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CN105399179A - A method of removing ionic liquid in a water body by activated carbon adsorption promoted by utilization of phosphates - Google Patents

A method of removing ionic liquid in a water body by activated carbon adsorption promoted by utilization of phosphates Download PDF

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CN105399179A
CN105399179A CN201510909745.4A CN201510909745A CN105399179A CN 105399179 A CN105399179 A CN 105399179A CN 201510909745 A CN201510909745 A CN 201510909745A CN 105399179 A CN105399179 A CN 105399179A
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activated carbon
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ionic liquid
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water
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邱宇平
施凯顺
董志强
李月
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Tongji University
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Abstract

本发明涉及一种利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,属于水污染控制领域。该方法为:向含有离子液体的水体中加入磷酸盐,充分混和并溶解;用活性炭吸附水体中的离子液体,在达到吸附平衡或吸附饱和后,首先用酸性洗脱剂洗脱离子液体,再用碱性溶液回调活性炭pH至弱碱性,使活性炭重复利用于下一轮吸附中。与现有技术相比,本发明利用磷酸盐显著提升了活性炭吸附去除离子液体的能力。本发明无需进行其它额外操作处理,对离子液体的吸附去除效果提升明显,活性炭可重复使用多次,具有较好的推广应用前景。The invention relates to a method for using phosphate to promote active carbon adsorption to remove ionic liquid in water, belonging to the field of water pollution control. The method is as follows: add phosphate to the water body containing ionic liquid, fully mix and dissolve; use activated carbon to adsorb the ionic liquid in the water body, and after reaching adsorption equilibrium or adsorption saturation, firstly use an acidic eluent to elute the ionic liquid, and then Adjust the pH of the activated carbon to weak alkaline with alkaline solution, so that the activated carbon can be reused in the next round of adsorption. Compared with the prior art, the invention significantly improves the ability of the activated carbon to adsorb and remove the ionic liquid by utilizing the phosphate. The present invention does not need to perform other additional operations, and the adsorption and removal effect on the ionic liquid is significantly improved, and the activated carbon can be reused for many times, thus having a good promotion and application prospect.

Description

利用磷酸盐促进活性炭吸附去除水体中离子液体的方法The method of using phosphate to promote the adsorption of activated carbon to remove ionic liquid in water

技术领域technical field

本发明涉及一种离子液体处理方法,尤其是涉及一种利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,属于水污染控制领域。The invention relates to an ionic liquid treatment method, in particular to a method for using phosphate to promote the adsorption of activated carbon to remove the ionic liquid in water, belonging to the field of water pollution control.

背景技术Background technique

离子液体是指在室温下呈液态,完全由阴阳离子组成的熔盐化合物。它具有难挥发、对水和空气稳定、对多种物质溶解性能优越等特点,因此被称为“绿色溶剂”,被广泛应用于化工、医药、生物技术、农业和食品等领域。进入环境水体的离子液体不易被微生物所降解,对动物、植物和微生物都具有一定的毒性。因此,必须对工业水体中含有的离子液体进行合理有效的处置。Ionic liquids refer to molten salt compounds that are liquid at room temperature and are completely composed of anions and cations. It is difficult to volatilize, stable to water and air, and has excellent solubility for various substances, so it is called "green solvent" and is widely used in chemical, pharmaceutical, biotechnology, agriculture and food fields. The ionic liquids entering the environmental water body are not easy to be degraded by microorganisms, and have certain toxicity to animals, plants and microorganisms. Therefore, reasonable and effective disposal of ionic liquids contained in industrial water bodies must be carried out.

目前对离子液体溶液的处理措施主要有两类方法,一类是对离子液体的结构进行破坏,将离子液体转变为其他无害或低毒的小分子。相关措施包括热解、化学氧化以及生物处理等;这类方法不能对水体中的离子液体进行有效地资源回收。另一类方法是将离子液体从水体中进行有效分离回收,主要措施包括减压蒸馏、结晶、萃取以及吸附等。其中,减压蒸馏、结晶和萃取的方法并不适宜大规模地处理含离子液体的水体。因此,吸附是推荐的方法。目前虽然有采用活性炭吸附处理离子液体水体的文献报道,但活性炭吸附离子液体的能力普遍很低,如果以现有技术参数加以工业应用,将导致处理成本居高不下。At present, there are two main methods for the treatment of ionic liquid solutions. One is to destroy the structure of ionic liquids and convert ionic liquids into other harmless or low-toxic small molecules. Relevant measures include pyrolysis, chemical oxidation, and biological treatment; such methods cannot effectively recover resources of ionic liquids in water bodies. Another method is to effectively separate and recover ionic liquids from water, and the main measures include vacuum distillation, crystallization, extraction, and adsorption. Among them, the methods of vacuum distillation, crystallization and extraction are not suitable for large-scale treatment of water containing ionic liquids. Therefore, adsorption is the recommended method. At present, although there are reports in the literature on the use of activated carbon to adsorb and treat ionic liquid water, the ability of activated carbon to adsorb ionic liquid is generally very low. If it is applied industrially with the existing technical parameters, the treatment cost will remain high.

