Immersion enthalpy and the constants of Langmuir model in the 3-chloro phenol adsorption on activated carbon

被引:7
作者
Giraldo, Liliana [2 ]
Carlos Moreno, Juan [1 ]
机构
[1] Univ Los Andes, Fac Ciencias, Dept Quim, Grp Invest Solidos Porosos & Calorimet, Bogota, Colombia
[2] Univ Nacl Colombia, Fac Ciencias, Dept Quim, Bogota, Colombia
关键词
3-chloro phenol; Activated carbon; Adsorption capacity; Immersion enthalpy; pH; LIQUID-PHASE ADSORPTION; DYES;
D O I
10.1007/s10973-009-0192-3
中图分类号
O414.1 [热力学];
学科分类号
摘要
The adsorption process of 3-chloro phenol from aqueous solution on a activated carbon prepared from African palm stone and which presents a specific surface area of 685 m(2) g(-1), a greater quantity of total acid groups and a pH(PZC) of 6.8 is studied. The adsorption isotherms are determined at pH values of 3, 5, 7, 9 and 11. The adsorption isotherms are fitted to the Langmuir model and the values of the maximum quantity adsorbed that are between 96.2 and 46.4 mg g(-1) are obtained along with the constant K-L with values between 0.422 and 0.965 L mg(-1). The maximum quantity adsorbed diminishes with the pH and the maximum value for this is a pH of 5. The immersion enthalpies of the activated carbon in a 3-chloro phenol solution of constant concentration, of 100 mg L-1, are determined for the different pH levels, with results between 37.6 and 21.2 J g(-1). Immersion enthalpies of the activated carbon in function of 3-chloro phenol solution concentration are determined to pH 5, of maximum adsorption, with values between 28.3 and 38.4 J g(-1), and by means of linearization, the maximum immersion enthalpy is calculated, with a value of 41.67 J g(-1). With the results of the immersion enthalpy, maximum quantity adsorbed and the constant K-L, establish relations that describe the adsorption process of 3-chloro phenol from aqueous solution on activated carbon.
引用
收藏
页码:695 / 700
页数:6
相关论文
共 50 条
  • [21] Adsorption equilibrium and kinetics of phenol on activated carbon
    Yan, Y. (yingyan@scut.edu.cn), 2013, South China University of Technology (41): : 56 - 61
  • [22] ADSORPTION ISOTHERMS OF PHENOL AND ANILINE ON ACTIVATED CARBON
    Vijan, Loredana Elena
    Neagu, Mihaela
    REVUE ROUMAINE DE CHIMIE, 2012, 57 (02) : 85 - 93
  • [23] RELATION BETWEEN IMMERSION ENTHALPY OF ACTIVATED CARBON MONOLITHS AND TEXTURAL PARAMETERS
    Vargas, Diana P.
    Giraldo Gutierrez, Liliana
    Carlos Moreno, Juan
    QUIMICA NOVA, 2011, 34 (02): : 196 - 199
  • [24] Characterization of aramid based activated carbon fibres by adsorption and immersion techniques
    Villar-Rodil, S
    Denoyel, R
    Rouquerol, J
    Martínez-Alonso, A
    Tascón, JMD
    CARBON, 2002, 40 (08) : 1376 - 1380
  • [25] Relation between immersion enthalpies of activated carbons in different liquids, textural properties, and phenol adsorption
    Liliana Giraldo
    Juan Carlos Moreno-Piraján
    Journal of Thermal Analysis and Calorimetry, 2014, 117 : 1517 - 1523
  • [26] Relation between immersion enthalpies of activated carbons in different liquids, textural properties, and phenol adsorption
    Giraldo, Liliana
    Carlos Moreno-Pirajan, Juan
    JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2014, 117 (03) : 1517 - 1523
  • [27] Influence of the pH of Pb2+ aqueous solutions on the immersion enthalpy and the adsorption capacity of activated carbons
    Girado, Liliana
    Moreno, Juan Carlos
    AFINIDAD, 2007, 64 (530) : 517 - 522
  • [28] Relatioship between the adsorption capacity and the immersion enthalpy of chemically modified activated carbons on aqueous solutions of methylparaben
    Moreno-Marenco, A. R.
    Giraldo, L.
    Moreno-Pirajan, J. C.
    AFINIDAD, 2019, 76 (587) : 213 - 220
  • [29] Adsorption of Phenol Using Activated Carbon Adsorbent from Waste Tyres
    Amri, Nurulhuda
    Zakaria, Ridzuan
    Abu Bakar, Mohamad Zailani
    PERTANIKA JOURNAL OF SCIENCE AND TECHNOLOGY, 2009, 17 (02): : 371 - 379
  • [30] Behavior of phenol adsorption on thermal modified activated carbon
    Dengfeng Zhang
    Peili Huo
    Wei Liu
    Chinese Journal of Chemical Engineering, 2016, 24 (04) : 446 - 452