Hydrogen production by the Cu-Cl thermochemical cycle: Investigation of the key step of hydrolysing CuCl2 to Cu2OCl2 and HCl using a spray reactor

被引:68
作者
Ferrandon, Magali S. [1 ]
Lewis, Michele A. [1 ]
Tatterson, David F. [2 ]
Gross, Adam [1 ]
Doizi, Denis [3 ]
Croize, L. [3 ]
Dauvois, V. [3 ]
Roujou, J. L. [3 ]
Zanella, Y. [3 ]
Carles, P. [3 ]
机构
[1] Argonne Natl Lab, Chem Sci & Engn Div, Argonne, IL 60439 USA
[2] Orion Consulting Co, Downers Grove, IL 60515 USA
[3] CE Saclay, CEA, Dept Phys Chem, F-91191 Gif Sur Yvette, France
关键词
Thermochemical cycle; Cu-Cl cycle; Hydrogen production; Hydrolysis; Spray reactor; ELECTROLYSIS;
D O I
10.1016/j.ijhydene.2009.09.086
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
One of the most challenging steps in the thermochemical Cu-Cl cycle for the production of hydrogen is the hydrolysis Of CuCl2 into Cu2OCl2 and HCl while avoiding the need for excess water and the undesired thermolysis reaction, which gives CuCl and Cl-2. Argonne National Laboratory has designed a spray reactor where an aqueous solution of CuCl2 is atomized into a heated zone, into which steam/Ar are injected in co- or counter-current flow. The solid products of the reaction were analyzed by XRD and SEM. With a pneumatic nebulizer, the counter-current flow design gave high yields Of Cu2OCl2 compared to the co-current flow design, but some CuCl2 remained unreacted in both designs. With an ultrasonic nozzle, essentially 100% yields Of Cu2OCl2 were obtained. Some CuCl was present in the products with both types of atomizers but this is believed to be due to decomposition of Cu2OCl2 rather than CuCl2. Analyses of gaseous products from the hydrolysis reactions in a fixed bed were conducted at the Commissariat L'Energie Atomique using ultraviolet-visible spectrometry and conductivity. At a reaction temperature of 390 degrees C, the desired HCl was formed while no Cl-2 was detected until the bed temperature was above 400 degrees C. (C) 2009 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:992 / 1000
页数:9
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