发明内容Contents of the invention

本发明需要解决的是离子液体(特别是亲水性离子液体)在活性炭上吸附量不高的问题。目前主要的改进方法是提高活性炭用量增加,这将导致处理成本提升。本发明通过在水体中添加少量磷酸盐,在不改变其它技术参数的条件下,能够实现了活性炭对离子液体吸附能力的显著提升。What the present invention needs to solve is the problem that the adsorption capacity of ionic liquids (especially hydrophilic ionic liquids) on activated carbon is not high. At present, the main improvement method is to increase the amount of activated carbon, which will lead to an increase in treatment costs. In the present invention, by adding a small amount of phosphate into the water body, the activated carbon can significantly improve the adsorption capacity of the ionic liquid without changing other technical parameters.

本发明的目的可以通过以下技术方案来实现:The purpose of the present invention can be achieved through the following technical solutions:

利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,向含有离子液体的水体中加入磷酸盐,充分混和并溶解;用活性炭吸附水体中的离子液体,在达到吸附平衡或吸附饱和后,首先用酸性洗脱剂洗脱离子液体,再用碱性溶液回调活性炭pH至大于8.0的弱碱性,使活性炭重复利用于下一轮吸附中。Using phosphate to promote the adsorption of activated carbon to remove ionic liquids in water, add phosphate to the water containing ionic liquids, fully mix and dissolve; use activated carbon to adsorb ionic liquids in water, after reaching adsorption equilibrium or adsorption saturation, first use The acidic eluent elutes the ionic liquid, and then the pH of the activated carbon is adjusted to a weak alkalinity greater than 8.0 with an alkaline solution, so that the activated carbon can be reused in the next round of adsorption.

水体中的离子液体包括咪唑类离子液体、吡啶类离子液体、季胺类离子液体、季膦类离子液体、吡咯烷类离子液体或哌啶类离子液体。The ionic liquid in water includes imidazole ionic liquid, pyridine ionic liquid, quaternary ammonium ionic liquid, quaternary phosphine ionic liquid, pyrrolidine ionic liquid or piperidine ionic liquid.

所述的磷酸盐包括磷酸钠、磷酸钾或磷酸铵。The phosphate includes sodium phosphate, potassium phosphate or ammonium phosphate.

投加磷酸盐后,水体中磷酸盐的摩尔浓度与离子液体摩尔浓度的比值维持在1/500至1/50的范围内。After the phosphate is added, the ratio of the molar concentration of the phosphate in the water to the molar concentration of the ionic liquid is maintained in the range of 1/500 to 1/50.

所述的酸性洗脱剂包括pH=1-3的盐酸或者硫酸溶液。The acid eluent includes hydrochloric acid or sulfuric acid solution with pH=1-3.

所述的碱性溶液包括pH=11-13的氢氧化钠或氢氧化钾水溶液。The alkaline solution includes sodium hydroxide or potassium hydroxide aqueous solution with pH=11-13.

活性炭吸附水体中的离子液体的方式为静态平衡吸附模式或动态柱吸附模式。The way activated carbon adsorbs ionic liquids in water is static equilibrium adsorption mode or dynamic column adsorption mode.

静态平衡吸附模式为:向一定量含离子液体的水体中投加少量磷酸盐,进一步投加一定质量的活性炭,充分振荡使得活性炭吸附离子液体达到平衡,将活性炭过滤取出,置入酸性洗脱剂中,被活性炭吸附的离子液体将脱附至酸性洗脱剂中,然后将活性炭从酸性洗脱剂中取出,置于碱性溶液中,将活性炭pH调为弱碱性,使活性炭重复利用。The static equilibrium adsorption mode is: add a small amount of phosphate to a certain amount of water containing ionic liquids, further add a certain quality of activated carbon, fully oscillate to make the activated carbon adsorb ionic liquids to reach equilibrium, filter out the activated carbon, and put in an acidic eluent In the process, the ionic liquid adsorbed by the activated carbon will be desorbed into the acidic eluent, then the activated carbon is taken out from the acidic eluent, placed in an alkaline solution, and the pH of the activated carbon is adjusted to be weakly alkaline, so that the activated carbon can be reused.

