CN115228437B - A surface modification method to make the surface of activated carbon positively charged - Google Patents
A surface modification method to make the surface of activated carbon positively charged Download PDFInfo
- Publication number
- CN115228437B CN115228437B CN202210992876.3A CN202210992876A CN115228437B CN 115228437 B CN115228437 B CN 115228437B CN 202210992876 A CN202210992876 A CN 202210992876A CN 115228437 B CN115228437 B CN 115228437B
- Authority
- CN
- China
- Prior art keywords
- activated carbon
- hydrochloric acid
- quinoline
- modification method
- concentrated hydrochloric
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 216
- 238000002715 modification method Methods 0.000 title claims abstract description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 49
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 claims abstract description 42
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 239000008367 deionised water Substances 0.000 claims description 15
- 229910021641 deionized water Inorganic materials 0.000 claims description 15
- MMKYUTRZRJHJRT-UHFFFAOYSA-N CN1C2=CC=CC=C2C=CC1.Cl Chemical group CN1C2=CC=CC=C2C=CC1.Cl MMKYUTRZRJHJRT-UHFFFAOYSA-N 0.000 claims description 13
- 238000006243 chemical reaction Methods 0.000 claims description 10
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 6
- 238000012546 transfer Methods 0.000 claims description 6
- 238000005292 vacuum distillation Methods 0.000 claims description 6
- 238000001027 hydrothermal synthesis Methods 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 3
- 230000007935 neutral effect Effects 0.000 claims description 2
- 235000011837 pasties Nutrition 0.000 claims 1
- 238000002791 soaking Methods 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 25
- SNGREZUHAYWORS-UHFFFAOYSA-N perfluorooctanoic acid Chemical compound OC(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F SNGREZUHAYWORS-UHFFFAOYSA-N 0.000 abstract description 21
- 239000007864 aqueous solution Substances 0.000 abstract description 6
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- 238000011065 in-situ storage Methods 0.000 abstract description 3
- 230000002378 acidificating effect Effects 0.000 abstract description 2
- 238000006555 catalytic reaction Methods 0.000 abstract 1
- 230000005611 electricity Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 14
- -1 perfluorooctanoate anion Chemical class 0.000 description 9
- 230000000694 effects Effects 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- LTVDFSLWFKLJDQ-UHFFFAOYSA-N α-tocopherolquinone Chemical compound CC(C)CCCC(C)CCCC(C)CCCC(C)(O)CCC1=C(C)C(=O)C(C)=C(C)C1=O LTVDFSLWFKLJDQ-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 125000000524 functional group Chemical group 0.000 description 3
- 239000005457 ice water Substances 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000011068 loading method Methods 0.000 description 3
- 229910021645 metal ion Inorganic materials 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000012512 characterization method Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 230000002209 hydrophobic effect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000000967 suction filtration Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- SNGREZUHAYWORS-UHFFFAOYSA-M 2,2,3,3,4,4,5,5,6,6,7,7,8,8,8-pentadecafluorooctanoate Chemical compound [O-]C(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F SNGREZUHAYWORS-UHFFFAOYSA-M 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- YOALFLHFSFEMLP-UHFFFAOYSA-N azane;2,2,3,3,4,4,5,5,6,6,7,7,8,8,8-pentadecafluorooctanoic acid Chemical compound [NH4+].[O-]C(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F YOALFLHFSFEMLP-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- XIVLWOXCLOIZSW-UHFFFAOYSA-M chloromethyl-(2-hydroxypropyl)-dimethylazanium;chloride Chemical group [Cl-].CC(O)C[N+](C)(C)CCl XIVLWOXCLOIZSW-UHFFFAOYSA-M 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 210000003238 esophagus Anatomy 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 210000003734 kidney Anatomy 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 210000004994 reproductive system Anatomy 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000000870 ultraviolet spectroscopy Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28011—Other properties, e.g. density, crush strength
Landscapes
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
Description
技术领域Technical field
本发明涉及吸附材料技术领域,具体涉及一种使活性炭表面呈正电性的表面修饰方法。The present invention relates to the technical field of adsorbent materials, and in particular to a surface modification method for making the surface of activated carbon positively charged.
背景技术Background technique
全氟辛酸(PFOA)具有独特的热稳定性、化学稳定性和高表面活性,被广泛应用于许多日常和工业品的生产。由于PFOA的C–F键具有极其高的键能,使得PFOA分子难以被光解、水解以及生物降解。已有研究表明,PFOA能通过呼吸道、食道等进入到人体,对人们的生殖系统、肝脏和肾脏造成严重损伤,甚至可能致癌。因此,探索快速、高效、低成本的PFOA去除方法,对生态环境保护以及人类的健康具有重要的意义。Perfluorooctanoic acid (PFOA) has unique thermal stability, chemical stability and high surface activity, and is widely used in the production of many daily and industrial products. Because the C–F bond of PFOA has extremely high bond energy, it is difficult for PFOA molecules to be photolyzed, hydrolyzed, and biodegraded. Studies have shown that PFOA can enter the human body through the respiratory tract, esophagus, etc., causing serious damage to people's reproductive system, liver and kidneys, and may even cause cancer. Therefore, exploring fast, efficient, and low-cost PFOA removal methods is of great significance to ecological environment protection and human health.
