Thermodynamic and experimental analysis on ethanol steam reforming for hydrogen production over Ni-modified TiO2/MMT nanoclay catalyst

被引:39
作者
Tahir, Muhammad [1 ]
Mulewa, William [1 ,2 ]
Amin, Nor Aishah Saidina [1 ]
Zakaria, Zaki Yamani [1 ]
机构
[1] Univ Teknol Malaysia, Fac Chem Energy Engn, Dept Chem Engn, CREG, Utm Johor Bahru 81310, Johor, Malaysia
[2] Tech Univ Mombasa, Mombasa 80100, Kenya
关键词
Thermodynamics; Montmorillonite; Ni/TiO2; Ethanol steam reforming; H-2; production; Stability performance; BIO-OIL; CO2; METHANATION; H-2; PRODUCTION; REDUCTION; GLYCEROL; CARBON; MONTMORILLONITE; PERFORMANCE; METHANOL; HYDROCARBON;
D O I
10.1016/j.enconman.2017.10.042
中图分类号
O414.1 [热力学];
学科分类号
摘要
Catalytic ethanol steam reforming (ESR) offers a sustainable and attractive route for hydrogen production, which can be utilized as a substitute for fossil fuels. ESR for hydrogen production involves complex reactions and yield of hydrogen depends upon several process variables such as temperature, molar feed ratio and pressure. In this study, a thermodynamics analysis coupled with experimentation for ESR toward hydrogen production has been investigated. The structured montmorillonite (MMT) nanoclay and TiO2 supported catalyst incorporated by nickel (Ni) was developed via a sol-gel and impregnation methods. The catalyst samples were characterized by XRD, FE-SEM, EDX, BET and TGA to understand crystallinity, surface morphology, pore structure and stability. Initially, thermodynamic analysis was employed to study the effect of reaction conditions on equilibrium product distribution of ESR. The equilibrium concentrations of different compounds were calculated by the method of direct minimization of the Gibbs free energy. Optimum conditions for ESR were found to be; atmospheric pressure, temperatures between 600 and 700 degrees C and steam to ethanol (S/E) feed molar ratio of 10:1, at which highest hydrogen can be produced with minimum coke formation. Next, catalytic performance of NiO/MMT-TiO2 catalyst for enhanced ESR for hydrogen production was conducted in a tubular fixed bed reactor at 500 degrees C and atmospheric pressure. Noticeably, Ni-promoted TiO2 NPs found efficient for selective hydrogen production, yet MMT-supported Ni/TiO2 gave much higher ethanol conversion with improved hydrogen yield. Using 12% Ni-10% MMT/TiO2 catalyst, ethanol conversion of 89% with H-2 selectivity and yield of 61 and 55%, respectively were obtained. The stability test revealed MMT-supported catalysts maintained activity even after 20 h. By comparing results, it was possible to explain deviations between thermodynamic analysis and experimental results regarding carbon deposition and selective hydrogen production.
引用
收藏
页码:25 / 37
页数:13
相关论文
共 57 条
[1]   A comparative thermodynamic and experimental analysis on hydrogen production by steam reforming of glycerin [J].
Adhikari, Sushil ;
Fernando, Sandun ;
Haryanto, Agus .
ENERGY & FUELS, 2007, 21 (04) :2306-2310
[2]   Hydrogen production by thermal partial oxidation of ethanol: Thermodynamics and kinetics study [J].
Al-Hamamre, Z. ;
Hararah, M. A. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (11) :5367-5377
[3]   CO2 methanation over Ni-promoted mesostructured silica nanoparticles: Influence of Ni loading and water vapor on activity and response surface methodology studies [J].
Aziz, M. A. A. ;
Jalil, A. A. ;
Triwahyono, S. ;
Saad, M. W. A. .
CHEMICAL ENGINEERING JOURNAL, 2015, 260 :757-764
[4]   Oxygenated hydrocarbons steam reforming over Ni/CeZrGdO2 catalyst: Kinetics and reactor modeling [J].
Bakhtiari, Mehrdad ;
Abu Zahid, Md. ;
Ibrahim, Hussameldin ;
Khan, Ataullah ;
Sengupta, Protyai ;
Idem, Raphael .
CHEMICAL ENGINEERING SCIENCE, 2015, 138 :363-374
[5]   Hydrogen production from methanol by oxidative steam reforming carried out in a membrane reactor [J].
Basile, A ;
Gallucci, F ;
Paturzo, L .
CATALYSIS TODAY, 2005, 104 (2-4) :251-259
[6]   Production of hydrogen by steam reforming of ethanol over alumina supported nano-NiO/SiO2 catalyst [J].
Bej, Barnali ;
Pradhan, Narayan C. ;
Neogi, Swati .
CATALYSIS TODAY, 2014, 237 :80-88
[7]   Influence of acid activation on adsorption of Ni(II) and Cu(II) on kaolinite and montmorillonite: Kinetic and thermodynamic study [J].
Bhattacharyya, Krishna G. ;
Sen Gupta, Susmita .
CHEMICAL ENGINEERING JOURNAL, 2008, 136 (01) :1-13
[8]   Kaolinite and montmorillonite as adsorbents for Fe(III), Co(II) and Ni(II) in aqueous medium [J].
Bhattacharyya, Krishna G. ;
Sen Gupta, Susmita .
APPLIED CLAY SCIENCE, 2008, 41 (1-2) :1-9
[9]   Hydrogen production from natural gas, sequestration of recovered CO2 in depleted gas wells and enhanced natural gas recovery [J].
Blok, K ;
Williams, RH ;
Katofsky, RE ;
Hendriks, CA .
ENERGY, 1997, 22 (2-3) :161-168
[10]   Ethanol steam reforming on Ni/Al2O3 catalysts: Effect of the addition of Zn and Pt [J].
Buitrago-Sierra, R. ;
Ruiz-Martinez, J. ;
Serrano-Ruiz, J. C. ;
Rodriguez-Reinoso, F. ;
Sepulveda-Escribano, A. .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2012, 383 :148-154