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CN103754978B - A method of selective adsorption and separation of lead ions using KNbWO6 - Google Patents

A method of selective adsorption and separation of lead ions using KNbWO6 Download PDF

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CN103754978B
CN103754978B CN201410027131.9A CN201410027131A CN103754978B CN 103754978 B CN103754978 B CN 103754978B CN 201410027131 A CN201410027131 A CN 201410027131A CN 103754978 B CN103754978 B CN 103754978B
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lead
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knbwo
tungstate
lead ions
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CN103754978A (en
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庞广生
韩永男
焦世惠
徐曼
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Jilin University
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Abstract

本发明公开了一种利用烧绿石结构的KNbWO6·H2O选择吸附分离重金属铅离子的方法。在水中加入铌钨酸钾,在pH值4~5.5下搅拌20~50小时,离心分离固体和清液;铌钨酸钾用量按水体积计算为0.2~0.6克/升。KNbWO6·H2O可以通过离子交换作用吸附分离铅离子,且对于铅离子的吸附有很好的选择性。本发明方法简便、高效,对重金属铅离子的分离吸附具有很好的效果,可以应用于废水污水中重金属铅的去除以及复杂体系中铅离子的分离,吸附铅离子后的铌钨酸钾可以利用硝酸交换再生,重复利用。

The invention discloses a method for selectively adsorbing and separating heavy metal lead ions by using pyrochlore-structured KNbWO 6 ·H 2 O. Add potassium niobate tungstate into water, stir for 20-50 hours at pH 4-5.5, and centrifuge to separate the solid and clear liquid; the dosage of potassium niobate tungstate is calculated as 0.2-0.6 g/L based on the volume of water. KNbWO 6 ·H 2 O can adsorb and separate lead ions through ion exchange, and has good selectivity for the adsorption of lead ions. The method of the present invention is simple and efficient, and has a good effect on the separation and adsorption of heavy metal lead ions, and can be applied to the removal of heavy metal lead in waste water and the separation of lead ions in complex systems, and the potassium niobate tungstate after the lead ion adsorption can be used Nitric acid exchange regeneration, reuse.

Description

一种利用KNbWO6选择吸附分离铅离子的方法A method of selective adsorption and separation of lead ions using KNbWO6

技术领域 technical field

本发明属于重金属吸附分离的技术领域,涉及一种无机离子交换剂的应用,用于污水废水中铅离子的吸附分离。 The invention belongs to the technical field of adsorption and separation of heavy metals, and relates to the application of an inorganic ion exchanger for the adsorption and separation of lead ions in sewage and wastewater.

背景技术 Background technique

采矿、废气排放和使用金属制品等产生的重金属污染成为影响人类健康的重要问题。铅是一种十分常见且毒很强的重金属污染物,在金属电镀,原油精炼,油漆和颜料产业以及电池生产等过程中都会产生污染。环境中的无机铅及其化合物十分稳定,不易代谢和降解,接触到铅会对人体器官特别是肺、肾脏、生殖系统、心血管系统带来不良影响。由于铅的毒性和污染特点,对其在环境中的标准值要求很高,特别是西方发达国家对铅的使用有严格的限制,中国2012年最新的《生活饮用水卫生标准》要求铅含量不可超过0.01mg/L。 Heavy metal pollution from mining, exhaust emissions and use of metal products has become an important issue affecting human health. Lead is a very common and highly toxic heavy metal pollutant, which can be polluted in processes such as metal plating, crude oil refining, paint and pigment industry, and battery production. Inorganic lead and its compounds in the environment are very stable and difficult to metabolize and degrade. Exposure to lead will have adverse effects on human organs, especially the lungs, kidneys, reproductive system, and cardiovascular system. Due to the toxicity and pollution characteristics of lead, the standard value of lead in the environment is very high, especially the western developed countries have strict restrictions on the use of lead. China's latest "Drinking Water Sanitation Standard" in 2012 requires that the lead content is More than 0.01mg/L.

