Batch and continuous cultivation processes of Candida tropicalis TISTR 5306 for ethanol and pyruvate decarboxylase production in fresh longan juice with optimal carbon to nitrogen molar ratio
© 2019 Wiley Periodicals, Inc. The carbon to nitrogen (C/N) molar ratio of 21.88 ± 0.20 in fresh juice from C-grade longan (FLJ-C) supplemented with ammonium sulfate (AMS) was optimal for cultivation of Candida tropicalis TISTR 5306 producing ethanol concentration of 24.0 ± 1.1 g/L and specific pyru...
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th-cmuir.6653943832-665672019-09-16T12:49:11Z Batch and continuous cultivation processes of Candida tropicalis TISTR 5306 for ethanol and pyruvate decarboxylase production in fresh longan juice with optimal carbon to nitrogen molar ratio Rojarej Nunta Charin Techapun Kittisak Jantanasakulwong Thanongsak Chaiyaso Phisit Seesuriyachan Julaluk Khemacheewakul Chatchadaporn Mahakuntha Kritsadaporn Porninta Sumeth Sommanee Ngoc T. Trinh Noppol Leksawasdi Agricultural and Biological Sciences Chemical Engineering © 2019 Wiley Periodicals, Inc. The carbon to nitrogen (C/N) molar ratio of 21.88 ± 0.20 in fresh juice from C-grade longan (FLJ-C) supplemented with ammonium sulfate (AMS) was optimal for cultivation of Candida tropicalis TISTR 5306 producing ethanol concentration of 24.0 ± 1.1 g/L and specific pyruvate decarboxylase (PDC) activity of 0.138 ± 0.001 U/mg protein. The highest ethanol concentration in a 10 L continuous process (34.3 ± 0.5 g/L, dilution rate [D] = 0.0492 hr−1) was significantly higher (p ≤.05) than that in 100 L batch process (13.2 ± 0.2 g/L at 108 hr). The highest volumetric PDC activities of 0.081 ± 0.001 U/ml (D = 0.0070 hr−1) and 0.107 ± 0.001 U/ml (48 hr) were attained for continuous and batch processes, respectively. The affinity constants and growth-related weighting factors on sucrose and monosaccharides (glucose and fructose with the same values) utilization were (123 ± 1 g/L, 0.14 ± 0.01) and (34.1 ± 1.5 g/L, 0.43 ± 0.01) with MS and R2 of 92.2 and.9552, respectively. Practical applications: FLJ-C is an example of agricultural produces with relatively high production quantity (50,000 t/year in Thailand) and high sugars content but low marketing demands due to the smallest size of pulp. The complex nitrogen source contains costly components (yeast extract—78.3 USD/kg, malt extract—148 USD/kg, and peptone—151 USD/kg) which can be replaced with an inexpensive AMS (1.05 USD/kg). Further consideration of C/N molar ratio in FLJ-C can optimize growth, ethanol (alternative biofuel/industrial solvent) production, and specific PDC (biocatalyst for phenylacetylcarbinol—PAC, anti-asthmatic and nasal decongestant precursors) activity of C. tropicalis TISTR 5306 whole cells which can be used as a case study for other related yeasts. Batch and continuous production at 100 L and 10 L also illustrate practical utilization of FLJ-C with AMS supplement at larger scales for development of subsequent zero waste process. 2019-09-16T12:46:46Z 2019-09-16T12:46:46Z 2019-01-01 Journal 17454530 01458876 2-s2.0-85070763347 10.1111/jfpe.13227 https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=85070763347&origin=inward http://cmuir.cmu.ac.th/jspui/handle/6653943832/66567 |
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Agricultural and Biological Sciences Chemical Engineering Rojarej Nunta Charin Techapun Kittisak Jantanasakulwong Thanongsak Chaiyaso Phisit Seesuriyachan Julaluk Khemacheewakul Chatchadaporn Mahakuntha Kritsadaporn Porninta Sumeth Sommanee Ngoc T. Trinh Noppol Leksawasdi Batch and continuous cultivation processes of Candida tropicalis TISTR 5306 for ethanol and pyruvate decarboxylase production in fresh longan juice with optimal carbon to nitrogen molar ratio |
