广州化工
廣州化工
엄주화공
GUANGZHOU CHEMICAL INDUSTRY AND TECHNOLOGY
2015年
14期
57-58,77
,共3页
黎艳容%谭超雄%梁继业%张燕厚
黎豔容%譚超雄%樑繼業%張燕厚
려염용%담초웅%량계업%장연후
活性炭%双酚A%硝酸%改性%吸附
活性炭%雙酚A%硝痠%改性%吸附
활성탄%쌍분A%초산%개성%흡부
activated carbon%bisphenol A%nitric acid%modification%adsorption
采用硝酸氧化法对活性炭( AC)进行改性,考察改性前后活性炭的孔面结构与表面性质的变化,并进行双酚A吸附特性的对比。 BET分析表明,改性后活性炭( MAC)虽然比表面积减小,但总孔容增大,平均孔径也由改性前的1.87 nm增大到2.01 nm。 FTIR分析表明, MAC的表面引入羧酸等含氧基团,减少了醌基等基团。 AC的双酚A的平衡吸附量约为3.72 mg/g,且随初始浓度的增大,吸附量变化不大,而MAC对双酚A的平衡吸附量随初始浓度增大而明显增大,当溶液初始浓度为100 mg/L时,最大吸附量在5.78 mg/g左右。说明硝酸改性活性炭更利于对双酚A的吸附。
採用硝痠氧化法對活性炭( AC)進行改性,攷察改性前後活性炭的孔麵結構與錶麵性質的變化,併進行雙酚A吸附特性的對比。 BET分析錶明,改性後活性炭( MAC)雖然比錶麵積減小,但總孔容增大,平均孔徑也由改性前的1.87 nm增大到2.01 nm。 FTIR分析錶明, MAC的錶麵引入羧痠等含氧基糰,減少瞭醌基等基糰。 AC的雙酚A的平衡吸附量約為3.72 mg/g,且隨初始濃度的增大,吸附量變化不大,而MAC對雙酚A的平衡吸附量隨初始濃度增大而明顯增大,噹溶液初始濃度為100 mg/L時,最大吸附量在5.78 mg/g左右。說明硝痠改性活性炭更利于對雙酚A的吸附。
채용초산양화법대활성탄( AC)진행개성,고찰개성전후활성탄적공면결구여표면성질적변화,병진행쌍분A흡부특성적대비。 BET분석표명,개성후활성탄( MAC)수연비표면적감소,단총공용증대,평균공경야유개성전적1.87 nm증대도2.01 nm。 FTIR분석표명, MAC적표면인입최산등함양기단,감소료곤기등기단。 AC적쌍분A적평형흡부량약위3.72 mg/g,차수초시농도적증대,흡부량변화불대,이MAC대쌍분A적평형흡부량수초시농도증대이명현증대,당용액초시농도위100 mg/L시,최대흡부량재5.78 mg/g좌우。설명초산개성활성탄경리우대쌍분A적흡부。
A study was carried out to investigate the modifying of activated carbon ( AC ) by nitric acid oxidation process.BET analyses indicated that, in comparing with the original AC, the modified activated carbon ( MAC) had a smaller specific surface area but larger pore volume and average pore diameter.FTIR ditection revealed that the oxidation process could change the surface chemical property of AC by incresing the content of carboxyl group and decreasing the one of quinone group.As the two kinds of activated carbon were used to adsorpt aqueous bisphenol A.MAC showed to be better than AC.The results showed that the oxidation process was advantageous to activated carbon for adsorpting bisphenol A.