高效的去除污水中铅等重金属离子的有效方法对于保护环境和人类健康十分重要。处理废水中的重金属离子有很多种方法,例如:还原沉积、蒸发、电化学还原、吸附和直接沉降。吸附被认为是高效且比较经济的用于处理污水中重金属离子的方法,包括活性炭等吸附剂可以用于除去污水中的重金属离子。天然或人造沸石、金属亚铁氰化物及铁氰化物、层状化合物、过渡金属水合氧化物和氢氧化物等无机材料也可以作为重金属离子的吸附剂。近年来,有报道利用钛酸盐纳米结构(J.Phys.Chem.C.,112,16275-16280,2008)及钛酸盐与四氧化三铁复合物(J.Mater.Chem.A.,1,805-813,2013)作为铅离子的吸附剂;层状锰氧化物也用于铅离子的吸附剂(J.Hazard.Mater.,196,318-326,2011)。 Effective methods to efficiently remove heavy metal ions such as lead in sewage are very important for protecting the environment and human health. There are many methods for treating heavy metal ions in wastewater, such as: reductive deposition, evaporation, electrochemical reduction, adsorption and direct sedimentation. Adsorption is considered to be an efficient and economical method for treating heavy metal ions in sewage, including activated carbon and other adsorbents that can be used to remove heavy metal ions in sewage. Inorganic materials such as natural or artificial zeolites, metal ferrocyanides and ferricyanides, layered compounds, transition metal hydrated oxides and hydroxides can also be used as adsorbents for heavy metal ions. In recent years, it has been reported that titanate nanostructures (J.Phys.Chem.C., 112, 16275-16280, 2008) and titanate-ferric oxide complexes (J.Mater.Chem.A., 1,805-813,2013) as an adsorbent for lead ions; layered manganese oxides are also used as adsorbents for lead ions (J.Hazard.Mater.,196,318-326,2011).

发明内容 Contents of the invention

本发明要解决的技术问题是,提供了不同于现有技术的一种利用烧绿石结构铌钨酸盐KNbWO6通过离子交换作用吸附分离铅离子的方法。 The technical problem to be solved by the present invention is to provide a method for adsorbing and separating lead ions by using pyrochlore structure niobium tungstate KNbWO 6 through ion exchange, which is different from the prior art.

烧绿石结构铌钨酸钾对于铅离子Pb2+的吸附有很好的选择性,将KNbWO6·H2O和同时含有Cd2+、Co2+、Mn2+、Pb2+离子的溶液进行吸附实验时发现,Cd2+、Co2+、Mn2+三种离子的存在对于铅离子的吸附效果无明显影响。吸附铅离子后的铌钨酸盐可以利用硝酸交换再生,重复利用。本发明方法简便、高效,对重金属铅的分离吸附具有很好的效果,可以用于污水中重金属的去除,以及复杂体系中铅离子的分离。 Pyrochlore - structured potassium niobate tungstate has good selectivity for the adsorption of lead ion Pb 2+ . When the solution was subjected to adsorption experiments, it was found that the presence of three ions, Cd 2+ , Co 2+ , and Mn 2+ , had no significant effect on the adsorption effect of lead ions. The niobium tungstate after adsorbing lead ions can be regenerated by nitric acid exchange and reused. The method of the invention is simple and efficient, has a good effect on the separation and adsorption of the heavy metal lead, and can be used for the removal of heavy metals in sewage and the separation of lead ions in complex systems.

具体的技术方案如下。 Concrete technical scheme is as follows.

