Protein refolding in an oscillatory-flow-mixing reactor
We demonstrate that an oscillatory flow-mixing reactor (OFMR) operating in fed-batch mode is viable for industrial protein refolding. OFMR offers the advantage of uniform, controllable, and scalable mixing. Denatured lysozyme (15 mg/ml, in 8 M guanidine hydrochloride (GuHCl) or 8 M urea, and 32 mM...
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my.utm.31172017-07-24T01:00:17Z http://eprints.utm.my/id/eprint/3117/ Protein refolding in an oscillatory-flow-mixing reactor Lee, C. T. Middelberg, Anton TP Chemical technology We demonstrate that an oscillatory flow-mixing reactor (OFMR) operating in fed-batch mode is viable for industrial protein refolding. OFMR offers the advantage of uniform, controllable, and scalable mixing. Denatured lysozyme (15 mg/ml, in 8 M guanidine hydrochloride (GuHCl) or 8 M urea, and 32 mM dithiothreitol) was fed into a 150-ml OFMR for 2 h and the final solution was incubated for a further 3 h. A control experiment used a small perfectly-mixed stirred-tank reactor (STR). Both systems were operated under mild and intense mixing conditions. With GuHCl denaturation, the refolding yield profiles throughout the 5 h period were identical in both the OFMR and STR, and yield was independent of mixing intensity. Conversely, refolding yield in both reactors following urea denaturation decreased from 25% to 15% as mixing intensity decreased. Clearly, imperfect mixing in large STRs may lead to reduced refolding yield when urea is used as a denaturant. This effect can be minimised by using a reactor with uniform, controllable and scaleable mixing, such as the OFMR. 2001 Conference or Workshop Item NonPeerReviewed Lee, C. T. and Middelberg, Anton (2001) Protein refolding in an oscillatory-flow-mixing reactor. In: The Proceeding of the 10th European Congress on Biotechnology, 8-11th July 2001, Madrid, Spain. |
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TP Chemical technology Lee, C. T. Middelberg, Anton Protein refolding in an oscillatory-flow-mixing reactor |
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We demonstrate that an oscillatory flow-mixing reactor (OFMR) operating in fed-batch mode is viable for industrial protein refolding. OFMR offers the advantage of uniform, controllable, and scalable mixing. Denatured lysozyme (15 mg/ml, in 8 M guanidine hydrochloride (GuHCl) or 8 M urea, and 32 mM dithiothreitol) was fed into a 150-ml OFMR for 2 h and the final solution was incubated for a further 3 h. A control experiment used a small perfectly-mixed stirred-tank reactor (STR). Both systems were operated under mild and intense mixing conditions. With GuHCl denaturation, the refolding yield profiles throughout the 5 h period were identical in both the OFMR and STR, and yield was independent of mixing intensity. Conversely, refolding yield in both reactors following urea denaturation decreased from 25% to 15% as mixing intensity decreased. Clearly, imperfect mixing in large STRs may lead to reduced refolding yield when urea is used as a denaturant. This effect can be minimised by using a reactor with uniform, controllable and scaleable mixing, such as the OFMR. |
format |
Conference or Workshop Item |
author |
Lee, C. T. Middelberg, Anton |
author_facet |
Lee, C. T. Middelberg, Anton |
author_sort |
Lee, C. T. |
title |
Protein refolding in an oscillatory-flow-mixing reactor |
title_short |
Protein refolding in an oscillatory-flow-mixing reactor |
title_full |
Protein refolding in an oscillatory-flow-mixing reactor |
title_fullStr |
Protein refolding in an oscillatory-flow-mixing reactor |
title_full_unstemmed |
Protein refolding in an oscillatory-flow-mixing reactor |
title_sort |
protein refolding in an oscillatory-flow-mixing reactor |
publishDate |
2001 |
url |
http://eprints.utm.my/id/eprint/3117/ |
_version_ |
1643643739719073792 |
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13.211869 |