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© 2019 Wiley Periodicals, Inc. The carbon to nitrogen (C/N) molar ratio of 21.88 ± 0.20 in fresh juice from C-grade longan (FLJ-C) supplemented with ammonium sulfate (AMS) was optimal for cultivation of Candida tropicalis TISTR 5306 producing ethanol concentration of 24.0 ± 1.1 g/L and specific pyruvate decarboxylase (PDC) activity of 0.138 ± 0.001 U/mg protein. The highest ethanol concentration in a 10 L continuous process (34.3 ± 0.5 g/L, dilution rate [D] = 0.0492 hr−1) was significantly higher (p ≤.05) than that in 100 L batch process (13.2 ± 0.2 g/L at 108 hr). The highest volumetric PDC activities of 0.081 ± 0.001 U/ml (D = 0.0070 hr−1) and 0.107 ± 0.001 U/ml (48 hr) were attained for continuous and batch processes, respectively. The affinity constants and growth-related weighting factors on sucrose and monosaccharides (glucose and fructose with the same values) utilization were (123 ± 1 g/L, 0.14 ± 0.01) and (34.1 ± 1.5 g/L, 0.43 ± 0.01) with MS and R2 of 92.2 and.9552, respectively. Practical applications: FLJ-C is an example of agricultural produces with relatively high production quantity (50,000 t/year in Thailand) and high sugars content but low marketing demands due to the smallest size of pulp. The complex nitrogen source contains costly components (yeast extract—78.3 USD/kg, malt extract—148 USD/kg, and peptone—151 USD/kg) which can be replaced with an inexpensive AMS (1.05 USD/kg). Further consideration of C/N molar ratio in FLJ-C can optimize growth, ethanol (alternative biofuel/industrial solvent) production, and specific PDC (biocatalyst for phenylacetylcarbinol—PAC, anti-asthmatic and nasal decongestant precursors) activity of C. tropicalis TISTR 5306 whole cells which can be used as a case study for other related yeasts. Batch and continuous production at 100 L and 10 L also illustrate practical utilization of FLJ-C with AMS supplement at larger scales for development of subsequent zero waste process. |
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Rojarej Nunta Charin Techapun Kittisak Jantanasakulwong Thanongsak Chaiyaso Phisit Seesuriyachan Julaluk Khemacheewakul Chatchadaporn Mahakuntha Kritsadaporn Porninta Sumeth Sommanee Ngoc T. Trinh Noppol Leksawasdi |
author_facet |
Rojarej Nunta Charin Techapun Kittisak Jantanasakulwong Thanongsak Chaiyaso Phisit Seesuriyachan Julaluk Khemacheewakul Chatchadaporn Mahakuntha Kritsadaporn Porninta Sumeth Sommanee Ngoc T. Trinh Noppol Leksawasdi |
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Rojarej Nunta |
title |
Batch and continuous cultivation processes of Candida tropicalis TISTR 5306 for ethanol and pyruvate decarboxylase production in fresh longan juice with optimal carbon to nitrogen molar ratio |
title_short |
Batch and continuous cultivation processes of Candida tropicalis TISTR 5306 for ethanol and pyruvate decarboxylase production in fresh longan juice with optimal carbon to nitrogen molar ratio |
title_full |
Batch and continuous cultivation processes of Candida tropicalis TISTR 5306 for ethanol and pyruvate decarboxylase production in fresh longan juice with optimal carbon to nitrogen molar ratio |
title_fullStr |
Batch and continuous cultivation processes of Candida tropicalis TISTR 5306 for ethanol and pyruvate decarboxylase production in fresh longan juice with optimal carbon to nitrogen molar ratio |
title_full_unstemmed |
Batch and continuous cultivation processes of Candida tropicalis TISTR 5306 for ethanol and pyruvate decarboxylase production in fresh longan juice with optimal carbon to nitrogen molar ratio |
title_sort |
batch and continuous cultivation processes of candida tropicalis tistr 5306 for ethanol and pyruvate decarboxylase production in fresh longan juice with optimal carbon to nitrogen molar ratio |
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2019 |
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https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=85070763347&origin=inward http://cmuir.cmu.ac.th/jspui/handle/6653943832/66567 |
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