活性炭是最为常见的炭吸附材料。PFOA分子尺寸较大,具有一定的疏水特性,且在溶液中以全氟辛酸根阴离子的形式存在。因此,利用吸附剂的疏水作用和静电吸附作用除去水溶液中的PFOA是最有效的方法。然而,普通活性炭表面含有大量含氧官能团,这些官能团使得活性炭的表面在水溶液中呈负电性,而全氟辛酸根离子在水溶液中也为负电性,两者极易产生排斥而导致活性炭对全氟辛酸根离子的吸附性能降低。现有技术也考虑在活性炭表面接枝或负载其他使活性炭呈正电的化合物,例如负载金属阳离子,或者接枝3-氯-2-羟基丙基三甲氯化铵等,以达到提升吸附效果的目的,但负载的金属离子容易从活性炭表面脱落造成二次污染,环氧接枝的季铵盐的长碳链会增加PFOA吸附的空间位阻(原子电子云重叠,表现为斥力),从而影响其吸附PFOA性能的提高。Activated carbon is the most common carbon adsorption material. PFOA has a large molecular size, has certain hydrophobic properties, and exists in the form of perfluorooctanoate anion in the solution. Therefore, using the hydrophobic effect and electrostatic adsorption of adsorbents to remove PFOA from aqueous solutions is the most effective method. However, the surface of ordinary activated carbon contains a large number of oxygen-containing functional groups. These functional groups make the surface of activated carbon electronegative in aqueous solution, and perfluorooctanoate ions are also electronegative in aqueous solution. The two are easily repulsive, resulting in the activated carbon's rejection of perfluorooctanoate ions. Adsorption performance is reduced. Existing technology also considers grafting or loading other compounds that make activated carbon positively charged on the surface of activated carbon, such as loading metal cations, or grafting 3-chloro-2-hydroxypropyltrimethylammonium chloride, etc., to achieve the purpose of improving the adsorption effect. , but the loaded metal ions are easy to fall off from the surface of activated carbon, causing secondary pollution. The long carbon chain of the epoxy-grafted quaternary ammonium salt will increase the steric hindrance of PFOA adsorption (atom electron cloud overlap, manifested as repulsion), thus affecting its Improvement of PFOA adsorption performance.
发明内容Contents of the invention
针对现有技术存在的上述不足,本发明的目的在于提供一种使活性炭在水溶液中表面呈正电性的修饰方法,以解决现有技术活性炭对水体中全氟辛酸吸附效果不好、在活性炭表面负载的化合物容易脱落的问题。In view of the above-mentioned deficiencies in the prior art, the purpose of the present invention is to provide a method for modifying the surface of activated carbon to be positively charged in an aqueous solution, so as to solve the problem of poor adsorption effect of activated carbon on perfluorooctanoic acid in water and loading on the surface of activated carbon. The compound easily falls off.
为了解决上述技术问题,本发明采用如下技术方案:In order to solve the above technical problems, the present invention adopts the following technical solutions:
一种使活性炭表面呈正电性的表面修饰方法,具体包括以下步骤:A surface modification method to make the surface of activated carbon electropositive, specifically including the following steps:
步骤1:对活性炭进行筛选,再用去离子水清洗,然后加热干燥后备用;Step 1: Screen the activated carbon, wash it with deionized water, and then heat and dry it for later use;
步骤2:将步骤1得到的活性炭加入浓度为1 mol/L的盐酸中浸泡,然后洗涤干净后干燥至恒重;Step 2: Add the activated carbon obtained in step 1 to soak in hydrochloric acid with a concentration of 1 mol/L, then wash it and dry it to constant weight;
步骤3:向步骤2得到的活性炭中加入喹啉;活性炭与喹啉的比例为1g:(0.5~3.5)mL,并轻微搅拌0.5~1 h,使活性炭充分吸附喹啉;Step 3: Add quinoline to the activated carbon obtained in step 2; the ratio of activated carbon to quinoline is 1g: (0.5~3.5) mL, and stir slightly for 0.5~1 h to allow the activated carbon to fully adsorb quinoline;
步骤4:向步骤3的混合物中缓慢加入浓盐酸,加入的浓盐酸摩尔数为喹啉摩尔数的3-5倍,浓盐酸滴加完毕后,并轻微搅拌0.5~1 h,使活性炭充分吸附浓盐酸;Step 4: Slowly add concentrated hydrochloric acid to the mixture in step 3. The number of moles of concentrated hydrochloric acid added is 3-5 times the number of moles of quinoline. After the dropwise addition of concentrated hydrochloric acid is completed, stir slightly for 0.5-1 h to allow the activated carbon to fully adsorb. Concentrated hydrochloric acid;
步骤5:将步骤4得到的混合物置于45℃条件下减压蒸馏;Step 5: Distill the mixture obtained in Step 4 under reduced pressure at 45°C;
步骤6:将步骤5得到的产物转移至水热反应釜中,并加入甲醇混合均匀后密闭,在145-180℃条件下反应6-12 h;其中,甲醇加入的摩尔数为喹啉摩尔数的2-3倍;Step 6: Transfer the product obtained in step 5 to the hydrothermal reaction kettle, add methanol, mix evenly, seal it, and react at 145-180°C for 6-12 hours; where the number of moles of methanol added is the number of moles of quinoline 2-3 times;
步骤7:待反应釜冷却后,将反应釜中的产物取出,并在70℃条件下减压蒸馏,除去未反应的甲醇;Step 7: After the reaction kettle is cooled, take out the product in the reaction kettle and distill it under reduced pressure at 70°C to remove unreacted methanol;
步骤8:将步骤7处理后的活性炭先用无水乙醇反复洗涤,再用去离子水反复洗涤,然后对其进行干燥后,得到氯化-1-甲基喹啉修饰后的活性炭。Step 8: Wash the activated carbon treated in step 7 repeatedly with absolute ethanol and then with deionized water, and then dry it to obtain activated carbon modified with 1-methylquinoline chloride.
