Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation

Background Clostridium pasteurianum CH4 was used to produce butanol from glycerol. The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membra...
Ausführliche Beschreibung

Gespeichert in:

Autor*in:	Lin, De-Shun [verfasserIn] Yen, Hong-Wei Kao, Wei-Chen Cheng, Chieh-Lun Chen, Wen-Ming Huang, Chieh-Chen Chang, Jo-Shu

Format:	E-Artikel
Sprache:	Englisch

Erschienen:	2015

Schlagwörter:	Bio-butanol Vacuum membrane distillation (VMD) Butyrate addition Glycerol

Anmerkung:	© Lin et al. 2015

Übergeordnetes Werk:	Enthalten in: Biotechnology for biofuels - London : BioMed Central, 2008, 8(2015), 1 vom: 13. Okt.
Übergeordnetes Werk:	volume:8 ; year:2015 ; number:1 ; day:13 ; month:10

Links:	Volltext

DOI / URN:	10.1186/s13068-015-0352-6

Katalog-ID:	SPR030147808

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520			\|a Background Clostridium pasteurianum CH4 was used to produce butanol from glycerol. The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration. Results Adding 6 g $ L^{−1} $ butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol)−1. Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g $ L^{−1} $, while the yield was also improved to 0.39 mol butanol (mol glycerol)−1. The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution. Conclusions The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. The VMD-based technology not only alleviates the inhibitory effect of butanol, but also markedly increases butanol concentration in the permeate after condensation, thereby making downstream processing easier and more cost-effective.
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700	1		\|a Chang, Jo-Shu \|4 aut
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author_variant	d s l dsl h w y hwy w c k wck c l c clc w m c wmc c c h cch j s c jsc
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allfields	10.1186/s13068-015-0352-6 doi (DE-627)SPR030147808 (SPR)s13068-015-0352-6-e DE-627 ger DE-627 rakwb eng Lin, De-Shun verfasserin aut Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation 2015 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Lin et al. 2015 Background Clostridium pasteurianum CH4 was used to produce butanol from glycerol. The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration. Results Adding 6 g $ L^{−1} $ butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol)−1. Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g $ L^{−1} $, while the yield was also improved to 0.39 mol butanol (mol glycerol)−1. The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution. Conclusions The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. The VMD-based technology not only alleviates the inhibitory effect of butanol, but also markedly increases butanol concentration in the permeate after condensation, thereby making downstream processing easier and more cost-effective. Bio-butanol (dpeaa)DE-He213 Vacuum membrane distillation (VMD) (dpeaa)DE-He213 Butyrate addition (dpeaa)DE-He213 Glycerol (dpeaa)DE-He213 Yen, Hong-Wei aut Kao, Wei-Chen aut Cheng, Chieh-Lun aut Chen, Wen-Ming aut Huang, Chieh-Chen aut Chang, Jo-Shu aut Enthalten in Biotechnology for biofuels London : BioMed Central, 2008 8(2015), 1 vom: 13. Okt. (DE-627)563167882 (DE-600)2421351-2 1754-6834 nnns volume:8 year:2015 number:1 day:13 month:10 https://dx.doi.org/10.1186/s13068-015-0352-6 kostenfrei Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_206 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_2003 GBV_ILN_2005 GBV_ILN_2009 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2027 GBV_ILN_2055 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2119 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 8 2015 1 13 10
spelling	10.1186/s13068-015-0352-6 doi (DE-627)SPR030147808 (SPR)s13068-015-0352-6-e DE-627 ger DE-627 rakwb eng Lin, De-Shun verfasserin aut Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation 2015 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Lin et al. 2015 Background Clostridium pasteurianum CH4 was used to produce butanol from glycerol. The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration. Results Adding 6 g $ L^{−1} $ butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol)−1. Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g $ L^{−1} $, while the yield was also improved to 0.39 mol butanol (mol glycerol)−1. The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution. Conclusions The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. The VMD-based technology not only alleviates the inhibitory effect of butanol, but also markedly increases butanol concentration in the permeate after condensation, thereby making downstream processing easier and more cost-effective. Bio-butanol (dpeaa)DE-He213 Vacuum membrane distillation (VMD) (dpeaa)DE-He213 Butyrate addition (dpeaa)DE-He213 Glycerol (dpeaa)DE-He213 Yen, Hong-Wei aut Kao, Wei-Chen aut Cheng, Chieh-Lun aut Chen, Wen-Ming aut Huang, Chieh-Chen aut Chang, Jo-Shu aut Enthalten in Biotechnology for biofuels London : BioMed Central, 2008 8(2015), 1 vom: 13. Okt. (DE-627)563167882 (DE-600)2421351-2 1754-6834 nnns volume:8 year:2015 number:1 day:13 month:10 https://dx.doi.org/10.1186/s13068-015-0352-6 kostenfrei Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_206 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_2003 GBV_ILN_2005 GBV_ILN_2009 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2027 GBV_ILN_2055 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2119 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 8 2015 1 13 10