动态柱吸附模式为:在柱体内填充一定质量的活性炭,在稳定流速条件下,用含离子液体和少量磷酸盐的水体流经活性炭填充柱进行柱吸附,吸附达到饱和后将水体抽干,用1个床体积酸性洗脱剂洗脱吸附柱,再用1个床体积的蒸馏水洗脱吸附柱,离子液体达到脱附完全,进一步用1个床体积的碱性溶液淋洗吸附柱,将活性炭pH调回至弱碱性,使活性炭重复利用。The dynamic column adsorption mode is as follows: a certain quality of activated carbon is filled in the column, and under the condition of a stable flow rate, the water containing ionic liquid and a small amount of phosphate flows through the activated carbon-filled column for column adsorption. 1 bed volume of acidic eluent is used to elute the adsorption column, and then 1 bed volume of distilled water is used to elute the adsorption column. The pH is adjusted back to weak alkaline, so that the activated carbon can be reused.

静态平衡吸附模式或动态柱吸附模式的吸附条件可以参考常规活性炭吸附工艺。The adsorption conditions of static equilibrium adsorption mode or dynamic column adsorption mode can refer to the conventional activated carbon adsorption process.

本发明的原理为:三价磷酸盐具有盐析效应,能够通过静电作用强烈水合自由溶剂的水分子,从而有效降低水分子与离子液体的水合作用,进而降低水体中离子液体的溶解度。The principle of the invention is: the trivalent phosphate has a salting-out effect, and can strongly hydrate the water molecules of the free solvent through electrostatic action, thereby effectively reducing the hydration between the water molecules and the ionic liquid, and further reducing the solubility of the ionic liquid in the water body.

与现有技术相比,本发明只需在水体中投加少量的磷酸盐溶液,就可大大促进活性炭对离子液体的吸附效果,成本低廉,效果显著。Compared with the prior art, the present invention only needs to add a small amount of phosphate solution into the water body to greatly promote the adsorption effect of the activated carbon on the ionic liquid, and the cost is low and the effect is remarkable.

具体实施方式detailed description

下面结合具体实施例对本发明进行详细说明。The present invention will be described in detail below in conjunction with specific embodiments.

实施例1:Example 1:

磷酸钠促进活性炭静态吸附离子液体(1-乙基-3-甲基咪唑四氟硼酸盐)Sodium Phosphate Promotes Static Adsorption of Ionic Liquids (1-Ethyl-3-methylimidazolium Tetrafluoroborate) on Activated Carbon

【投加磷酸钠实验】具体步骤为:向待处理的1mmol/L的1-乙基-3-甲基咪唑四氟硼酸盐水溶液中投加少量磷酸钠,稳定后磷酸钠的浓度为0.01mmol/L。进一步投加一定量的粉末商品活性炭振荡24h,待吸附达到平衡后,测得活性炭对1-乙基-3-甲基咪唑四氟硼酸盐的饱和吸附量为40.6mg/g。置入pH=1的盐酸溶液中,1-乙基-3-甲基咪唑四氟硼酸盐可被酸溶液完全脱附。将活性炭置于pH=13的氢氧化钠水溶液中,可将活性炭pH调为10的弱碱性。活性炭可重复使用多次。[Dosing sodium phosphate experiment] The specific steps are: add a small amount of sodium phosphate to the 1mmol/L 1-ethyl-3-methylimidazolium tetrafluoroborate aqueous solution to be treated, and the concentration of sodium phosphate after stabilization is 0.01 mmol/L. A certain amount of powdered commercial activated carbon was further added and oscillated for 24 hours. After the adsorption reached equilibrium, the saturated adsorption capacity of activated carbon for 1-ethyl-3-methylimidazolium tetrafluoroborate was measured to be 40.6 mg/g. When placed in a hydrochloric acid solution with pH=1, 1-ethyl-3-methylimidazolium tetrafluoroborate can be completely desorbed by the acid solution. Put the activated carbon in the sodium hydroxide aqueous solution with pH = 13, and the pH of the activated carbon can be adjusted to a weak alkalinity of 10. Activated charcoal can be reused many times.

【不投加磷酸钠对比实验】具体步骤为:向待处理的1mmol/L的1-乙基-3-甲基咪唑四氟硼酸盐水溶液中投加一定量的粉末商品活性炭,振荡24h,待吸附达到平衡后,测得活性炭对1-乙基-3-甲基咪唑四氟硼酸盐的饱和吸附量为16.2mg/g,然后将活性炭取出,用蒸馏水洗净。置入pH=1的盐酸溶液中,吸附的离子液体全部脱附至酸溶液中。[Comparative experiment without adding sodium phosphate] The specific steps are: add a certain amount of powdered commercial activated carbon to the 1mmol/L 1-ethyl-3-methylimidazolium tetrafluoroborate aqueous solution to be treated, shake for 24h, After the adsorption reached equilibrium, it was measured that the saturated adsorption capacity of activated carbon to 1-ethyl-3-methylimidazolium tetrafluoroborate was 16.2 mg/g, and then the activated carbon was taken out and washed with distilled water. Putting it into a hydrochloric acid solution with pH=1, all the adsorbed ionic liquid will be desorbed into the acid solution.