在现有技术中,为了提高活性炭的吸附PFOA的性能,往往是在活性炭表面直接负载金属离子或者接枝3-氯-2-羟基丙基三甲氯化铵等化合物。但是金属离子容易脱落,而3-氯-2-羟基丙基三甲氯化铵的长链结构会增加污染物吸附的空间位阻,堵塞活性炭的微孔,从而会对活性炭的吸附性能的提高带来不利的影响。本发明通过在活性炭表面原位合成非长链结构的季铵盐——氯化-1-甲基喹啉,不仅能增大活性炭对全氟辛酸根离子的吸附量,也提升了活性炭对全氟辛酸根离子的吸附速度,从而改善了活性炭对全氟辛酸根离子的吸附效果。In the prior art, in order to improve the PFOA adsorption performance of activated carbon, metal ions are often directly loaded on the surface of activated carbon or compounds such as 3-chloro-2-hydroxypropyltrimethylammonium chloride are grafted. However, metal ions are easy to fall off, and the long-chain structure of 3-chloro-2-hydroxypropyltrimethylammonium chloride will increase the steric hindrance of pollutant adsorption and block the micropores of activated carbon, which will affect the improvement of the adsorption performance of activated carbon. have adverse effects. By in-situ synthesizing the quaternary ammonium salt with a non-long-chain structure, 1-methylquinoline chloride, on the surface of activated carbon, the present invention can not only increase the adsorption capacity of perfluorooctanoate ions by activated carbon, but also improve the adsorption capacity of perfluorooctanoate ions by activated carbon. The adsorption speed of activated carbon improves the adsorption effect of perfluorooctanoate ions on activated carbon.
与现有技术相比,本发明具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
1、本发明所述方法采用先将活性炭用酸预处理,一是洗掉活性炭制备过程中留下的无机盐和灰分,产生了新的孔隙,增大了活性炭的比表面积;二是使活性炭的酸性含氧官能团增加,利用喹啉的碱性,既能使喹啉被吸附在活性炭的表面,不易从活性炭表面脱落,又能提升活性炭对全氟辛酸的吸附效果。1. The method of the present invention adopts the method of first pretreating activated carbon with acid. First, the inorganic salts and ash left during the preparation process of activated carbon are washed away, creating new pores and increasing the specific surface area of activated carbon; second, making the activated carbon The acidic oxygen-containing functional groups are increased, and the alkalinity of quinoline is used to not only make quinoline adsorbed on the surface of activated carbon and not easily fall off from the surface of activated carbon, but also improve the adsorption effect of activated carbon on perfluorooctanoic acid.
2、本发明所述方法中采用的是浓盐酸而非HCl气体作为催化剂,通过减压蒸馏除去水分,避免HCl气体带来的环境污染,以及运输和储存不便的问题。2. In the method of the present invention, concentrated hydrochloric acid is used as a catalyst instead of HCl gas, and water is removed through vacuum distillation to avoid environmental pollution caused by HCl gas and inconvenient transportation and storage problems.
附图说明Description of the drawings
图1为未改性的活性炭SEM图。Figure 1 shows the SEM image of unmodified activated carbon.
图2为示例2得到的氯化-1-甲基喹啉修饰后的活性炭图。Figure 2 is a diagram of activated carbon modified with 1-methylquinoline chloride obtained in Example 2.
图3为活性炭吸附PFOA性能评价图。Figure 3 is an evaluation chart of the performance evaluation of activated carbon adsorption of PFOA.
具体实施方式Detailed ways
下面将结合附图和示例对本发明作进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and examples.