allfields_unstemmed	10.1186/s13068-015-0352-6 doi (DE-627)SPR030147808 (SPR)s13068-015-0352-6-e DE-627 ger DE-627 rakwb eng Lin, De-Shun verfasserin aut Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation 2015 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Lin et al. 2015 Background Clostridium pasteurianum CH4 was used to produce butanol from glycerol. The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration. Results Adding 6 g $ L^{−1} $ butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol)−1. Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g $ L^{−1} $, while the yield was also improved to 0.39 mol butanol (mol glycerol)−1. The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution. Conclusions The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. The VMD-based technology not only alleviates the inhibitory effect of butanol, but also markedly increases butanol concentration in the permeate after condensation, thereby making downstream processing easier and more cost-effective. Bio-butanol (dpeaa)DE-He213 Vacuum membrane distillation (VMD) (dpeaa)DE-He213 Butyrate addition (dpeaa)DE-He213 Glycerol (dpeaa)DE-He213 Yen, Hong-Wei aut Kao, Wei-Chen aut Cheng, Chieh-Lun aut Chen, Wen-Ming aut Huang, Chieh-Chen aut Chang, Jo-Shu aut Enthalten in Biotechnology for biofuels London : BioMed Central, 2008 8(2015), 1 vom: 13. Okt. (DE-627)563167882 (DE-600)2421351-2 1754-6834 nnns volume:8 year:2015 number:1 day:13 month:10 https://dx.doi.org/10.1186/s13068-015-0352-6 kostenfrei Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_206 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_2003 GBV_ILN_2005 GBV_ILN_2009 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2027 GBV_ILN_2055 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2119 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 8 2015 1 13 10
allfieldsGer	10.1186/s13068-015-0352-6 doi (DE-627)SPR030147808 (SPR)s13068-015-0352-6-e DE-627 ger DE-627 rakwb eng Lin, De-Shun verfasserin aut Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation 2015 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Lin et al. 2015 Background Clostridium pasteurianum CH4 was used to produce butanol from glycerol. The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration. Results Adding 6 g $ L^{−1} $ butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol)−1. Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g $ L^{−1} $, while the yield was also improved to 0.39 mol butanol (mol glycerol)−1. The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution. Conclusions The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. The VMD-based technology not only alleviates the inhibitory effect of butanol, but also markedly increases butanol concentration in the permeate after condensation, thereby making downstream processing easier and more cost-effective. Bio-butanol (dpeaa)DE-He213 Vacuum membrane distillation (VMD) (dpeaa)DE-He213 Butyrate addition (dpeaa)DE-He213 Glycerol (dpeaa)DE-He213 Yen, Hong-Wei aut Kao, Wei-Chen aut Cheng, Chieh-Lun aut Chen, Wen-Ming aut Huang, Chieh-Chen aut Chang, Jo-Shu aut Enthalten in Biotechnology for biofuels London : BioMed Central, 2008 8(2015), 1 vom: 13. Okt. (DE-627)563167882 (DE-600)2421351-2 1754-6834 nnns volume:8 year:2015 number:1 day:13 month:10 https://dx.doi.org/10.1186/s13068-015-0352-6 kostenfrei Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_206 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_2003 GBV_ILN_2005 GBV_ILN_2009 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2027 GBV_ILN_2055 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2119 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 8 2015 1 13 10
allfieldsSound	10.1186/s13068-015-0352-6 doi (DE-627)SPR030147808 (SPR)s13068-015-0352-6-e DE-627 ger DE-627 rakwb eng Lin, De-Shun verfasserin aut Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation 2015 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Lin et al. 2015 Background Clostridium pasteurianum CH4 was used to produce butanol from glycerol. The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration. Results Adding 6 g $ L^{−1} $ butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol)−1. Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g $ L^{−1} $, while the yield was also improved to 0.39 mol butanol (mol glycerol)−1. The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution. Conclusions The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. The VMD-based technology not only alleviates the inhibitory effect of butanol, but also markedly increases butanol concentration in the permeate after condensation, thereby making downstream processing easier and more cost-effective. Bio-butanol (dpeaa)DE-He213 Vacuum membrane distillation (VMD) (dpeaa)DE-He213 Butyrate addition (dpeaa)DE-He213 Glycerol (dpeaa)DE-He213 Yen, Hong-Wei aut Kao, Wei-Chen aut Cheng, Chieh-Lun aut Chen, Wen-Ming aut Huang, Chieh-Chen aut Chang, Jo-Shu aut Enthalten in Biotechnology for biofuels London : BioMed Central, 2008 8(2015), 1 vom: 13. Okt. (DE-627)563167882 (DE-600)2421351-2 1754-6834 nnns volume:8 year:2015 number:1 day:13 month:10 https://dx.doi.org/10.1186/s13068-015-0352-6 kostenfrei Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_206 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_2003 GBV_ILN_2005 GBV_ILN_2009 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2027 GBV_ILN_2055 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2119 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 8 2015 1 13 10
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source	Enthalten in Biotechnology for biofuels 8(2015), 1 vom: 13. Okt. volume:8 year:2015 number:1 day:13 month:10
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The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration. Results Adding 6 g $ L^{−1} $ butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol)−1. Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g $ L^{−1} $, while the yield was also improved to 0.39 mol butanol (mol glycerol)−1. The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution. Conclusions The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. 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author	Lin, De-Shun