比较投加磷酸钠前后活性炭的吸附量,投加前后活性炭对离子液体的吸附量提升约2.5倍,证明磷酸盐能够有效促进活性炭对离子液体的吸附。Comparing the adsorption capacity of activated carbon before and after adding sodium phosphate, the adsorption capacity of activated carbon on ionic liquids before and after adding sodium phosphate was increased by about 2.5 times, which proved that phosphate can effectively promote the adsorption of activated carbon on ionic liquids.

实施例2:Example 2:

磷酸铵促进活性炭静态吸附离子液体(N-丁基-3-甲基吡啶六氟磷酸盐)Ammonium Phosphate Facilitated Static Adsorption of Ionic Liquids on Activated Carbon (N-Butyl-3-methylpyridine Hexafluorophosphate)

【投加磷酸铵实验】具体步骤为:向待处理的1mmol/L的N-丁基-3-甲基吡啶六氟磷酸盐水溶液中投加少量磷酸铵,稳定后磷酸铵的浓度为0.01mmol/L。进一步投加将一定量的粉末商品活性炭振荡24h,待吸附达到平衡后,测得活性炭对N-丁基-3-甲基吡啶六氟磷酸盐的饱和吸附量为56.6mg/g。置入pH=1的硫酸溶液中,N-丁基-3-甲基吡啶六氟磷酸盐可被酸溶液完全脱附。将活性炭置于pH=13的氢氧化钾水溶液中,可将活性炭pH调为9.5弱碱性。活性炭可重复使用多次。[Ammonium phosphate addition experiment] The specific steps are: add a small amount of ammonium phosphate to the 1mmol/L N-butyl-3-methylpyridine hexafluorophosphate aqueous solution to be treated, and the concentration of ammonium phosphate after stabilization is 0.01mmol /L. Further add a certain amount of powdered commercial activated carbon and oscillate for 24 hours. After the adsorption reaches equilibrium, the saturated adsorption capacity of activated carbon for N-butyl-3-methylpyridine hexafluorophosphate is measured to be 56.6 mg/g. When placed in a sulfuric acid solution with pH=1, N-butyl-3-picoline hexafluorophosphate can be completely desorbed by the acid solution. Put the activated carbon in the potassium hydroxide aqueous solution with pH = 13, and the pH of the activated carbon can be adjusted to 9.5 weakly alkaline. Activated charcoal can be reused many times.

【不投加磷酸铵对比实验】具体步骤为:向待处理的1mmol/L的N-丁基-3-甲基吡啶六氟磷酸盐水溶液中投加一定量的粉末商品活性炭,振荡24h,待吸附达到平衡后,测得活性炭对N-丁基-3-甲基吡啶六氟磷酸盐的饱和吸附量为29.0mg/g,然后将活性炭取出,用蒸馏水洗净。置入pH=1的硫酸溶液中,吸附的离子液体全部脱附至酸溶液中。[Comparative experiment without adding ammonium phosphate] The specific steps are: add a certain amount of powdered commercial activated carbon to the 1mmol/L N-butyl-3-picoline hexafluorophosphate aqueous solution to be treated, shake for 24 hours, and wait for After the adsorption reaches equilibrium, the saturated adsorption capacity of N-butyl-3-picoline hexafluorophosphate measured by activated carbon is 29.0 mg/g, and then the activated carbon is taken out and washed with distilled water. Putting it into a sulfuric acid solution with pH=1, all the adsorbed ionic liquid will be desorbed into the acid solution.

比较投加磷酸铵前后活性炭的吸附量,投加前后活性炭对离子液体的吸附量提升约2.0倍,证明磷酸盐能够有效促进活性炭对离子液体的吸附。Comparing the adsorption capacity of activated carbon before and after adding ammonium phosphate, the adsorption capacity of activated carbon on ionic liquids before and after adding ammonium phosphate was increased by about 2.0 times, which proved that phosphate can effectively promote the adsorption of activated carbon on ionic liquids.

