-1溶液(1%,w/w),震荡20min(120r/min)后,离心分离15min(4000r/min),取2份10mL上层清液,分别测试溶液中Pb2+浓度,计算吸附剂对Pb2+去除率和吸附率。用相同的方法,以海藻酸钠溶液(1%,w/w)为对比进行测试,将结果进行对比。从表4中可以看出,随着Pb2+浓度加大,吸附剂的吸附趋于饱和,吸附量也趋于稳定。OSA-NH4-CS-1的饱和吸附量高于SA的饱和吸附量,说明改性后的吸附剂吸附性能优于海藻酸钠,从金属离子去除率来看,当Pb2+浓度较低时效果较佳。 The initial concentration of metal ions in the solution affects the adsorption of the adsorbent. Therefore, we investigated the effects of different concentrations of Pb 2+ solution on the adsorption of different adsorbents. Pb(NO 3 ) 2 solutions with concentrations of 5.0, 10.0, 20.0, 40.0, 50.0 (mmol/L) were prepared, each taking 50 mL, and 10 mL of OSA-NH 4 -CS-1 solution (1%, w/w) was added. After shaking for 20 min (120 r/min), centrifuge for 15 min (4000 r/min), take 2 parts of 10 mL of supernatant, test the concentration of Pb 2+ in the solution, calculate the removal rate and adsorption rate of Pb 2+ by the adsorbent. In the same manner, sodium alginate solution (1%, w/w) was used as a comparison, and the results were compared. It can be seen from Table 4 that as the concentration of Pb 2+ increases, the adsorption of the adsorbent tends to be saturated, and the adsorption amount tends to be stable. The saturated adsorption capacity of OSA-NH 4 -CS-1 is higher than that of SA, indicating that the adsorption performance of the modified adsorbent is better than that of sodium alginate. When the metal ion removal rate is low, the Pb 2+ concentration is lower. The effect is better.
表4 Pb2+初始浓度对吸附效果的影响Table 4 Effect of initial concentration of Pb 2+ on adsorption
Figure PCTCN2015079757-appb-000005
Figure PCTCN2015079757-appb-000005
R:去除率;Q:吸附容量R: removal rate; Q: adsorption capacity
溶液的pH对吸附效果至关重要,将OSA-NH4-CS-1溶液加入不同Pb(NO3)2溶液后,调节溶液pH,测得吸附剂对于Pb2+离子的去除率及吸附容量结果如表5所示,从表中可以看出,在pH 5-6之间,吸附剂的吸附性能差别不大。The pH of the solution is very important for the adsorption effect. After the OSA-NH 4 -CS-1 solution is added to different Pb(NO 3 ) 2 solutions, the pH of the solution is adjusted, and the removal rate and adsorption capacity of the adsorbent for Pb 2+ ions are measured. The results are shown in Table 5. As can be seen from the table, the adsorption performance of the adsorbent did not differ much between pH 5-6.
表5 溶液pH对吸附性能的影响Table 5 Effect of solution pH on adsorption performance
样品编号Sample serial number 溶液pHSolution pH R(%)R (%) Q(mmol/L)Q (mmol/L)
11 44 6.46.4 0.160.16
22 55 10.610.6 0.260.26
33 66 39.739.7 0.990.99
44 77 73.6073.60 1.831.83
55 88 90.490.4 2.252.25
66 99 96.4096.40 2.402.40
77 1010 96.4096.40 2.402.40
综上所述,本发明通过将海藻酸钠改性,制备得到一种重金属离子吸附剂,海藻酸钠的来源丰富,价格便宜,改性步骤少,产物使用方便,后处理容易,无二次污染,环境友好;该吸附剂上带有较多的氨基、硫代羧酸根等基团,这两类基团对于重金属的捕捉能力极强,吸附容量大、脱除率高、速度快,加上海藻酸钠结构中的羧基,几种基团协同作用,可与重金属离子形成螯合物,因此对于重金属离子有较好的吸附作用,将其应用于污水的处理,操作简单,成本低廉,重金属残留率低;该重金属离子吸附剂与现有的海藻酸钠相比,吸附能力更强,吸附容量更大,而且适用的pH范围广,因此适用面广。In summary, the present invention prepares a heavy metal ion adsorbent by modifying sodium alginate. The source of sodium alginate is abundant, the price is cheap, the modification step is small, the product is convenient to use, and the post-treatment is easy, no secondary Contaminated, environmentally friendly; the adsorbent has a large number of amino groups, thiocarboxylates and other groups, these two groups have strong capture ability for heavy metals, large adsorption capacity, high removal rate, fast speed, plus The carboxyl group in the sodium alginate structure of Shanghai has synergistic effects to form a chelate with heavy metal ions. Therefore, it has a good adsorption effect on heavy metal ions, and is applied to the treatment of sewage, which is simple in operation and low in cost. The heavy metal residual ratio is low; the heavy metal ion adsorbent has higher adsorption capacity, larger adsorption capacity, and wider pH range than the existing sodium alginate, so it is suitable for a wide range of applications.
以上所述仅为本发明的优选实施例而已,并不用于限制本发明,对于本领域的技术人员来说,本发明可以有各种更改和变化。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。 The above description is only the preferred embodiment of the present invention, and is not intended to limit the present invention, and various modifications and changes can be made to the present invention. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and scope of the present invention are intended to be included within the scope of the present invention.