一种利用KNbWO6选择吸附分离铅离子的方法,在水中加入铌钨酸钾(KNbWO6·H2O),在pH值4~5.5下搅拌20~50小时,离心分离固体和清液;铌钨酸钾用量按水体积计算为0.2~0.6克/升。 A method for selective adsorption and separation of lead ions using KNbWO 6 , adding potassium niobate tungstate (KNbWO 6 ·H 2 O) to water, stirring at pH 4-5.5 for 20-50 hours, and centrifuging to separate the solid and clear liquid; niobium The dosage of potassium tungstate is 0.2-0.6 g/L calculated by volume of water.

所述的铌钨酸钾,是烧绿石结构的KNbWO6·H2O。 The potassium niobate tungstate mentioned above is KNbWO 6 ·H 2 O with pyrochlore structure.

优选的离子交换条件为,铌钨酸钾用量按水体积计算为0.4~0.5克/升,在pH值5~5.5下搅拌48~50小时。铌钨酸钾用量大于0.5克/升效果也很好,但大于0.6克/升就浪费了。 The preferred ion exchange condition is that the dosage of potassium niobate tungstate is 0.4-0.5 g/liter calculated by volume of water, and the mixture is stirred for 48-50 hours at a pH value of 5-5.5. Potassium niobate tungstate dosage greater than 0.5 g/L is also very effective, but more than 0.6 g/L is wasted.

可以用浓度0.1摩尔/升的硝酸调节pH值。 The pH can be adjusted with nitric acid at a concentration of 0.1 mol/L.

温度的升高有助于Pb2+离子吸附率的提高。但对废水污水中Pb2+离子吸附分离而言,大多数是在常温下进行的。 The increase of temperature contributes to the improvement of the adsorption rate of Pb 2+ ions. But for the adsorption and separation of Pb 2+ ions in wastewater, most of them are carried out at room temperature.

本发明首次提出利用铌钨酸钾通过离子交换作用吸附分离铅离子,这种利用离子交换作用进行吸附分离的方法与现有的、利用表面吸附作用吸附分离铅离子在原理上完全不同;本发明方法简便、高效;烧绿石结构的KNbWO6·H2O对重金属铅离子的分离吸附更具有非常好的效果,吸附率在75%以上,对吸附后所得清液进行感应耦合等离子体(ICP)分析测试,利用Langmuir等温吸附方程进行拟合计算,KNbWO6·H2O样品在pH值为5.0,对硝酸铅溶液中铅离子最大吸附量为86.95毫克/克;在只有离子可以进入的烧绿石结构的KNbWO6·H2O的孔道结构中,通过离子交换吸附分离铅离子,且对于铅离子的吸附具有更好的选择性,可以避免复杂体系中其他杂质对吸附效果产生影响;本发明可以应用于污水中重金属铅(铅离子)的去除以及复杂体系中铅离子的分离,吸附铅离子后的铌钨酸钾可以利用硝酸交换再生,重复利用。 The present invention proposes for the first time to use potassium niobate tungstate to adsorb and separate lead ions through ion exchange. This method of adsorbing and separating lead ions using ion exchange is completely different in principle from the existing method of using surface adsorption to adsorb and separate lead ions; the present invention The method is simple and efficient; pyrochlore-structured KNbWO 6 ·H 2 O has a very good effect on the separation and adsorption of heavy metal lead ions, and the adsorption rate is above 75%. The inductively coupled plasma (ICP ) analysis test, using the Langmuir isotherm adsorption equation for fitting calculation, the KNbWO 6 ·H 2 O sample has a pH value of 5.0, and the maximum adsorption capacity of lead ions in the lead nitrate solution is 86.95 mg/g; In the pore structure of KNbWO 6 ·H 2 O with a green stone structure, lead ions are separated by ion exchange adsorption, and the adsorption of lead ions has better selectivity, which can avoid other impurities in the complex system from affecting the adsorption effect; this paper The invention can be applied to the removal of heavy metal lead (lead ions) in sewage and the separation of lead ions in complex systems. Potassium niobium tungstate after adsorbing lead ions can be regenerated by nitric acid exchange and reused.