一、示例1. Example
示例1Example 1
(1)将活性炭用标准筛筛分,筛选出粒径为20-60目活性炭,用去离子水清洗3-6次,以除去活性炭表面杂质与粉尘,然后在110℃的鼓风干燥箱内干燥至恒重,冷却至室温后将装入样品袋;(1) Sieve the activated carbon with a standard sieve to screen out activated carbon with a particle size of 20-60 mesh, wash it with deionized water 3-6 times to remove impurities and dust on the surface of the activated carbon, and then place it in a blast drying oven at 110°C Dry to constant weight, cool to room temperature and then put into sample bag;
(2)将步骤(1)得到的5 g活性炭放置于烧杯中,加入400 mL浓度为1 mol/L的盐酸,室温下浸泡24 h。然后用去离子水洗涤和抽滤3-6次,干燥至恒重;(2) Place 5 g of activated carbon obtained in step (1) into a beaker, add 400 mL of hydrochloric acid with a concentration of 1 mol/L, and soak at room temperature for 24 hours. Then wash with deionized water and suction filter 3-6 times, and dry to constant weight;
(3)称取步骤(2)得到的活性炭2.5g加入三颈烧瓶中,将三颈烧瓶置于冰水浴中,控制三颈烧瓶内的温度不超过50℃;然后滴加2 mL的喹啉。(3) Weigh 2.5g of the activated carbon obtained in step (2) and add it to the three-necked flask. Place the three-necked flask in an ice water bath and control the temperature in the three-necked flask to not exceed 50°C; then add 2 mL of quinoline dropwise. .
(4)待活性炭吸附喹啉0.5 h后,通过滴液漏斗向三颈烧瓶缓慢滴加4.2 mL的浓盐酸;(4) After the activated carbon adsorbs quinoline for 0.5 h, slowly add 4.2 mL of concentrated hydrochloric acid dropwise to the three-neck flask through the dropping funnel;
(5)待滴加完浓盐酸0.5 h后,将三颈烧瓶中放置于45℃恒温水浴锅中,进行减压蒸馏;(5) After adding concentrated hydrochloric acid dropwise for 0.5 h, place the three-neck flask in a 45°C constant temperature water bath and perform vacuum distillation;
(6)减压蒸馏完毕后,将三颈烧瓶中的活性炭和溶液全部转移至水热合成反应釜中,再分别加入1.37 mL的甲醇,用玻璃棒轻微搅拌均匀后密闭,放入置于145℃烘箱中反应6 h;(6) After the vacuum distillation is completed, transfer all the activated carbon and solution in the three-neck flask to the hydrothermal synthesis reaction kettle, then add 1.37 mL of methanol respectively, stir slightly with a glass rod, seal it, and place it at 145 React in oven at ℃ for 6 hours;
(7)取出反应釜,自然冷却至室温后将活性炭和液体转移至三颈烧瓶中,在70℃下,减压蒸馏,蒸馏除去未反应的甲醇;(7) Take out the reaction kettle, cool it naturally to room temperature, transfer the activated carbon and liquid to a three-neck flask, and distill under reduced pressure at 70°C to remove unreacted methanol;
(8)将活性炭先用无水乙醇抽滤洗涤3-6次,再用去离子水抽滤洗涤3-6次,然后再得到的活性炭放入70℃烘箱中干燥至恒重,得氯化-1-甲基喹啉修饰后的活性炭。(8) First filter and wash the activated carbon with absolute ethanol 3-6 times, then use deionized water to filter and wash it 3-6 times, and then put the obtained activated carbon into a 70°C oven to dry to constant weight to obtain chlorination -1-Methylquinoline modified activated carbon.
其中,氯化-1-甲基喹啉的结构式为:Among them, the structural formula of 1-methylquinoline chloride is:
示例2Example 2
(1)将活性炭用标准筛筛分,筛选出粒径为20-60目活性炭,用去离子水清洗3-6次,以除去活性炭表面杂质与粉尘,然后在110℃的鼓风干燥箱内干燥至恒重,冷却至室温后将装入样品袋;(1) Sieve the activated carbon with a standard sieve to screen out activated carbon with a particle size of 20-60 mesh, wash it with deionized water 3-6 times to remove impurities and dust on the surface of the activated carbon, and then place it in a blast drying oven at 110°C Dry to constant weight, cool to room temperature and then put into sample bag;
(2)将步骤(1)得到的5 g 活性炭放置于烧杯中,加入400 mL浓度为1mol/L的盐酸,室温下浸泡24 h。然后用去离子水洗涤和抽滤3-6次,干燥至恒重;(2) Place 5 g of activated carbon obtained in step (1) into a beaker, add 400 mL of hydrochloric acid with a concentration of 1 mol/L, and soak at room temperature for 24 hours. Then wash with deionized water and suction filter 3-6 times, and dry to constant weight;
(3)称取步骤(2)得到的活性炭2.5 g加入三颈烧瓶中,将三颈烧瓶置于冰水浴中,冰水浴控制三颈烧瓶内的温度不超过50℃;然后滴加6.5 mL的喹啉。(3) Weigh 2.5 g of the activated carbon obtained in step (2) and add it to the three-neck flask. Place the three-neck flask in an ice water bath. The ice water bath controls the temperature in the three-neck flask to not exceed 50°C; then add 6.5 mL dropwise quinoline.