实施例3:Example 3:

活性炭柱动态吸附离子液体(1-乙基-3-甲基咪唑六氟磷酸盐)Dynamic adsorption of ionic liquid (1-ethyl-3-methylimidazolium hexafluorophosphate) on activated carbon column

【投加磷酸钾实验】具体步骤为:向待处理的1mmol/L的1-乙基-3-甲基咪唑六氟磷酸盐水溶液中投加少量磷酸钾,稳定后磷酸钾的浓度为0.01mmol/L。取10g颗粒活性炭填装内径1cm,高10cm的玻璃柱。在稳定流速下条件下,将上述溶液流经活性炭填充柱进行柱吸附,测得达到吸附饱和可处理的溶液体积为1600ml。将柱内的溶液抽干,加入1个床体积pH=1的盐酸溶液进行洗脱,再用1个床体积的蒸馏水洗脱吸附柱,1-乙基-3-甲基咪唑六氟磷酸盐可被完全脱附。再加入1个床体积pH=13的氢氧化钾水溶液,可将活性炭pH调为9.0的弱碱性。活性炭可重复使用多次。[Dosing potassium phosphate experiment] The specific steps are: add a small amount of potassium phosphate to the 1mmol/L 1-ethyl-3-methylimidazolium hexafluorophosphate aqueous solution to be treated, and the concentration of potassium phosphate after stabilization is 0.01mmol /L. Take 10g of granular activated carbon to fill a glass column with an inner diameter of 1cm and a height of 10cm. Under the condition of a steady flow rate, the above solution was flowed through an activated carbon packed column for column adsorption, and it was measured that the volume of the solution that reached adsorption saturation was 1600ml. Drain the solution in the column, add 1 bed volume of hydrochloric acid solution with pH=1 to elute, then use 1 bed volume of distilled water to elute the adsorption column, 1-ethyl-3-methylimidazole hexafluorophosphate can be completely desorbed. Then add 1 bed volume of potassium hydroxide aqueous solution with pH=13, the pH of activated carbon can be adjusted to weak alkalinity of 9.0. Activated charcoal can be reused many times.

【不投加磷酸钾对比实验】具体步骤为:不添加磷酸钾,其它处理操作与【投加磷酸钠实验】相同,测得达到吸附饱和可处理的溶液体积为500ml。[Comparative experiment without adding potassium phosphate] The specific steps are: without adding potassium phosphate, other treatment operations are the same as [experiment of adding sodium phosphate].

比较投加磷酸盐前后溶液处理量,投加前处理水量为500ml,投加后处理水量为1600ml,吸附处理量提升约3.2倍。Comparing the solution treatment volume before and after adding phosphate, the treatment water volume before dosing is 500ml, and the treatment water volume after dosing is 1600ml, and the adsorption treatment volume is increased by about 3.2 times.

实施例4:Example 4:

活性炭柱动态吸附离子液体(氯化N-丁基-3-甲基吡啶)Dynamic adsorption of ionic liquid (N-butyl-3-picoline chloride) on activated carbon column

【投加磷酸钠实验】具体步骤为:向待处理的1mmol/L的氯化N-丁基-3-甲基吡啶水溶液中投加少量磷酸钠,稳定后磷酸钠的浓度为0.01mmol/L。取10g颗粒活性炭填装内径1cm,高10cm的玻璃柱。在稳定流速下条件下,将上述溶液流经活性炭填充柱进行柱吸附,测得达到吸附饱和可处理的溶液体积为2000ml。将柱内的溶液抽干,加入1个床体积pH=1的硫酸溶液进行洗脱,再用1个床体积的蒸馏水洗脱吸附柱,N-丁基-3-甲基吡啶可被完全脱附。再加入1个床体积pH=13的氢氧化钠水溶液,可将活性炭pH调为pH9.5的弱碱性。活性炭可重复使用多次。[Dosing sodium phosphate experiment] The specific steps are: add a small amount of sodium phosphate to the 1mmol/L aqueous solution of N-butyl-3-picoline chloride to be treated, and the concentration of sodium phosphate after stabilization is 0.01mmol/L . Take 10g of granular activated carbon to fill a glass column with an inner diameter of 1cm and a height of 10cm. Under the condition of a steady flow rate, the above solution was flowed through an activated carbon packed column for column adsorption, and it was measured that the volume of the solution that reached adsorption saturation was 2000 ml. Drain the solution in the column, add 1 bed volume of sulfuric acid solution with pH=1 for elution, then use 1 bed volume of distilled water to elute the adsorption column, N-butyl-3-picoline can be completely removed attached. Then add 1 bed volume of sodium hydroxide aqueous solution with pH=13, the pH of activated carbon can be adjusted to the weak alkalinity of pH9.5. Activated charcoal can be reused many times.

【不投加磷酸钠对比实验】具体步骤为:不添加磷酸钠,其它处理操作与【投加磷酸钠实验】相同,测得达到吸附饱和可处理的溶液体积为600ml。[Comparative experiment without adding sodium phosphate] The specific steps are: without adding sodium phosphate, other treatment operations are the same as [experiment of adding sodium phosphate].

比较投加磷酸盐前后溶液处理量,投加前处理水量为600ml,投加后处理水量为2000ml,吸附处理量提升3.3倍。Comparing the solution treatment volume before and after adding phosphate, the treatment water volume before dosing is 600ml, and the treatment water volume after dosing is 2000ml, and the adsorption treatment volume is increased by 3.3 times.

