Conceptual design and simulation of a plant for the production of high purity (S)-ibuprofen acid using innovative enzymatic membrane technology
dc.contributor.author | Lau, John | |
dc.contributor.author | Gonawan, F. | |
dc.contributor.author | Bhatia, S. | |
dc.contributor.author | Kamaruddin, A. | |
dc.contributor.author | Uzir, M. | |
dc.date.accessioned | 2018-05-18T08:00:56Z | |
dc.date.available | 2018-05-18T08:00:56Z | |
dc.date.created | 2018-05-18T00:23:00Z | |
dc.date.issued | 2011 | |
dc.identifier.citation | Lau, J. and Gonawan, F. and Bhatia, S. and Kamaruddin, A. and Uzir, M. 2011. Conceptual design and simulation of a plant for the production of high purity (S)-ibuprofen acid using innovative enzymatic membrane technology. Chemical Engineering Journal. 166 (2): pp. 726-737. | |
dc.identifier.uri | http://hdl.handle.net/20.500.11937/68117 | |
dc.identifier.doi | 10.1016/j.cej.2010.11.072 | |
dc.description.abstract |
(S)-Ibuprofen is a low volume but high value pharmaceutical product which is categorized as non-steroidal anti-inflammatory drug (NSAID). This precious chiral drug may be produced using racemic ibuprofen as raw material through the dynamic kinetic resolution. In this work, a simulation of (S)-ibuprofen production is carried out using ASPEN PLUS ® process simulation software. A pilot scale production with the capacity of 500g/day of (S)-ibuprofen acid is considered in the present study. The product is synthesized through a three-step process: (i) substrate preparation via esterification; (ii) enzymatic dynamic kinetic resolution of substrate ester and (iii) product purification. Mass and energy balances of major equipment were calculated. The performance of the enzyme-mediated membrane reactor (EMR) was investigated by manipulating substrate and base concentrations as well as the flow rates. Besides, a number of issues related to the evaporation and crystallization of the product were identified and addressed. It was found that the optimum operating condition of EMR at 40°C, 50-100ml/min lumen flow rate with substrate and base concentrations, respectively at 10-20mM and 60-100mM, gave 0.92 conversion and 0.9 ee p of the product. An overall yield of 82.5% product crystal was achieved by operating the cooling-crystallizer in the temperature range of 5-10°C. © 2010 Elsevier B.V. | |
dc.publisher | Elsevier BV | |
dc.title | Conceptual design and simulation of a plant for the production of high purity (S)-ibuprofen acid using innovative enzymatic membrane technology | |
dc.type | Journal Article | |
dcterms.source.volume | 166 | |
dcterms.source.number | 2 | |
dcterms.source.startPage | 726 | |
dcterms.source.endPage | 737 | |
dcterms.source.issn | 1385-8947 | |
dcterms.source.title | Chemical Engineering Journal | |
curtin.department | Curtin Malaysia | |
curtin.accessStatus | Fulltext not available |
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