附图说明 Description of drawings

图1为铌钨酸钾KNbWO6·H2O交换铅离子的朗格缪尔(Langmuir)等温吸附曲线拟合模型。 Figure 1 is the fitting model of the Langmuir isotherm adsorption curve for potassium niobate tungstate KNbWO 6 ·H 2 O exchanging lead ions.

图2为实施例2的离子交换吸附效率随时间变化曲线。其中离子交换效率是: Fig. 2 is the time-varying curve of ion exchange adsorption efficiency in Example 2. where the ion exchange efficiency is:

纵坐标是交换后溶液中剩余铅离子浓度。 The ordinate is the remaining lead ion concentration in the solution after exchange.

图3为铌钨酸钾KNbWO6·H2O对50毫克/升硝酸铅溶液的离子交换吸附效率以及硝酸铅与硝酸钴、氯化锰、氯化镉溶液共存时铅离子交换吸附结果比较。 Figure 3 shows the ion exchange adsorption efficiency of potassium niobate tungstate KNbWO 6 ·H 2 O on 50 mg/L lead nitrate solution and the comparison of lead ion exchange adsorption results when lead nitrate coexists with cobalt nitrate, manganese chloride and cadmium chloride solutions.

具体实施方式 Detailed ways

实施例1  Example 1

配制浓度为20,30,40,50,60,80,90,100毫克/升的硝酸铅溶液各50毫升,用1摩尔/升的硝酸调节溶液pH值为5.0,室温条件下,将20毫克烧绿石结构的KNbWO6·H2O加入到上述50毫升硝酸铅溶液中,磁力搅拌作用下离子交换时间48小时后,离心方法将固液分离,得到的清液利用感应耦合等离子体(ICP)进行铅离子浓度分析。测得的实验结果与朗格缪尔(Langmuir)等温吸附方程式进行拟合,用平衡浓度Ce(毫克/升)对Ce/Qe(克/升,Qe是平衡吸附量)作图,发现Langmuir等温吸附曲线很好的拟合了等温线数据。 Prepare 50 milliliters of lead nitrate solutions with concentrations of 20, 30, 40, 50, 60, 80, 90, and 100 mg/L, adjust the pH value of the solution to 5.0 with 1 mol/L of nitric acid, and mix 20 mg/L of KNbWO 6 ·H 2 O with a pyrochlore structure was added to the above 50 ml lead nitrate solution, and after 48 hours of ion exchange time under the action of magnetic stirring, the solid-liquid was separated by centrifugation, and the obtained clear liquid was inductively coupled plasma (ICP ) for lead ion concentration analysis. The measured experimental results were fitted with the Langmuir isotherm adsorption equation, and the equilibrium concentration Ce (mg/L) was plotted against Ce/Qe (gram/L, Qe is the equilibrium adsorption amount), and it was found that the Langmuir isotherm The adsorption curves fit the isotherm data well.

图1给出Langmuir等温吸附拟合曲线数据。 Figure 1 shows the Langmuir isotherm adsorption curve fitting curve data.

实施例2  Example 2

配制30毫克/升硝酸铅溶液,用1摩尔/升的硝酸调节溶液pH值为5.0,室温条件下,将20毫克烧绿石结构的KNbWO6·H2O加入到上述50毫升硝酸铅溶液中,磁力搅拌作用下离子交换时间48小时后,离心方法将固液分离,得到的清液利用感应耦合等离子体(ICP)进行铅离子浓度分析。 Prepare a 30 mg/L lead nitrate solution, adjust the pH of the solution to 5.0 with 1 mol/L nitric acid, and add 20 mg of pyrochlore-structured KNbWO 6 ·H 2 O to the above 50 ml lead nitrate solution at room temperature After 48 hours of ion exchange time under the action of magnetic stirring, the solid and liquid were separated by centrifugation, and the obtained clear liquid was analyzed for lead ion concentration by inductively coupled plasma (ICP).