实施例5Example 5

利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,Utilize phosphate to promote activated carbon adsorption to remove the method of ionic liquid in water body,

磷酸钠促进活性炭静态吸附离子液体(1-乙基-3-甲基咪唑四氟硼酸盐)Sodium Phosphate Promotes Static Adsorption of Ionic Liquids (1-Ethyl-3-methylimidazolium Tetrafluoroborate) on Activated Carbon

【投加磷酸钠实验】具体步骤为:向待处理的1mmol/L的1-乙基-3-甲基咪唑四氟硼酸盐水溶液中投加少量磷酸钠,稳定后磷酸钠的浓度为0.002mmol/L。进一步投加一定量的粉末商品活性炭振荡24h,待吸附达到平衡后,测得活性炭对1-乙基-3-甲基咪唑四氟硼酸盐的饱和吸附量为28.8mg/g。置入pH=3的硫酸溶液中,1-乙基-3-甲基咪唑四氟硼酸盐可被酸溶液完全脱附。将活性炭置于pH=13的氢氧化钾水溶液中,可将活性炭pH调为10的弱碱性。活性炭可重复使用多次。[Dosing sodium phosphate experiment] The specific steps are: add a small amount of sodium phosphate to the 1mmol/L 1-ethyl-3-methylimidazolium tetrafluoroborate aqueous solution to be treated, and the concentration of sodium phosphate after stabilization is 0.002 mmol/L. A certain amount of powdered commercial activated carbon was further added and oscillated for 24 hours. After the adsorption reached equilibrium, the saturated adsorption capacity of activated carbon for 1-ethyl-3-methylimidazolium tetrafluoroborate was measured to be 28.8 mg/g. When placed in a sulfuric acid solution with pH=3, 1-ethyl-3-methylimidazolium tetrafluoroborate can be completely desorbed by the acid solution. Put the activated carbon in the potassium hydroxide aqueous solution with pH = 13, and the pH of the activated carbon can be adjusted to a weak alkalinity of 10. Activated charcoal can be reused many times.

【不投加磷酸钠对比实验】具体步骤为:向待处理的1mmol/L的1-乙基-3-甲基咪唑四氟硼酸盐水溶液中投加一定量的粉末商品活性炭,振荡24h,待吸附达到平衡后,测得活性炭对1-乙基-3-甲基咪唑四氟硼酸盐的饱和吸附量为16.2mg/g,然后将活性炭取出,用蒸馏水洗净。置入pH=3的硫酸溶液中,吸附的离子液体全部脱附至酸溶液中。[Comparative experiment without adding sodium phosphate] The specific steps are: add a certain amount of powdered commercial activated carbon to the 1mmol/L 1-ethyl-3-methylimidazolium tetrafluoroborate aqueous solution to be treated, shake for 24h, After the adsorption reached equilibrium, it was measured that the saturated adsorption capacity of activated carbon to 1-ethyl-3-methylimidazolium tetrafluoroborate was 16.2 mg/g, and then the activated carbon was taken out and washed with distilled water. When placed in a sulfuric acid solution with pH=3, all the adsorbed ionic liquids are desorbed into the acid solution.

比较投加磷酸钠前后活性炭的吸附量,投加前后活性炭对离子液体的吸附量提升约1.8倍,证明磷酸盐能够有效促进活性炭对离子液体的吸附。Comparing the adsorption capacity of activated carbon before and after adding sodium phosphate, the adsorption capacity of activated carbon on ionic liquids before and after adding sodium phosphate was increased by about 1.8 times, which proved that phosphate can effectively promote the adsorption of activated carbon on ionic liquids.

实施例6Example 6

利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,Utilize phosphate to promote activated carbon adsorption to remove the method of ionic liquid in water body,

磷酸钠促进活性炭静态吸附离子液体(1-乙基-3-甲基咪唑四氟硼酸盐)Sodium Phosphate Promotes Static Adsorption of Ionic Liquids (1-Ethyl-3-methylimidazolium Tetrafluoroborate) on Activated Carbon

