H2S adsorption onto Cu-Zn-Ni nanoparticles loaded activated carbon and Ni-Co nanoparticles loaded γ-Al2O3: Optimization and adsorption isotherms

被引:76
作者
Daneshyar, A. [1 ]
Ghaedi, M. [2 ]
Sabzehmeidani, M. M. [3 ]
Daneshyar, A. [1 ]
机构
[1] Islamic Azad Univ, Omidiyeh Branch, Dept Chem, Omidiyeh, Khuzestan State, Iran
[2] Univ Yasuj, Dept Chem, Yasuj 7591874831, Iran
[3] Univ Yasuj, Dept Chem Engn, Yasuj, Iran
关键词
Hydrogen sulfide (H2S); Adsorption; Cu-Zn-Ni/AC; Co-Ni/gamma-Al2O3 Natural gas; Isotherm and thermodynamic study; CENTRAL COMPOSITE DESIGN; ALIZARIN RED S; HYDROGEN-SULFIDE; SURFACE-CHEMISTRY; AQUEOUS-SOLUTION; BIOTRICKLING FILTERS; METHYL MERCAPTAN; ASSISTED REMOVAL; PORE STRUCTURE; GAS-MIXTURES;
D O I
10.1016/j.jcis.2016.11.068
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The nanocomposites based on copper, zinc and nickel were loaded on activated carbon (Cu-Zn-Ni-NPsAC) and cobalt and nickel nanoparticles was loaded on 7 -alumina (Ni-Co-NPs-gamma Al2O3) and applied for removal of hydrogen sulfide (H2S) from natural gas and their efficiency were compared. Cu-Zn-Ni/AC and Ni-Co/gamma-Al2O3 was characterized using different techniques such as energy -dispersive X-ray spectroscopy (EDX), X-ray diffraction (XRD) and field emission scanning electron microscopy (FE-SEM). The effects of variables such as amount of adsorbent, flow rate, temperature, pressure and volume of gas on H2S removal were examined and optimum values were found to be 0.3 g adsorbent, and flow rate of 0.15 Limin and 15 degrees C and 7 Psi for both adsorbent and also 5.5 and 6.5 L of sample by Cu-Zn-Ni/C and Co-Ni/gamma-Al2O3, respectively. Setting conditions at the above optimum conditions lead to achievement of maximum removal of H25 (94% and 91.6%) by Cu-Zn-Ni/AC and Co-Ni/gamma-Al2O3. The negative value of Delta G degrees and its numerical value confirm physisorption nature of adsorption. The experimental equilibrium data with high efficiency were explained and represented by Langmuir model for both adsorbents with the highest correlation coefficients. (C) 2016 Elsevier Inc. All rights reserved.
引用
收藏
页码:553 / 561
页数:9
相关论文
共 57 条
[1]   A review of biogas purification processes [J].
Abatzoglou, Nicolas ;
Boivin, Steve .
BIOFUELS BIOPRODUCTS & BIOREFINING-BIOFPR, 2009, 3 (01) :42-71
[2]   Effect of pH and surface chemistry on the mechanism of H2S removal by activated carbons [J].
Adib, F ;
Bagreev, A ;
Bandosz, TJ .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1999, 216 (02) :360-369
[3]   Analysis of the relationship between H2S removal capacity and surface properties of unimpregnated activated carbons [J].
Adib, F ;
Bagreev, A ;
Bandosz, TJ .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2000, 34 (04) :686-692
[4]   Removal of methylene blue from colored effluents by adsorption on montmorillonite clay [J].
Almeida, C. A. P. ;
Debacher, N. A. ;
Downs, A. J. ;
Cottet, L. ;
Mello, C. A. D. .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2009, 332 (01) :46-53
[5]   HIGH-TEMPERATURE HYDROGEN-SULFIDE CHEMISORPTION ON NICKEL-CATALYSTS [J].
ALSTRUP, I ;
ROSTRUPNIELSEN, JR ;
ROEN, S .
APPLIED CATALYSIS, 1981, 1 (05) :303-314
[6]  
[Anonymous], BERICHTE BUNSENGESEL
[7]   Bituminous coal-based activated carbons modified with nitrogen as adsorbents of hydrogen sulfide [J].
Bagreev, A ;
Menendez, JA ;
Dukhno, I ;
Tarasenko, Y ;
Bandosz, TJ .
CARBON, 2004, 42 (03) :469-476
[8]   Dual role of water in the process of methyl mercaptan adsorption on activated carbons [J].
Bagreev, A ;
Bashkova, S ;
Bandosz, TJ .
LANGMUIR, 2002, 18 (22) :8553-8559
[9]   Thermal regeneration of a spent activated carbon previously used as hydrogen sulfide adsorbent [J].
Bagreev, A ;
Rahman, H ;
Bandosz, TJ .
CARBON, 2001, 39 (09) :1319-1326
[10]   On the adsorption/oxidation of hydrogen sulfide on activated carbons at ambient temperatures [J].
Bandosz, TJ .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2002, 246 (01) :1-20