离子交换48小时后,离子交换效率为99.0%。图2给出铌钨酸钾KNbWO6·H2O对30毫克/升硝酸铅溶液的离子交换吸附效率随时间变化曲线。右图2可知,本实施例条件下离子交换时间20小时,离子交换效率88.7%。 After 48 hours of ion exchange, the ion exchange efficiency was 99.0%. Figure 2 shows the time-dependent curve of the ion exchange adsorption efficiency of potassium niobate tungstate KNbWO 6 ·H 2 O to 30 mg/L lead nitrate solution. It can be seen from Figure 2 on the right that under the conditions of this example, the ion exchange time is 20 hours, and the ion exchange efficiency is 88.7%.

实施例3  Example 3

配制50毫克/升硝酸铅溶液,用1摩尔/升的硝酸调节溶液pH值为5.0,室温条件下,将20毫克烧绿石结构的KNbWO6·H2O加入到上述50毫升硝酸铅溶液中,磁力搅拌作用下离子交换时间48小时后,离心方法将固液分离,得到的清液利用感应耦合等离子体(ICP)进行铅离子浓度分析。 Prepare a 50 mg/L lead nitrate solution, adjust the pH of the solution to 5.0 with 1 mol/L nitric acid, and add 20 mg of pyrochlore-structured KNbWO 6 ·H 2 O to the above 50 ml lead nitrate solution at room temperature After 48 hours of ion exchange time under the action of magnetic stirring, the solid and liquid were separated by centrifugation, and the obtained clear liquid was analyzed for lead ion concentration by inductively coupled plasma (ICP).

与实施例2相比较,增加铅离子初始浓度,离子交换效率76.2%。 Compared with Example 2, increasing the initial concentration of lead ions, the ion exchange efficiency was 76.2%.

实施例4  Example 4

配制30毫克/升硝酸铅溶液,用1摩尔/升的硝酸调节溶液pH值为4.0,室温条件下,将20毫克烧绿石结构的KNbWO6·H2O加入到上述50毫升硝酸铅溶液中,磁力搅拌作用下离子交换时间48小时后,离心方法将固液分离,得到的清液利用ICP进行铅离子浓度分析。 Prepare a 30 mg/L lead nitrate solution, adjust the pH of the solution to 4.0 with 1 mol/L nitric acid, and add 20 mg of pyrochlore-structured KNbWO 6 ·H 2 O to the above 50 ml lead nitrate solution at room temperature After 48 hours of ion exchange time under the action of magnetic stirring, the solid and liquid were separated by centrifugation, and the obtained clear liquid was analyzed for lead ion concentration by ICP.

与实施例2相比较,反应pH值下降,离子交换效率降低。 Compared with Example 2, the reaction pH value decreased, and the ion exchange efficiency decreased.

实施例5  Example 5

配制30毫克/升硝酸铅溶液,用1摩尔/升的硝酸调节溶液pH值为5.5,室温条件下,将20毫克烧绿石结构的KNbWO6·H2O加入到上述50毫升硝酸铅溶液中,磁力搅拌作用下离子交换时间48小时后,离心方法将固液分离,得到的清液利用ICP进行铅离子浓度分析。 Prepare a 30 mg/L lead nitrate solution, adjust the pH of the solution to 5.5 with 1 mol/L nitric acid, and add 20 mg of pyrochlore-structured KNbWO 6 ·H 2 O to the above 50 ml lead nitrate solution at room temperature After 48 hours of ion exchange time under the action of magnetic stirring, the solid and liquid were separated by centrifugation, and the obtained clear liquid was analyzed for lead ion concentration by ICP.

与实施例2相比较,反应pH值增大,离子交换效率无明显变化。 Compared with Example 2, the reaction pH value increases, but the ion exchange efficiency does not change significantly.

