Effect of temperature and pressure on the reduction of U(VI) to U(IV) by hydrogen over Pt/SiO2: Reaction kinetics and modeling

被引:0
作者
Reddy, S. Ramakrishna [1 ,2 ]
Ayyappa, S. V. N. [2 ]
Mishra, Satyabrata [2 ]
Sreepriya, T. [1 ]
Desigan, N. [2 ]
Venkatesan, K. A. [1 ,2 ]
Sivaraman, N. [1 ,3 ]
Ananthasivan, K. [1 ,2 ]
机构
[1] Indira Gandhi Ctr Atom Res, Homi Bhabha Natl Inst, Kalpakkam 603102, Tamil Nadu, India
[2] Indira Gandhi Ctr Atom Res, Reproc Grp, Kalpakkam 603102, Tamil Nadu, India
[3] Indira Gandhi Ctr Atom Res, Mat Chem & Met Fuel Cycle Grp, Kalpakkam 603102, Tamil Nadu, India
关键词
Uranium; Reduction; Kinetics; Catalysis; Hydrogen; CATALYTIC-REDUCTION; NITROPHENOL; TECHNOLOGY; PARAMETERS; CHEMISTRY; ACID;
D O I
10.1016/j.cherd.2023.03.053
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The kinetics of catalytic reduction of U(VI) by H2 over Pt/SiO2 was investigated as a function of various parameters. The effect of agitation speed and particle size on the reduction of U(VI) was studied initially to eliminate the mass transfer resistance. Later, the effect of catalyst loading, concentration of U(VI), HNO3, N2H4, H2 pressure and temperature on the reduction of U(VI) was studied. Langmuir-Hinshelwood- Hougen-Watson (LHHW) approach was employed to derive kinetic model equations and understand the reaction mechanism. Among the various models, the model - IX corresponding to the adsorption of nitric acid on the catalyst surface was found to be suitable for explaining the concentration profiles of U(VI) and HNO3 in all the temperature and pressure range. The activation energy of the reaction was determined to be around 22.6 kJ mol-1 indicating the reduction of U(VI) with H2 was falling in chemical and diffusion controlled regime. (c) 2023 Institution of Chemical Engineers. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:613 / 625
页数:13
相关论文
共 39 条
[1]  
Ananiev AV, 2005, USP KHIM+, V74, P1132
[2]   Reaction mechanism and intrinsic kinetics of sugar hydrogenation to sugar alcohols on solid foam Ru/C catalysts - From arabinose and galactose to arabitol and galactitol [J].
Araujo Barahona, German ;
Eranen, Kari ;
Murzin, Dmitry ;
Garcia Serna, Juan ;
Salmi, Tapio .
CHEMICAL ENGINEERING SCIENCE, 2022, 254
[3]   Experimental and kinetic studies of ethyltoluenes production via different alkylation reactions [J].
Atanda, Luqman A. ;
Aitani, Abdullah M. ;
Al-Khattaf, Sulaiman S. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2015, 95 :34-46
[4]   An overview of solvent extraction processes developed in Europe for advanced nuclear fuel recycling, Part 2-homogeneous recycling [J].
Authen, Thea Lyseid ;
Adnet, Jean-Marc ;
Bourgb, Stephane ;
Carrottc, Michael ;
Ekberg, Christian ;
Galan, Hitos ;
Geist, Andreas ;
Guilbaud, Philippe ;
Miguirditchian, Manuel ;
Modolo, Giuseppe ;
Rhodes, Chris ;
Wilden, Andreas ;
Taylor, Robin .
SEPARATION SCIENCE AND TECHNOLOGY, 2022, 57 (11) :1724-1744
[5]   Hydrogenation of p-nitrophenol to metol using Raney nickel catalyst:: Reaction kinetics [J].
Bawane, SP ;
Sawant, SB .
APPLIED CATALYSIS A-GENERAL, 2005, 293 (1-2) :162-170
[6]   Reaction kinetics of the liquid-phase hydrogenation of benzonitrile to benzylamine using Raney nickel catalyst [J].
Bawane, SP ;
Sawant, SB .
CHEMICAL ENGINEERING JOURNAL, 2004, 103 (1-3) :13-19
[7]  
Boltoeva MY, 2008, RADIOCHEMISTRY+, V50, P38, DOI 10.1134/S1066362208010050
[8]   Kinetics of hydrogenation of o-nitrophenol to o-aminophenol on Pd/carbon catalysts in a stirred three-phase slurry reactor [J].
Choudhary, VR ;
Sane, MG ;
Tambe, SS .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (10) :3879-3887
[9]   New method of determination of intrinsic kinetic and mass transport parameters from typical catalyst activity tests: Problem of mass transfer resistance and diffusional limitation of reaction rate [J].
Jodlowski, P. J. ;
Jedrzejczyk, Rd. ;
Gancarczyk, A. ;
Lojewska, J. ;
Kolodziej, A. .
CHEMICAL ENGINEERING SCIENCE, 2017, 162 :322-331
[10]  
Kittrell J.R., 2015, TECHNOL AUDIT PROD R, V2, P11, DOI [10.15587/2312-8372.2015.41070, DOI 10.15587/2312-8372.2015.41070]