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硅酸盐通报 ›› 2018, Vol. 37 ›› Issue (4): 1447-1454.

• • 上一篇    下一篇

表面接枝改性有机膨润土的制备及其对苯酚吸附

李树白;姚培;刘媛;张启蒙;刘春晓   

  1. 常州工程职业技术学院绿色技术研究所,常州 213164;常州工程职业技术学院化学与材料工程学院,常州 213164;常州工程职业技术学院绿色技术研究所,常州,213164
  • 出版日期:2018-04-15 发布日期:2021-01-18
  • 基金资助:
    江苏省高校"青蓝工程"科技创新团队项目%江苏高校品牌建设工程项目(PPZY2015B178)%江苏省高校自然科学研究面上项目(16KJB530005)%常州市社会发展科技计划项目(CE20155049,CE20155009)%江苏省高校优秀中青年教师和校长境外研修计划

Grafting Modification on the Surface of Organobentonite and Its Application on Phenol Absorption

LI Shu-bai;YAO Pei;LIU Yuan;ZHANG Qi-meng;LIU Chun-xiao   

  • Online:2018-04-15 Published:2021-01-18

摘要: 利用阳离子表面活性剂十六烷基三甲基氯化铵插层钙基膨润土,硅烷偶联剂接枝得到新型有机膨润土.并对其进行FTIR、XRD、SEM、TG和BET表征.结果表明:有机改性后阳离子表面活性剂成功进入膨润土层间,层间距增大,硅烷偶联剂水解后接枝膨润土表面.SEM显示有机膨润土表面片层叠起,疏松.TG显示十六烷基三甲基氯化铵和硅烷偶联剂的分解在200 ℃以后,有机膨润土热稳定性较好,改性过程中没有破坏晶格.有机膨润土N2吸附-脱附曲线表明,有机膨润土具有微孔和介孔特性,为苯酚的吸附提供通道.以有机膨润土作为吸附剂,对苯酚处理过程中加量、吸附时间,pH值对苯酚影响因素进行考察,得到10 ℃时,pH值为7.2,最佳加量为3 g· L-1,吸附时间60 min时,苯酚废水去除率达79.8%.有机膨润土吸附苯酚符合Langmuir等温吸附模型,动力学符合伪二级动力学方程,表面化学吸附和颗粒扩散控制吸附过程;属于放热、熵减型吸附反应.

关键词: 有机膨润土;表面活性剂;硅烷偶联剂;苯酚;吸附;动力学

Abstract: A novel Organobentonite was prepared by modifying calcium bentonite using cationic surfactant hexadecyltrimethyl-ammonium chloride(HTMAC)as intercalation agents and grafting with silane coupling agent(KH570).The Organobentonite was characterized and analysed with Fourier transform infrared(FT-IR),X-ray diffraction(XRD), scanning electron microscope(SEM), thermogravimetric differential thermal analysis(TG-DTA)and Brunauer-Emmett-Teller(BET).The results show: the modified reagent(HTMAC)has been intercalated to the layer of bentonite,and the d001values increase from 1.533 nm to 2.342 nm.The phenol molecule can be adsorbed in multiple layers or obliquely inserted into the layer of organobentonite(Diameter of phenol is 0.69nm).From the TG-DTA curve,It shows the organobentonite exhibited there steps of weight loss.The adsorbed water was lost at T<225℃,corresponding to 2.9%.A mass lose(15%)in the temperature range of 490 ℃ due to the decomposition of HTMAC and KH570.Another mass loss(2%)centered in the range of 490-600 ℃due to the dehydroxylation of OH units.The N2adsorption-desorption isotherm of organobentonite exhibited that it belongs to IV isotherm with H3 hysteresis loop, indicating that organobentonite was a mixed microporous/mesoporous material.The specific surface area of purified bentonite and organobentonite were 5.43 m2· g-1and 46.87 m2· g-1respectively.Pore volume of puried bentonite and organobentonite were up to 0.102 cm3· g-1and 0.213 cm3· g-1.Factors affecting the adsorption of phenol(such as pH, equilibrium time temperature, the dosage of adsorbent and initial concentration) were investigated.The highest removal rate of phenol waste water is 79.8%,and the best condition is:dosage of organobentonite 3 g· L-1,adsorption time 60 min,pH 7.2 and adsorption temperature 10℃. The phenol adsorption data gives good fits with Langmuir isotherm model.The parameter factor RL falls between 0 and 1,indicating the adsorption of phenol is favorable.The adsorption process is exothermic with negative ΔH values.The negative ΔS suggested an decrease randomness at the solid-liquid interface during the adsorption process.The spontaneous adsorption depends on the exothermic characteristics of the adsorption process.The adsorption trend follows the pseudo-second order kinetics model.The whole adsorption process was controlled by surface chemical adsorption and intraparticle diffusion.

Key words: organobentonite;surfactants;silane coupling agent;phenol;adsorption;kinetics

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