【投加磷酸钠实验】具体步骤为:向待处理的1mmol/L的1-乙基-3-甲基咪唑四氟硼酸盐水溶液中投加少量磷酸钠,稳定后磷酸钠的浓度为0.002mmol/L。进一步投加一定量的粉末商品活性炭振荡24h,待吸附达到平衡后,测得活性炭对1-乙基-3-甲基咪唑四氟硼酸盐的饱和吸附量为50.5mg/g。置入pH=2的盐酸溶液中,1-乙基-3-甲基咪唑四氟硼酸盐可被酸溶液完全脱附。将活性炭置于pH=12的氢氧化钠水溶液中,可将活性炭pH调为10的弱碱性。活性炭可重复使用多次。[Dosing sodium phosphate experiment] The specific steps are: add a small amount of sodium phosphate to the 1mmol/L 1-ethyl-3-methylimidazolium tetrafluoroborate aqueous solution to be treated, and the concentration of sodium phosphate after stabilization is 0.002 mmol/L. A certain amount of powdered commercial activated carbon was further added and oscillated for 24 hours. After the adsorption reached equilibrium, the saturated adsorption capacity of activated carbon for 1-ethyl-3-methylimidazolium tetrafluoroborate was measured to be 50.5 mg/g. When placed in a hydrochloric acid solution with pH=2, 1-ethyl-3-methylimidazolium tetrafluoroborate can be completely desorbed by the acid solution. Put the activated carbon in the sodium hydroxide aqueous solution with pH = 12, and the pH of the activated carbon can be adjusted to a weak alkalinity of 10. Activated charcoal can be reused many times.

【不投加磷酸钠对比实验】具体步骤为:向待处理的1mmol/L的1-乙基-3-甲基咪唑四氟硼酸盐水溶液中投加一定量的粉末商品活性炭,振荡24h,待吸附达到平衡后,测得活性炭对1-乙基-3-甲基咪唑四氟硼酸盐的饱和吸附量为16.2mg/g,然后将活性炭取出,用蒸馏水洗净。置入pH=2的盐酸溶液中,吸附的离子液体全部脱附至酸溶液中。[Comparative experiment without adding sodium phosphate] The specific steps are: add a certain amount of powdered commercial activated carbon to the 1mmol/L 1-ethyl-3-methylimidazolium tetrafluoroborate aqueous solution to be treated, shake for 24h, After the adsorption reached equilibrium, it was measured that the saturated adsorption capacity of activated carbon to 1-ethyl-3-methylimidazolium tetrafluoroborate was 16.2 mg/g, and then the activated carbon was taken out and washed with distilled water. When placed in a hydrochloric acid solution with pH=2, all the adsorbed ionic liquids are desorbed into the acid solution.

比较投加磷酸钠前后活性炭的吸附量,投加前后活性炭对离子液体的吸附量提升约3.1倍,证明磷酸盐能够有效促进活性炭对离子液体的吸附。Comparing the adsorption capacity of activated carbon before and after adding sodium phosphate, the adsorption capacity of activated carbon on ionic liquids before and after adding sodium phosphate was increased by about 3.1 times, which proved that phosphate can effectively promote the adsorption of activated carbon on ionic liquids.

上述的对实施例的描述是为便于该技术领域的普通技术人员能理解和使用发明。熟悉本领域技术的人员显然可以容易地对这些实施例做出各种修改,并把在此说明的一般原理应用到其他实施例中而不必经过创造性的劳动。因此,本发明不限于上述实施例,本领域技术人员根据本发明的揭示,不脱离本发明范畴所做出的改进和修改都应该在本发明的保护范围之内。The above descriptions of the embodiments are for those of ordinary skill in the art to understand and use the invention. It is obvious that those skilled in the art can easily make various modifications to these embodiments, and apply the general principles described here to other embodiments without creative efforts. Therefore, the present invention is not limited to the above-mentioned embodiments. Improvements and modifications made by those skilled in the art according to the disclosure of the present invention without departing from the scope of the present invention should fall within the protection scope of the present invention.

Claims (9)