实施例6  Example 6

配制30毫克/升硝酸铅溶液,用1摩尔/升的硝酸调节溶液pH值为5.0,室温条件下,将20毫克烧绿石结构的KNbWO6·H2O加入到上述50毫升硝酸铅溶液中,磁力搅拌作用下离子交换时间10小时后,离心方法将固液分离,得到的清液利用ICP进行铅离子浓度分析。 Prepare a 30 mg/L lead nitrate solution, adjust the pH of the solution to 5.0 with 1 mol/L nitric acid, and add 20 mg of pyrochlore-structured KNbWO 6 ·H 2 O to the above 50 ml lead nitrate solution at room temperature After 10 hours of ion exchange time under the action of magnetic stirring, the solid and liquid were separated by centrifugation, and the obtained clear liquid was analyzed for lead ion concentration by ICP.

与实施例2相比较,缩短离子交换时间,离子交换效率下降。离子交换时间10小时离子交换效率约为67%。 Compared with Example 2, the ion exchange time is shortened, and the ion exchange efficiency decreases. The ion exchange time is 10 hours and the ion exchange efficiency is about 67%.

实施例7  Example 7

配制30毫克/升硝酸铅溶液,用1摩尔/升的硝酸调节溶液pH值为5.0,室温条件下,将20毫克烧绿石结构的KNbWO6·H2O加入到上述50毫升硝酸铅溶液中,磁力搅拌作用下离子交换时间50小时后,离心方法将固液分离,得到的清液利用ICP进行铅离子浓度分析。 Prepare a 30 mg/L lead nitrate solution, adjust the pH of the solution to 5.0 with 1 mol/L nitric acid, and add 20 mg of pyrochlore-structured KNbWO 6 ·H 2 O to the above 50 ml lead nitrate solution at room temperature After 50 hours of ion exchange time under the action of magnetic stirring, the solid and liquid were separated by centrifugation, and the obtained clear liquid was analyzed for lead ion concentration by ICP.

与实施例2相比较,延长离子交换时间,离子交换效率无变化。 Compared with Example 2, the ion exchange efficiency does not change when the ion exchange time is prolonged.

实施例8  Example 8

配制30毫克/升硝酸铅溶液,用1摩尔/升的硝酸调节溶液pH值为5.0,室温条件下,将10毫克烧绿石结构的KNbWO6·H2O加入到上述50毫升硝酸铅溶液中,磁力搅拌作用下离子交换时间48小时后,离心方法将固液分离,得到的清液利用感应耦合等离子体(ICP)进行铅离子浓度分析。 Prepare a 30 mg/L lead nitrate solution, adjust the pH of the solution to 5.0 with 1 mol/L nitric acid, and add 10 mg of pyrochlore-structured KNbWO 6 ·H 2 O to the above 50 ml lead nitrate solution at room temperature After 48 hours of ion exchange time under the action of magnetic stirring, the solid and liquid were separated by centrifugation, and the obtained clear liquid was analyzed for lead ion concentration by inductively coupled plasma (ICP).

与实施例2相比较,减少KNbWO6·H2O用量,离子交换效率有所降低。 Compared with Example 2, reducing the amount of KNbWO 6 ·H 2 O reduces the ion exchange efficiency.

实施例9  Example 9

配制30毫克/升硝酸铅溶液,用1摩尔/升的硝酸调节溶液pH值为5.0,室温条件下,将30毫克烧绿石结构的KNbWO6·H2O加入到上述50毫升硝酸铅溶液中,磁力搅拌作用下离子交换时间48小时后,离心方法将固液分离,得到的清液利用感应耦合等离子体(ICP)进行铅离子浓度分析。 Prepare a 30 mg/L lead nitrate solution, adjust the pH of the solution to 5.0 with 1 mol/L nitric acid, and add 30 mg of pyrochlore-structured KNbWO 6 ·H 2 O to the 50 ml lead nitrate solution at room temperature After 48 hours of ion exchange time under the action of magnetic stirring, the solid and liquid were separated by centrifugation, and the obtained clear liquid was analyzed for lead ion concentration by inductively coupled plasma (ICP).