(4)待活性炭吸附喹啉0.5 h后,通过滴液漏斗向三颈烧瓶缓慢滴加13.65 mL的浓盐酸;(4) After the activated carbon adsorbs quinoline for 0.5 h, slowly add 13.65 mL of concentrated hydrochloric acid dropwise to the three-neck flask through the dropping funnel;
(5)待滴加完浓盐酸0.5 h后,将三颈烧瓶中放置于45℃恒温水浴锅中,进行减压蒸馏;(5) After adding concentrated hydrochloric acid dropwise for 0.5 h, place the three-neck flask in a 45°C constant temperature water bath and perform vacuum distillation;
(6)减压蒸馏完毕后,将三颈烧瓶中的活性炭和溶液全部转移至水热合成反应釜中,再分别加入4.45mL的甲醇,用玻璃棒轻微搅拌均匀后密闭,放入置于145℃烘箱中反应6h;(6) After the vacuum distillation is completed, transfer all the activated carbon and solution in the three-neck flask to the hydrothermal synthesis reaction kettle, then add 4.45mL of methanol respectively, stir slightly with a glass rod, seal it, and place it at 145 React in oven for 6 hours;
(7)取出反应釜,自然冷却至室温后将活性炭和液体转移至三颈烧瓶中,在70℃下,减压蒸馏,蒸馏除去未反应的甲醇;(7) Take out the reaction kettle, cool it naturally to room temperature, transfer the activated carbon and liquid to a three-neck flask, and distill under reduced pressure at 70°C to remove unreacted methanol;
(8)将活性炭先用无水乙醇洗涤、抽滤3-6次,再用去离子水洗涤、抽滤3-6次,然后再得到的活性炭放入70℃烘箱中干燥至恒重,得氯化-1-甲基喹啉修饰后的活性炭。(8) Wash the activated carbon with absolute ethanol and suction filtration 3-6 times, then wash it with deionized water and suction filtration 3-6 times, and then dry the obtained activated carbon in a 70°C oven to a constant weight to obtain Activated carbon modified with 1-methylquinoline chloride.
对照例:3-氯-2-羟基丙基三甲氯化铵修饰活性炭Comparative example: 3-chloro-2-hydroxypropyltrimethylammonium chloride modified activated carbon
(1)将活性炭用标准筛筛分,筛选出粒径为20-60目活性炭,用去离子水清洗3-6次,以除去活性炭表面杂质与粉尘,然后在110℃的鼓风干燥箱内干燥至恒重,冷却至室温后将装入样品袋;(1) Sieve the activated carbon with a standard sieve to screen out activated carbon with a particle size of 20-60 mesh, wash it with deionized water 3-6 times to remove impurities and dust on the surface of the activated carbon, and then place it in a blast drying oven at 110°C Dry to constant weight, cool to room temperature and then put into sample bag;
(2)将步骤(1)得到的5 g 活性炭放置于烧杯中,加入400 mL浓度为1mol/L的盐酸,室温下浸泡24 h。然后用去离子水洗涤和抽滤3-6次,干燥至恒重;(2) Place 5 g of activated carbon obtained in step (1) into a beaker, add 400 mL of hydrochloric acid with a concentration of 1 mol/L, and soak at room temperature for 24 hours. Then wash with deionized water and suction filter 3-6 times, and dry to constant weight;
(3)将步骤(2)得到的2.0 g活性炭放于250 mL锥形瓶中。向锥形瓶中加入20 mL3-氯-2-羟基丙基三甲氯化铵溶液,然后将锥形瓶密封;(3) Place 2.0 g of activated carbon obtained in step (2) into a 250 mL Erlenmeyer flask. Add 20 mL of 3-chloro-2-hydroxypropyltrimethylammonium chloride solution to the Erlenmeyer flask, and then seal the Erlenmeyer flask;
(4)将步骤(3)的锥形瓶放入恒温水浴震荡器中,在室温下震荡24 h,使3-氯-2-羟基丙基三甲氯化铵均匀地附着在活性炭表面;(4) Place the Erlenmeyer flask from step (3) into a constant-temperature water bath shaker and shake at room temperature for 24 hours to allow 3-chloro-2-hydroxypropyltrimethylammonium chloride to evenly adhere to the surface of the activated carbon;
(5)将步骤(4)的锥形瓶放入50 ℃水浴锅中,然后锥形瓶中滴加5 mol/L的NaOH溶液,将溶液pH调节至11-12.5以达到环氧反应所需的pH,将锥形瓶密封,反应8 h;(5) Place the Erlenmeyer flask in step (4) into a 50°C water bath, then add 5 mol/L NaOH solution dropwise into the Erlenmeyer flask, and adjust the pH of the solution to 11-12.5 to meet the requirements for the epoxy reaction pH, seal the Erlenmeyer flask and react for 8 hours;
(6)将步骤(5)的锥形瓶取出冷却至室温,向锥形瓶中滴加5 mol/L的HCl溶液将pH调节至小于7,终止阳离子化反应;(6) Take out the Erlenmeyer flask in step (5) and cool it to room temperature. Add 5 mol/L HCl solution dropwise into the Erlenmeyer flask to adjust the pH to less than 7 to terminate the cationization reaction;
(7)将步骤(6)得到的混合物过滤,用无水乙醇反复多次洗涤改性后的活性炭,然后用去离子水洗涤,直到洗涤水pH为中性,以除去未反应的3-氯-2-羟基丙基三甲氯化铵;(7) Filter the mixture obtained in step (6), wash the modified activated carbon with absolute ethanol several times, and then wash with deionized water until the pH of the washing water becomes neutral to remove unreacted 3-chlorine. -2-Hydroxypropyltrimethylammonium chloride;
(8)将将步骤(7)得到的改性活性炭在 60 ℃烘箱中干燥24 h,然后取出冷却至室温,得3-氯-2-羟基丙基三甲氯化铵修饰活性炭,标记为QAC-1:10。(8) Dry the modified activated carbon obtained in step (7) in an oven at 60°C for 24 h, then take it out and cool it to room temperature to obtain 3-chloro-2-hydroxypropyltrimethylammonium chloride modified activated carbon, labeled QAC- 1:10.
