Cost analysis of a commercial manufacturing process of a fine chemical compound using micro process engineering

被引:28
作者
Krtschil, Ulrich
Hessel, Volker
Kralisch, Dana
Kreisel, Guenther
Kuepper, Michael
Schenk, Rainer
机构
[1] Inst Mikrotech Mainz GmbH, D-55129 Mainz, Germany
[2] AzurChem GmbH, D-55129 Mainz, Germany
[3] Eindhoven Univ Technol, Dept Chem & Chem Engn, NL-5612 AZ Eindhoven, Netherlands
[4] Univ Jena, Inst Tech Chem & Umweltchem, D-07743 Jena, Germany
关键词
cost analysis; 4-cyanophenylboronic acid; micro process engineering; micro reactor; microstructured reactor;
D O I
10.2533/chimia.2006.611
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
In the last years micro process engineering has developed rapidly and commercial interest has increased. While process intensification was demonstrated, the question remains whether this novel technology can lead to economic profits. In this context, a cost analysis is performed here for an economic fine chemical process of the customized chemical producer AzurChem GmbH, i.e. the formation of the 4-cyanophenylboronic acid, using the benefits of micro process technology supplied by. IMM GmbH. This process is representative for several other fine and specialty chemical manufacturing processes proprietary to the AzurChem GmbH. This is the first time that a cost analysis is made accessible in open literature for a commercial chemical product made by micro process engineering, i.e. for a real-case scenario with validated database, i.e. real yields, micro-chemical plant, chemical and operator costs. The conclusions from this particular case are extended to more general statements on the micro processing of the whole class of high-value fine chemicals. This is achieved via some potential case scenarios of conceivable improvements by means of capacity or selectivity increases and a comparison with a traditional manufacturing method based on batch processing. In this way, some fundamental issues on the suitability of this novel technology are revealed, i.e. how process intensification translates into business drivers.
引用
收藏
页码:611 / 617
页数:7
相关论文
共 26 条
[1]   Exergy, waste accounting, and life-cycle analysis [J].
Ayres, RU ;
Ayres, LW ;
Martinas, K .
ENERGY, 1998, 23 (05) :355-363
[2]  
BELLONI A, 2006, PROCESS, V13, P64
[3]   Application of life cycle assessment to chemical processes [J].
Burgess, AA ;
Brennan, DJ .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (08) :2589-2604
[4]  
DEIBEL SR, 2006, CHEMANAGER, P2
[5]   Design and operation of a preferential oxidation microdevice for a portable fuel processor [J].
Delsman, ER ;
De Croon, MHJM ;
Pierik, A ;
Kramer, GJ ;
Cobden, PD ;
Hofmann, C ;
Cominos, V ;
Schouten, JC .
CHEMICAL ENGINEERING SCIENCE, 2004, 59 (22-23) :4795-4802
[6]  
DELSMAN ER, 2006, IN PRESS ENERGY
[7]   Green chemistry: synthesis in micro reactors [J].
Haswell, SJ ;
Watts, P .
GREEN CHEMISTRY, 2003, 5 (02) :240-249
[8]   Development of microstructured reactors to enable organic synthesis rather than subduing chemistry [J].
Hessel, V ;
Löb, P ;
Löwe, H .
CURRENT ORGANIC CHEMISTRY, 2005, 9 (08) :765-787
[9]   Organic synthesis with microstructured reactors [J].
Hessel, V ;
Löwe, H .
CHEMICAL ENGINEERING & TECHNOLOGY, 2005, 28 (03) :267-284
[10]   Selectivity gains and energy savings for the industrial phenyl boronic acid process using micromixer/tubular reactors [J].
Hessel, V ;
Hofmann, C ;
Löwe, H ;
Meudt, A ;
Scherer, S ;
Schönfeld, F ;
Werner, B .
ORGANIC PROCESS RESEARCH & DEVELOPMENT, 2004, 8 (03) :511-523