武汉科技大学学报(自然科学版)
武漢科技大學學報(自然科學版)
무한과기대학학보(자연과학판)
JOURNAL OF WUHAN UNIVERSITY OF SCIENCE AND TECHNOLOGY(NATURAL SCIENCE EDITION)
2014年
1期
54-58
,共5页
石飞%刘红%刘鲁建%董俊
石飛%劉紅%劉魯建%董俊
석비%류홍%류로건%동준
分子筛%C d2+%吸附%离子交换:重金属
分子篩%C d2+%吸附%離子交換:重金屬
분자사%C d2+%흡부%리자교환:중금속
molecular sieve%Cd2+%adsorption%ion exchange%heavy metal
以4A和13X分子筛为吸附材料,考察废水pH值和Cd2+初始浓度等对Cd2+去除率的影响,并研究了分子筛对Cd2+的吸附性能。结果表明,4A和13X分子筛投加量为0.16 g/L、废水pH值为5、Cd2+浓度为20 mg/L时,Cd2+去除率达到95%以上;分子筛对Cd2+的去除机理以离子交换吸附为主,交换出来的Na+与分子筛吸附的Cd2+摩尔浓度比为2;在吸附热力学和动力学方面,4A和13X分子筛均符合Langmuir吸附等温模型和Lagergren二级速率方程,计算的饱和吸附容量 Q0分别为150.15、163.67 mg/g ,二级反应速率常数K2分别为2.45×10-3、3.96×10-4 g/(mg · s)。该吸附反应是一种单分子层反应速度较快的化学吸附过程。
以4A和13X分子篩為吸附材料,攷察廢水pH值和Cd2+初始濃度等對Cd2+去除率的影響,併研究瞭分子篩對Cd2+的吸附性能。結果錶明,4A和13X分子篩投加量為0.16 g/L、廢水pH值為5、Cd2+濃度為20 mg/L時,Cd2+去除率達到95%以上;分子篩對Cd2+的去除機理以離子交換吸附為主,交換齣來的Na+與分子篩吸附的Cd2+摩爾濃度比為2;在吸附熱力學和動力學方麵,4A和13X分子篩均符閤Langmuir吸附等溫模型和Lagergren二級速率方程,計算的飽和吸附容量 Q0分彆為150.15、163.67 mg/g ,二級反應速率常數K2分彆為2.45×10-3、3.96×10-4 g/(mg · s)。該吸附反應是一種單分子層反應速度較快的化學吸附過程。
이4A화13X분자사위흡부재료,고찰폐수pH치화Cd2+초시농도등대Cd2+거제솔적영향,병연구료분자사대Cd2+적흡부성능。결과표명,4A화13X분자사투가량위0.16 g/L、폐수pH치위5、Cd2+농도위20 mg/L시,Cd2+거제솔체도95%이상;분자사대Cd2+적거제궤리이리자교환흡부위주,교환출래적Na+여분자사흡부적Cd2+마이농도비위2;재흡부열역학화동역학방면,4A화13X분자사균부합Langmuir흡부등온모형화Lagergren이급속솔방정,계산적포화흡부용량 Q0분별위150.15、163.67 mg/g ,이급반응속솔상수K2분별위2.45×10-3、3.96×10-4 g/(mg · s)。해흡부반응시일충단분자층반응속도교쾌적화학흡부과정。
With 4A and 13X molecular sieves as adsorption materials ,the effects of the pH value of waste water and the initial concentration of Cd2+ on Cd2+ removal rate were investigated and the sieves’ adsorption of Cd2+ was studied .The results show that ,at the 0 .16g/L of dosing quantity of 4A and 13X molecular sieves ,5 of initial pH and 20 mg/L of Cd2+ concentration ,Cd2+ removal rate reaches 95% or more .The primary mechanism of Cd2+ removal by molecular sieves is ion exchange adsorption .The molar concentration ratio between exchanged Na + and Cd2+ adsorbed by the sieves is 2∶ 1 ,In adsorption thermodynamics and dynamics ,4A and 13X molecular sieves conform to the Langmuir adsorption isothermal model and Lagergren secondary rate equation ,respectively .The sat-urated adsorption capacities are 150 .15 mg/g and 163 .67 mg/g ,and the secondary reaction rate con-stants are 2 .45 × 10 -3 g/(mg · s) and 3 .96 × 10-4 g/(mg · s) ,respectively .It is also found that the adsorption reaction is a fast single molecular layer chemical process .