与实施例2相比较,增加KNbWO6·H2O用量,离子交换效率无变化。 Compared with Example 2, increasing the amount of KNbWO 6 ·H 2 O does not change the ion exchange efficiency.

实施例10  Example 10

配制30毫克/升硝酸铅溶液,用1摩尔/升的硝酸调节溶液pH值为5.0,体系升温到90℃后,将20毫克烧绿石结构的KNbWO6·H2O加入到上述50毫升硝酸铅溶液中,磁力搅拌作用下离子交换时间2小时后,离心方法将固液分离,得到的清液利用感应耦合等离子体(ICP)进行铅离子浓度分析。 Prepare a 30 mg/L lead nitrate solution, adjust the pH of the solution to 5.0 with 1 mol/L nitric acid, and add 20 mg of pyrochlore-structured KNbWO 6 ·H 2 O to the above 50 mL of nitric acid after the system is heated to 90°C In the lead solution, after 2 hours of ion exchange time under the action of magnetic stirring, the solid and liquid were separated by centrifugation, and the obtained clear liquid was analyzed for lead ion concentration by inductively coupled plasma (ICP).

离子交换时间仅2小时,离子交换效率为100%。与实施例2相比,温度升高,离子交换效率得到明显提高。 The ion exchange time is only 2 hours, and the ion exchange efficiency is 100%. Compared with Example 2, the ion exchange efficiency is obviously improved when the temperature is raised.

实施例11  Example 11

为了考察pH值对KNbWO6·H2O离子吸附效果的影响,进行条件一致的吸附效果实验,配制五份初始浓度50毫克/升的硝酸铅溶液50mL,分别用1摩尔/升的硝酸调节溶液pH值为2、3、4、5.0、5.5,室温条件下,将20毫克烧绿石结构的KNbWO6·H2O加入到上述硝酸铅溶液中,磁力搅拌作用下离子交换时间30小时后,离心方法将固液分离,得到的清液利用感应耦合等离子体(ICP)进行铅离子浓度分析。 In order to investigate the effect of pH value on the adsorption effect of KNbWO 6 ·H 2 O ions, the adsorption effect experiment with the same conditions was carried out. Five parts of lead nitrate solution with an initial concentration of 50 mg/L were prepared 50 mL, and the solutions were adjusted with 1 mol/L nitric acid respectively. The pH values are 2, 3, 4, 5.0, 5.5. At room temperature, 20 mg of pyrochlore-structured KNbWO 6 ·H 2 O is added to the above lead nitrate solution, and after 30 hours of ion exchange time under the action of magnetic stirring, The solid and liquid were separated by centrifugation, and the resulting clear liquid was analyzed for lead ion concentration by inductively coupled plasma (ICP).

表1给出不同pH值条件下,铌钨酸钾KNbWO6·H2O对硝酸铅溶液中的铅离子交换影响。 Table 1 shows the effect of potassium niobate tungstate KNbWO 6 ·H 2 O on the lead ion exchange in lead nitrate solution under different pH values.

实验结果说明pH值为5.0和5.5铅离子吸附效果好,pH值大于5.5吸附效果有下降趋势。 The experimental results show that the pH value is 5.0 and 5.5 lead ion adsorption effect is good, the pH value is greater than 5.5 the adsorption effect has a downward trend.

