Analysis, modelling and simulation of hydrogen peroxide ultrapurification by multistage reverse osmosis

被引:21
作者
Abejon, R. [1 ]
Garea, A. [1 ]
Irabien, A. [1 ]
机构
[1] Univ Cantabria, Dept Ingn Quim & Quim Inorgan, E-39005 Santander, Cantabria, Spain
关键词
Ultrapurification; Electronic grade chemicals; Hydrogen peroxide; Reverse osmosis; WASTE-WATER RECLAMATION; MEMBRANES; REUSE; NANOFILTRATION;
D O I
10.1016/j.cherd.2011.07.025
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Very high purity chemicals are required for preparation of semiconductor materials and manufacture of printed circuit boards because low presence of metallic impurities is needed to avoid defects on silicon surface. Hydrogen peroxide is one of the most demanded chemical by the semiconductor industry and it must be submitted to ultrapurification processes to achieve the exigent requirements the chemical must fulfill to be accepted for semiconductor uses. In this paper, the potential of multistage reverse osmosis processes to reduce the metallic content of technical grade hydrogen peroxide below the limits fixed by the semiconductor industry is investigated. SEMI Grade 1 quality hydrogen peroxide was obtained by a two-pass reverse osmosis process in an experimental lab scale. A model based on xedem-xatchalsky transport equations together with system material balances was proposed to describe the behavior of the installation. A full analysis of the influence of the design (recovery rates) and operation (applied pressures) variables over the performance of a simulated industrial scale plant was carried out. The economic viability of the simulated plant was demonstrated. (C) 2011 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:442 / 452
页数:11
相关论文
共 42 条
[1]   Ultrapurification of hydrogen peroxide solution from ionic metals impurities to semiconductor grade by reverse osmosis [J].
Abejon, R. ;
Garea, A. ;
Irabien, A. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2010, 76 (01) :44-51
[2]   A comparative study on the membrane based palm oil mill effluent (POME) treatment plant [J].
Ahmad, A. L. ;
Chong, M. F. ;
Bhatia, S. .
JOURNAL OF HAZARDOUS MATERIALS, 2009, 171 (1-3) :166-174
[3]  
Atsumi J., 1990, P ELECTROCHEM SOC, V90, P59
[4]   Reverse osmosis applied to metal finishing wastewater [J].
Benito, Y ;
Ruíz, ML .
DESALINATION, 2002, 142 (03) :229-234
[5]  
Bianchi U. P., 2001, U.S. Patent, Patent No. 6333018
[6]  
Boughton J.H., 1989, US Patent, Patent No. 4879043
[7]   The use of integrated countercurrent nanofiltration cascades for advanced separations [J].
Caus, Alexander ;
Braeken, Leen ;
Boussu, Katleen ;
Van der Bruggen, Bart .
JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2009, 84 (03) :391-398
[8]  
Chandan Das, 2010, International Journal of Environment and Waste Management, V5, P354, DOI 10.1504/IJEWM.2010.032013
[9]   Limits of Operation for the Integration of Water Removal by Membranes and Crystallization of L-Phenylalanine [J].
Cuellar, Maria C. ;
Herreilers, Simone N. ;
Straathof, Adrie J. J. ;
Heijnen, Joseph J. ;
van der Wielen, Luuk A. M. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (03) :1566-1573
[10]  
Daigle S., 2007, ULLMANNS ENCY IND CH