Claims (10)

  1. 一种重金属离子吸附剂的制备方法,其特征在于:包括以下步骤:A method for preparing a heavy metal ion adsorbent, comprising: the following steps:
    (1)将醛基海藻酸钠配成水溶液,加入多乙烯多胺反应,然后加入硼氢化钠还原,继续反应,得到氨基海藻酸钠;(1) The aldehyde-based sodium alginate is formulated into an aqueous solution, and the reaction with polyethene polyamine is added, followed by reduction with sodium borohydride, and the reaction is continued to obtain amino sodium alginate;
    (2)在所述步骤(1)中反应后的溶液中加入二硫化碳与氢氧化钠的混合溶液,继续反应至溶液中二硫化碳液滴消失,停止反应,加入醇类溶剂使产物沉淀,静置,分层,分离底层析出的沉淀,干燥后,得到重金属离子吸附剂。(2) adding a mixed solution of carbon disulfide and sodium hydroxide to the solution in the step (1), continuing the reaction until the carbon disulfide droplets disappear in the solution, stopping the reaction, adding an alcohol solvent to precipitate the product, and allowing to stand. The layers were separated, and the precipitate obtained by the bottom chromatography was separated, and after drying, a heavy metal ion adsorbent was obtained.
  2. 根据权利要求1所述的一种重金属离子吸附剂的制备方法,其特征在于:所述步骤(1)中,醛基海藻酸钠在水溶液中的质量百分含量为5.8%。The method for preparing a heavy metal ion adsorbent according to claim 1, wherein in the step (1), the mass percentage of the aldehyde-based sodium alginate in the aqueous solution is 5.8%.
  3. 根据权利要求1所述的一种重金属离子吸附剂的制备方法,其特征在于:所述多乙烯多胺包括乙二胺、二乙烯三胺、三乙烯四胺、四乙烯五胺中的任意一种或多种。The method for preparing a heavy metal ion adsorbent according to claim 1, wherein the polyethene polyamine comprises any one of ethylenediamine, diethylenetriamine, triethylenetetramine, and tetraethylenepentamine. Kind or more.
  4. 根据权利要求1所述的一种重金属离子吸附剂的制备方法,其特征在于:所述步骤(1)中,所述多乙烯多胺的质量是氧化海藻酸钠质量的1~3倍,所述硼氢化钠的质量是醛基海藻酸钠质量的60%。The method for preparing a heavy metal ion adsorbent according to claim 1, wherein in the step (1), the mass of the polyethene polyamine is 1 to 3 times that of the mass of the oxidized sodium alginate. The mass of sodium borohydride is 60% of the mass of aldehyde-based sodium alginate.
  5. 根据权利要求1所述的一种重金属离子吸附剂的制备方法,其特征在于:所述步骤(1)中,醛基海藻酸钠与多乙烯多胺的反应温度为40℃,反应时间为24h。The method for preparing a heavy metal ion adsorbent according to claim 1, wherein in the step (1), the reaction temperature of the aldehyde-based sodium alginate and the polyethene polyamine is 40 ° C, and the reaction time is 24 h. .
  6. 根据权利要求1所述的一种重金属离子吸附剂的制备方法,其特征在于:所述步骤(2)中,二硫化碳与氢氧化钠的混合溶液由等体积的二硫化碳与质量百分含量为30%的氢氧化钠水溶液混合形成,氨基海藻酸钠与二硫化碳质量此为1∶0.8~1.2。 The method for preparing a heavy metal ion adsorbent according to claim 1, wherein in the step (2), the mixed solution of carbon disulfide and sodium hydroxide is composed of an equal volume of carbon disulfide and a mass percentage of 30%. The aqueous solution of sodium hydroxide is mixed, and the mass of sodium amino alginate and carbon disulfide is 1:0.8 to 1.2.
  7. 根据权利要求1所述的一种重金属离子吸附剂的制备方法,其特征在于:所述步骤(2)中,所述醇类溶剂包括甲醇、无水乙醇、异丙醇中的任意一种或多种,用量为反应物溶液体积的3倍。The method for preparing a heavy metal ion adsorbent according to claim 1, wherein in the step (2), the alcohol solvent comprises any one of methanol, absolute ethanol, and isopropanol. A variety of amounts of three times the volume of the reactant solution.
  8. 根据权利要求1所述的一种重金属离子吸附剂的制备方法,其特征在于:所述步骤(2)中反应温度为40℃。The method for preparing a heavy metal ion adsorbent according to claim 1, wherein the reaction temperature in the step (2) is 40 °C.
  9. 根据权利要求1所述的一种重金属离子吸附剂的制备方法,其特征在于:所述步骤(1)中醛基海藻酸钠的制备过程包括以下步骤:将海藻酸钠分散在无水乙醇中,配成质量百分含量为15~20%的分散液,然后加入0.8mol/L的高碘酸钠水溶液,高碘酸钠与海藻酸钠的质量此为1∶0.4~1,避光反应后,加入乙二醇终止反应,乙二醇的质量为海藻酸钠的22.5%,洗涤、烘干后得到醛基海藻酸钠。The method for preparing a heavy metal ion adsorbent according to claim 1, wherein the preparation process of the aldehyde-based sodium alginate in the step (1) comprises the steps of dispersing sodium alginate in anhydrous ethanol. , formulated into a mass percentage of 15-20% dispersion, and then added 0.8mol / L sodium periodate aqueous solution, the quality of sodium periodate and sodium alginate is 1:0.4 ~ 1, in the dark Thereafter, the reaction was terminated by adding ethylene glycol, and the mass of the ethylene glycol was 22.5% of sodium alginate. After washing and drying, an aldehyde-based sodium alginate was obtained.
  10. 一种重金属离子吸附剂的应用,其特征在于:将权利要求1-9中任意一项所述的重金属离子吸附剂用于含有重金属离子的工业污水的处理,吸附污水中的重金属离子。 An application of a heavy metal ion adsorbent, characterized in that the heavy metal ion adsorbent according to any one of claims 1 to 9 is used for the treatment of industrial sewage containing heavy metal ions, and adsorbs heavy metal ions in the sewage.
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