1.利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,其特征在于,1. Utilize phosphate to promote the method for activated carbon adsorption to remove ionic liquid in water body, it is characterized in that, 向含有离子液体的水体中加入磷酸盐,充分混和并溶解;Add phosphate to the water body containing the ionic liquid, mix well and dissolve; 用活性炭吸附水体中的离子液体,在达到吸附平衡或吸附饱和后,首先用酸性洗脱剂洗脱离子液体,再用碱性溶液回调活性炭pH至大于8.0的弱碱性范围,使活性炭重复利用于下一轮吸附中。Use activated carbon to adsorb the ionic liquid in the water body. After reaching the adsorption equilibrium or adsorption saturation, first use the acidic eluent to elute the ionic liquid, and then use the alkaline solution to adjust the pH of the activated carbon to a weak alkaline range greater than 8.0, so that the activated carbon can be reused in the next round of adsorption. 2.根据权利要求1所述的利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,其特征在于,水体中的离子液体包括咪唑类离子液体、吡啶类离子液体、季胺类离子液体、季膦类离子液体、吡咯烷类离子液体或哌啶类离子液体。2. the method utilizing phosphate to promote activated carbon adsorption and removal of ionic liquid in water according to claim 1, is characterized in that, the ionic liquid in water comprises imidazole ionic liquid, pyridine ionic liquid, quaternary ammonium ionic liquid, quaternary ionic liquid Phosphine-based ionic liquid, pyrrolidine-based ionic liquid or piperidine-based ionic liquid. 3.根据权利要求1所述的利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,其特征在于,所述的磷酸盐包括磷酸钠、磷酸钾或磷酸铵。3. The method for utilizing phosphate to promote activated carbon adsorption and removal of ionic liquid in water according to claim 1, wherein said phosphate comprises sodium phosphate, potassium phosphate or ammonium phosphate. 4.根据权利要求1所述的利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,其特征在于,投加磷酸盐后,水体中磷酸盐的摩尔浓度与离子液体摩尔浓度的比值为1/500至1/50。4. the method utilizing phosphate to promote activated carbon adsorption and removal of ionic liquid in water according to claim 1, is characterized in that, after adding phosphate, the ratio of the molar concentration of phosphate and the molar concentration of ionic liquid in the water body is 1/ 500 to 1/50. 5.根据权利要求1所述的利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,其特征在于,所述的酸性洗脱剂包括pH=1-3的盐酸或者硫酸溶液。5 . The method for utilizing phosphate to promote adsorption and removal of ionic liquids in water by activated carbon according to claim 1 , wherein the acidic eluent comprises hydrochloric acid or sulfuric acid solution with a pH of 1-3. 6.根据权利要求1所述的利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,其特征在于,所述的碱性溶液包括pH=11-13的氢氧化钠或氢氧化钾水溶液。6. The method for utilizing phosphate to promote adsorption of activated carbon to remove ionic liquids in water according to claim 1, wherein the alkaline solution comprises an aqueous solution of sodium hydroxide or potassium hydroxide with a pH of 11-13. 7.根据权利要求1所述的利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,其特征在于,活性炭吸附水体中的离子液体的方式为静态平衡吸附模式或动态柱吸附模式。7. The method for utilizing phosphate to promote activated carbon adsorption and removal of ionic liquids in water bodies according to claim 1, characterized in that the mode of activated carbon adsorption of ionic liquids in water bodies is a static equilibrium adsorption mode or a dynamic column adsorption mode. 8.根据权利要求7所述的利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,其特征在于,静态平衡吸附模式为:向一定量含离子液体的水体中投加少量磷酸盐,进一步投加一定质量的活性炭,充分振荡使得活性炭吸附离子液体达到平衡,将活性炭过滤取出,置入酸性洗脱剂中,被活性炭吸附的离子液体将脱附至酸性洗脱剂中,然后将活性炭从酸性洗脱剂中取出,置于碱性溶液中,将活性炭pH调为大于8.0的弱碱性,使活性炭重复利用。8. the method for utilizing phosphate to promote activated carbon adsorption and removal of ionic liquid in water according to claim 7, characterized in that, the static equilibrium adsorption mode is: add a small amount of phosphate to a certain amount of water containing ionic liquid, and further add Add a certain amount of activated carbon, fully oscillate to make the activated carbon adsorb the ionic liquid to reach equilibrium, filter the activated carbon, put it into the acidic eluent, the ionic liquid adsorbed by the activated carbon will be desorbed into the acidic eluent, and then remove the activated carbon from the acidic eluent Take it out from the eluent, place it in an alkaline solution, and adjust the pH of the activated carbon to a weak alkaline greater than 8.0, so that the activated carbon can be reused. 9.根据权利要求7所述的利用磷酸盐促进活性炭吸附去除水体中离子液体的方法,其特征在于,动态柱吸附模式为:在柱体内填充一定质量的活性炭,在稳定流速条件下,用含离子液体和少量磷酸盐的水体流经活性炭填充柱进行柱吸附,吸附达到饱和后将水体抽干,用1个床体积酸性洗脱剂洗脱吸附柱,再用1个床体积的蒸馏水洗脱吸附柱,离子液体达到脱附完全,进一步用1个床体积的碱性溶液淋洗吸附柱,将活性炭pH调回至大于8.0的弱碱性,使活性炭重复利用。9. the method for utilizing phosphate to promote activated carbon adsorption and removal of ionic liquids in water according to claim 7, characterized in that, the dynamic column adsorption mode is: fill a certain quality of activated carbon in the column, under the condition of steady flow rate, use The water body of ionic liquid and a small amount of phosphate flows through the activated carbon packed column for column adsorption. After the adsorption reaches saturation, the water body is drained, and the adsorption column is eluted with 1 bed volume of acidic eluent, and then 1 bed volume of distilled water. The adsorption column, the ionic liquid is completely desorbed, and the adsorption column is further rinsed with a bed volume of alkaline solution, and the pH of the activated carbon is adjusted back to a weak alkalinity greater than 8.0, so that the activated carbon can be reused.
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