表1  Table 1

实施例12  Example 12

为了考察KNbWO6·H2O离子选择性吸附效果,进行选择性吸附实验:配制硝酸铅浓度为50毫克/升、硝酸钴浓度为50毫克/升、氯化锰浓度为50毫克/升、氯化镉浓度为50毫克/升的混合溶液50毫升,用0.1摩尔/升硝酸调节溶液pH值为5.0到5.5之间,加入20毫克烧绿石结构的KNbWO6·H2O样品,室温条件下搅拌30小时,离心分离固体和清液,清液进行感应耦合等离子体(ICP)分析,Mn2+,Cd2+,Co2+,Pb2+的离子交换效率分别为7.2%,0.6%,21.2%和78.6%。 In order to investigate the selective adsorption effect of KNbWO 6 ·H 2 O ions, a selective adsorption experiment was carried out: the concentration of lead nitrate was 50 mg/L, the concentration of cobalt nitrate was 50 mg/L, the concentration of manganese chloride was 50 mg/L, and the concentration of chlorine 50 milliliters of the mixed solution with a cadmium chloride concentration of 50 mg/liter, adjust the pH value of the solution between 5.0 and 5.5 with 0.1 mol/liter nitric acid, add 20 milligrams of the KNbWO 6 ·H 2 O sample with a pyrochlore structure, under room temperature Stir for 30 hours, centrifuge to separate the solid and the supernatant, and analyze the supernatant by inductively coupled plasma (ICP). The ion exchange efficiencies of Mn 2+ , Cd 2+ , Co 2+ and Pb 2+ are 7.2%, 0.6%, respectively. 21.2% and 78.6%.

铌钨酸钾KNbWO6?H2O对50毫克/升硝酸铅溶液的离子交换吸附效率以及硝酸铅与硝酸钴、氯化锰、氯化镉溶液共存时铅离子交换吸附结果比较,见图3。 The ion exchange adsorption efficiency of potassium niobate tungstate KNbWO 6 ?H 2 O on 50 mg/L lead nitrate solution and the comparison of lead ion exchange adsorption results when lead nitrate coexists with cobalt nitrate, manganese chloride and cadmium chloride solution, see Figure 3 .

与实施例3相比,在几种离子同时的存在的条件下,KNbWO6·H2O仍然对Pb2+保持很高的离子交换效率,对Pb2+具有很好的选择性。 Compared with Example 3, KNbWO 6 ·H 2 O still maintains a high ion exchange efficiency for Pb 2+ under the condition of simultaneous presence of several ions, and has good selectivity for Pb 2+ .

Claims (3)

1.一种利用KNbWO6选择吸附分离铅离子的方法,在水中加入铌钨酸钾,在pH值4~5.5下搅拌20~50小时,离心分离固体和清液;铌钨酸钾用量按水体积计算为0.2~0.6克/升;所述的铌钨酸钾,是烧绿石结构的KNbWO6·H2O。1. A method of using KNbWO 6 to selectively adsorb and separate lead ions. Add potassium niobate tungstate to water, stir for 20 to 50 hours at a pH value of 4 to 5.5, and centrifuge to separate the solid and clear liquid; the amount of potassium niobate tungstate is based on water The calculated volume is 0.2-0.6 g/L; the potassium niobate tungstate is KNbWO 6 ·H 2 O with a pyrochlore structure. 2.根据权利要求1所述的利用KNbWO6选择吸附分离铅离子的方法,其特征在于,所述的吸附分离铅离子的方法,铌钨酸钾用量按水体积计算为0.4~0.5克/升,在pH值5~5.5下搅拌48~50小时。2. The method for utilizing KNbWO6 to selectively adsorb and separate lead ions according to claim 1, characterized in that, in the method for adsorbing and separating lead ions, the amount of potassium niobate tungstate is calculated as 0.4 to 0.5 grams per liter according to the volume of water , stirred at pH 5-5.5 for 48-50 hours. 3.根据权利要求1或2所述的利用KNbWO6选择吸附分离铅离子的方法,其特征在于,用浓度0.1摩尔/升的硝酸调节pH值。3. The method for utilizing KNbWO 6 to selectively adsorb and separate lead ions according to claim 1 or 2, characterized in that the pH value is adjusted with nitric acid with a concentration of 0.1 mol/liter.
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