二、性能研究2. Performance research
将未改性的活性炭和示例2得到的氯化-1-甲基喹啉修饰后的活性炭进行SEM表征,得到的SEM表征图分别如图1和图2所示。The unmodified activated carbon and the activated carbon modified with 1-methylquinoline chloride obtained in Example 2 were subjected to SEM characterization, and the obtained SEM characterization images are shown in Figure 1 and Figure 2 respectively.
从图1可以看出,未改性活性炭表面酥松、不平整并且有很多碎片。从图2可以看出,氯化-1-甲基喹啉修饰后的活性炭表面附着了很多蓬松的球形颗粒物,它们是生成的氯化-1-甲基喹啉。从图2还可以看出,这些合成的物质虽然经过多次的无水乙醇、去离子水洗涤仍未有从活性炭表面脱落,表明氯化-1-甲基喹啉和活性炭表面结合力较强,不易从活性炭表面脱落而导致二次污染。As can be seen from Figure 1, the surface of unmodified activated carbon is loose, uneven and has many fragments. As can be seen from Figure 2, many fluffy spherical particles are attached to the surface of activated carbon modified with 1-methylquinoline chloride, which are the generated 1-methylquinoline chloride. It can also be seen from Figure 2 that these synthesized substances have not fallen off from the surface of activated carbon even after repeated washings with anhydrous ethanol and deionized water, indicating that the binding force between 1-methylquinoline chloride and the surface of activated carbon is strong. , not easy to fall off from the surface of activated carbon and cause secondary pollution.
采用吸附动力学实验进行活性炭、示例1和2制备的氯化-1-甲基喹啉修饰后的活性炭和对照例3-氯-2-羟基丙基三甲氯化铵饰后的活性炭吸附PFOA性能评价。具体步骤如下,Adsorption kinetics experiments were used to conduct adsorption performance of activated carbon, activated carbon modified with 1-methylquinoline chloride prepared in Examples 1 and 2, and activated carbon modified with 3-chloro-2-hydroxypropyltrimethylammonium chloride in the control example. evaluate. Specific steps are as follows,
(1)用容量瓶配制50 mg/L的全氟辛酸溶液,装入塑料瓶中备用;(1) Use a volumetric flask to prepare a 50 mg/L perfluorooctanoic acid solution and put it into a plastic bottle for later use;
(2)用分析天平准确称取50 mg不同改性条件下的活性炭于100 mL磨口锥形瓶中,用移液管准确吸取50 mL全氟辛酸溶液于锥形瓶中密封;(2) Use an analytical balance to accurately weigh 50 mg of activated carbon under different modification conditions into a 100 mL ground-mouth Erlenmeyer flask, use a pipette to accurately draw 50 mL of PFOA solution and seal it in the Erlenmeyer flask;
(3)将锥形瓶放入水浴恒温振荡器中,室温反应;每隔12 h,取上清液1 mL于15 mL塑料管中,加入过量氨水,使全氟辛酸完全反应为全氟辛酸铵;(3) Place the Erlenmeyer flask in a water bath constant-temperature oscillator and react at room temperature; every 12 hours, take 1 mL of the supernatant into a 15 mL plastic tube, add excess ammonia, and allow the perfluorooctanoic acid to completely react into ammonium perfluorooctanoate;
(4)采用紫外分光光度法测全氟辛酸铵的浓度,进而得PFOA的浓度。(4) Use UV spectrophotometry to measure the concentration of perfluorooctanoate, and then obtain the concentration of PFOA.
从图3中可以看出,当活性炭进行了带表面正电荷修饰后,其吸附PFOA的吸附量和吸附速率均好于原始活性炭。示例2得到的氯化-1-甲基喹啉修饰活性炭由于加入的喹啉多于示例1,也就是合成的氯化-1-甲基喹啉比示例1多,造成了示例2得到的活性炭中一些微孔被堵塞,导致示例2得到的活性炭对PFOA的吸附性能要低于示例1得到的活性炭。而对照例3-氯-2-羟基丙基三甲氯化铵修饰的活性炭由于该季铵盐的长的碳链造成的位阻效应,使得其吸附性能低于示例1和示例2得到的活性炭。As can be seen from Figure 3, when the activated carbon is modified with a positive surface charge, its adsorption capacity and adsorption rate of PFOA are better than those of the original activated carbon. The 1-methylquinoline chloride modified activated carbon obtained in Example 2 was due to the addition of more quinoline than in Example 1, that is, more 1-methylquinoline chloride was synthesized than in Example 1, resulting in the activated carbon obtained in Example 2. Some micropores are blocked, resulting in the adsorption performance of the activated carbon obtained in Example 2 for PFOA being lower than that of the activated carbon obtained in Example 1. The adsorption performance of the activated carbon modified with chloro-2-hydroxypropyltrimethylammonium chloride in Comparative Example 3 is lower than that of the activated carbon obtained in Examples 1 and 2 due to the steric hindrance effect caused by the long carbon chain of the quaternary ammonium salt.