spellingShingle	Lin, De-Shun misc Bio-butanol misc Vacuum membrane distillation (VMD) misc Butyrate addition misc Glycerol Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation
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topic_title	Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation Bio-butanol (dpeaa)DE-He213 Vacuum membrane distillation (VMD) (dpeaa)DE-He213 Butyrate addition (dpeaa)DE-He213 Glycerol (dpeaa)DE-He213
topic	misc Bio-butanol misc Vacuum membrane distillation (VMD) misc Butyrate addition misc Glycerol
topic_unstemmed	misc Bio-butanol misc Vacuum membrane distillation (VMD) misc Butyrate addition misc Glycerol
topic_browse	misc Bio-butanol misc Vacuum membrane distillation (VMD) misc Butyrate addition misc Glycerol
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title	Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation
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title_full	Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation
author_sort	Lin, De-Shun
journal	Biotechnology for biofuels
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author_browse	Lin, De-Shun Yen, Hong-Wei Kao, Wei-Chen Cheng, Chieh-Lun Chen, Wen-Ming Huang, Chieh-Chen Chang, Jo-Shu
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author-letter	Lin, De-Shun
doi_str_mv	10.1186/s13068-015-0352-6
title_sort	bio-butanol production from glycerol with clostridium pasteurianum ch4: the effects of butyrate addition and in situ butanol removal via membrane distillation
title_auth	Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation
abstract	Background Clostridium pasteurianum CH4 was used to produce butanol from glycerol. The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration. Results Adding 6 g $ L^{−1} $ butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol)−1. Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g $ L^{−1} $, while the yield was also improved to 0.39 mol butanol (mol glycerol)−1. The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution. Conclusions The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. The VMD-based technology not only alleviates the inhibitory effect of butanol, but also markedly increases butanol concentration in the permeate after condensation, thereby making downstream processing easier and more cost-effective. © Lin et al. 2015
abstractGer	Background Clostridium pasteurianum CH4 was used to produce butanol from glycerol. The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration. Results Adding 6 g $ L^{−1} $ butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol)−1. Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g $ L^{−1} $, while the yield was also improved to 0.39 mol butanol (mol glycerol)−1. The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution. Conclusions The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. The VMD-based technology not only alleviates the inhibitory effect of butanol, but also markedly increases butanol concentration in the permeate after condensation, thereby making downstream processing easier and more cost-effective. © Lin et al. 2015
abstract_unstemmed	Background Clostridium pasteurianum CH4 was used to produce butanol from glycerol. The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration. Results Adding 6 g $ L^{−1} $ butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol)−1. Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g $ L^{−1} $, while the yield was also improved to 0.39 mol butanol (mol glycerol)−1. The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution. Conclusions The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. The VMD-based technology not only alleviates the inhibitory effect of butanol, but also markedly increases butanol concentration in the permeate after condensation, thereby making downstream processing easier and more cost-effective. © Lin et al. 2015
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title_short	Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation
url	https://dx.doi.org/10.1186/s13068-015-0352-6
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author2	Yen, Hong-Wei Kao, Wei-Chen Cheng, Chieh-Lun Chen, Wen-Ming Huang, Chieh-Chen Chang, Jo-Shu
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up_date	2024-07-03T14:16:00.172Z
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The performance of butanol fermentation was improved by adding butyrate as the precursor to trigger the metabolic pathway toward butanol production, and by combining this with in situ butanol removal via vacuum membrane distillation (VMD) to avoid the product inhibition arising from a high butanol concentration. Results Adding 6 g $ L^{−1} $ butyrate as precursor led to an increase in the butanol yield from 0.24 to 0.34 mol butanol (mol glycerol)−1. Combining VMD and butyrate addition strategies could further enhance the maximum effective butanol concentration to 29.8 g $ L^{−1} $, while the yield was also improved to 0.39 mol butanol (mol glycerol)−1. The butanol concentration in the permeate of VMD was nearly five times higher than that in the feeding solution. Conclusions The proposed butyrate addition and VMD in situ butanol removal strategies are very effective in enhancing both butanol titer and butanol yield. This would significantly enhance the economic feasibility of fermentative production of butanol. 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Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation

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