最后需要说明的是,以上示例仅用以说明本发明的技术方案而非限制技术方案,本领域的普通技术人员应当理解,那些对本发明的技术方案进行修改或者等同替换,而不脱离本技术方案的宗旨和范围,均应涵盖在本发明的权利要求范围当中。Finally, it should be noted that the above examples are only used to illustrate the technical solutions of the present invention rather than to limit the technical solutions. Those of ordinary skill in the art should understand that those technical solutions of the present invention can be modified or equivalently substituted without departing from the technical solutions. The purpose and scope of the present invention shall be covered by the claims of the present invention.
Claims (6)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210992876.3A CN115228437B (en) | 2022-08-18 | 2022-08-18 | A surface modification method to make the surface of activated carbon positively charged |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210992876.3A CN115228437B (en) | 2022-08-18 | 2022-08-18 | A surface modification method to make the surface of activated carbon positively charged |
Publications (2)
Publication Number | Publication Date |
---|---|
CN115228437A CN115228437A (en) | 2022-10-25 |
CN115228437B true CN115228437B (en) | 2023-10-31 |
Family
ID=83680286
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202210992876.3A Active CN115228437B (en) | 2022-08-18 | 2022-08-18 | A surface modification method to make the surface of activated carbon positively charged |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115228437B (en) |
Citations (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1291549A (en) * | 1960-07-19 | 1962-04-27 | May & Baker Ltd | New diazoamine compounds and their preparation |
DE2615342C3 (en) * | 1976-04-08 | 1980-06-04 | Bayer Ag, 5090 Leverkusen | Process for the preparation of dithiophosphoric acid diester halides |
WO2008129024A1 (en) * | 2007-04-24 | 2008-10-30 | Basf Se | Porous organometallic framework materials loaded with catalyst metal components |
CN101432227A (en) * | 2004-06-23 | 2009-05-13 | 海珀里昂催化国际有限公司 | Functionalized single walled carbon nanotubes |
CN102274714A (en) * | 2011-08-03 | 2011-12-14 | 上海理工大学 | Absorbing material for removing anion in water and preparation method thereof |
CN107486159A (en) * | 2017-10-13 | 2017-12-19 | 北京清水润土环保科技有限公司 | The curing materials for being used to fix manganese in river bottom mud based on attapulgite |
CN108144572A (en) * | 2017-12-28 | 2018-06-12 | 江苏大学 | A kind of application of graphite phase carbon nitride perfluoro caprylic acid in water removal is gone |
CN108620025A (en) * | 2018-05-14 | 2018-10-09 | 济南大学 | A kind of sulfamethoxazole is modified the preparation method of alumina silicate fibre adsorbent |
CN111318261A (en) * | 2020-03-09 | 2020-06-23 | 中国矿业大学(北京) | Modified activated carbon, preparation method thereof and method for removing bromate in water |
CN111514865A (en) * | 2020-05-09 | 2020-08-11 | 闫娟 | Preparation of resin microspheres and application of resin microspheres in printing and dyeing wastewater treatment |
CN112962042A (en) * | 2021-02-01 | 2021-06-15 | 江西科技师范大学 | Hot galvanizing explosion-proof agent and preparation method thereof |
CN113371780A (en) * | 2021-06-11 | 2021-09-10 | 上海力脉环保设备有限公司 | Treatment method of wastewater containing low-concentration perfluorooctanoic acid |
CN114082407A (en) * | 2021-10-15 | 2022-02-25 | 江苏海普功能材料有限公司 | Synthetic method of high-salinity medium-fluorine-removal adsorbent |
CN114772756A (en) * | 2022-04-20 | 2022-07-22 | 江苏美亚科泽过滤技术有限公司 | Phosphorus-free multifunctional microcapsule scale inhibitor and preparation method and application thereof |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020097694A1 (en) * | 2018-11-16 | 2020-05-22 | Hydrus Technology Pty. Ltd. | Method of treating a liquid including an organofluorine |
-
2022
- 2022-08-18 CN CN202210992876.3A patent/CN115228437B/en active Active
Patent Citations (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1291549A (en) * | 1960-07-19 | 1962-04-27 | May & Baker Ltd | New diazoamine compounds and their preparation |
DE2615342C3 (en) * | 1976-04-08 | 1980-06-04 | Bayer Ag, 5090 Leverkusen | Process for the preparation of dithiophosphoric acid diester halides |
CN101432227A (en) * | 2004-06-23 | 2009-05-13 | 海珀里昂催化国际有限公司 | Functionalized single walled carbon nanotubes |
WO2008129024A1 (en) * | 2007-04-24 | 2008-10-30 | Basf Se | Porous organometallic framework materials loaded with catalyst metal components |
CN102274714A (en) * | 2011-08-03 | 2011-12-14 | 上海理工大学 | Absorbing material for removing anion in water and preparation method thereof |
CN107486159A (en) * | 2017-10-13 | 2017-12-19 | 北京清水润土环保科技有限公司 | The curing materials for being used to fix manganese in river bottom mud based on attapulgite |
CN108144572A (en) * | 2017-12-28 | 2018-06-12 | 江苏大学 | A kind of application of graphite phase carbon nitride perfluoro caprylic acid in water removal is gone |
CN108620025A (en) * | 2018-05-14 | 2018-10-09 | 济南大学 | A kind of sulfamethoxazole is modified the preparation method of alumina silicate fibre adsorbent |
CN111318261A (en) * | 2020-03-09 | 2020-06-23 | 中国矿业大学(北京) | Modified activated carbon, preparation method thereof and method for removing bromate in water |
CN111514865A (en) * | 2020-05-09 | 2020-08-11 | 闫娟 | Preparation of resin microspheres and application of resin microspheres in printing and dyeing wastewater treatment |
CN112962042A (en) * | 2021-02-01 | 2021-06-15 | 江西科技师范大学 | Hot galvanizing explosion-proof agent and preparation method thereof |
CN113371780A (en) * | 2021-06-11 | 2021-09-10 | 上海力脉环保设备有限公司 | Treatment method of wastewater containing low-concentration perfluorooctanoic acid |
CN114082407A (en) * | 2021-10-15 | 2022-02-25 | 江苏海普功能材料有限公司 | Synthetic method of high-salinity medium-fluorine-removal adsorbent |
CN114772756A (en) * | 2022-04-20 | 2022-07-22 | 江苏美亚科泽过滤技术有限公司 | Phosphorus-free multifunctional microcapsule scale inhibitor and preparation method and application thereof |
Non-Patent Citations (3)
Title |
---|
"活性炭的表面修饰对其吸附全氟辛酸性能的影响";吉若澜;李雪梅;宋敏;邱春艳;文诗雨;汪柔;郝世雄;中国井矿盐;第54卷(第001期);全文 * |
何铁林主编.《水处理化学品手册》.化学工业出版社,2000,第386-387页. * |
苑晨."季铵盐改性活性炭吸附地下水中PFOA的效能及其机理研究".《中国博士学位论文全文数据库 工程科技Ⅰ辑》.2021,(第2021年01期期),第25-27页. * |
Also Published As
Publication number | Publication date |
---|---|
CN115228437A (en) | 2022-10-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110559998A (en) | Loaded biochar functional material for adsorbing heavy metal ions as well as preparation and application thereof | |
CN108912269B (en) | A kind of polyimidazole ionic liquid-based copolymer and its preparation method and application | |
CN102241406A (en) | Carboxylated MCM-41 mesoporous molecular sieve for adsorbing heavy metal ions, and preparation method thereof | |
CN110496608A (en) | A polyionic liquid@metal organic framework composite material xPILs@MIL-101 and its preparation method and application | |
CN105838384B (en) | Soil passivation repairing agent using nano-silica as carrier and preparation method thereof | |
Singhon et al. | Adsorption of Ni (II) ions on colloidal hybrid organic–inorganic silica composites | |
CN104984746A (en) | Modification method for nano silicon dioxide | |
CN104475023B (en) | A kind of preparation method of modified konjac glucomannan carbosphere heavy-metal adsorption material | |
CN108543516A (en) | A kind of lithium ion selective absorbent, preparation method and the technique for carrying lithium from brine | |
JP2016040032A (en) | Adsorbent comprising cellulose derivative and/or cross-linked chitosan derivative and adsorption method and recovery method for metal ion | |
CN111250059A (en) | Hyperbranched polyethyleneimine modified carbon fiber adsorption material for adsorbing indium (III) and preparation method thereof | |
Wang et al. | Chitosan functionalized with N, N-(2-aminoethyl) pyridinedicarboxamide for selective adsorption of gold ions from wastewater | |
CN107583620B (en) | A kind of chitosan-based metal ion adsorbent and preparation method thereof | |
CN110372737A (en) | A kind of nano silicon-based microballoon preparation method of sulfhydrylation and application | |
CN106824131A (en) | A kind of chitosan-modified mesoporous material and its preparation method and application | |
CN111001397B (en) | Method for synthesizing beta-cyclodextrin conjugated biochar by microwave-assisted one-pot method and application thereof | |
CN115228437B (en) | A surface modification method to make the surface of activated carbon positively charged | |
CN114426677A (en) | A kind of amino-modified metal organic framework material, preparation method and application thereof | |
CN116478420B (en) | A covalent triazine framework material and its preparation method and application | |
CN109675527A (en) | It is a kind of for go water removal in heavy metal adsorbent material and its preparation method and application | |
CN106345429B (en) | A kind of bagasse base anion adsorbent and its preparation method and application | |
CN115672280B (en) | Preparation method of perfluoro caprylic acid adsorbent | |
CN115634669A (en) | 3D mushroom waste aerogel, preparation method thereof and application thereof in adsorption of radionuclide technetium | |
CN112516966A (en) | Preparation method and application of imine diacetic acid functionalized magnetic adsorption material | |
Simatupang et al. | Fabrication of silica-based chitosan biocomposite material from volcanic ash and shrimp husk by sol gel method for adsorbent of cadmium (II) Ions |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |