Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form

Abstract This study introduced an automated long‐term fermentation process for fungals grown in pellet form. The goal was to reduce the overgrowth of bioreactor internals and sensors while better rheological properties in the fermentation broth, such as oxygen transfer and mixing time, can be achiev...
Ausführliche Beschreibung

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Autor*in:	Winda Soerjawinata [verfasserIn] Isabelle Kockler [verfasserIn] Lars Wommer [verfasserIn] Robert Frank [verfasserIn] Anja Schüffler [verfasserIn] Tanja Schirmeister [verfasserIn] Roland Ulber [verfasserIn] Percy Kampeis [verfasserIn]

Format:	E-Artikel
Sprache:	Englisch

Erschienen:	2022

Schlagwörter:	bioreactor internals fungal growth fungal pellets repeated‐batch fermentation sporulation conditions

Übergeordnetes Werk:	In: Engineering in Life Sciences - Wiley-VCH, 2020, 22(2022), 7, Seite 474-483
Übergeordnetes Werk:	volume:22 ; year:2022 ; number:7 ; pages:474-483

Links:	Link aufrufen Link aufrufen Link aufrufen Journal toc Journal toc

DOI / URN:	10.1002/elsc.202100094

Katalog-ID:	DOAJ036065900

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520			\|a Abstract This study introduced an automated long‐term fermentation process for fungals grown in pellet form. The goal was to reduce the overgrowth of bioreactor internals and sensors while better rheological properties in the fermentation broth, such as oxygen transfer and mixing time, can be achieved. Because this could not be accomplished with continuous culture and fed‐batch fermentation, repeated‐batch fermentation was implemented with the help of additional bioreactor internals (“sporulation supports”). This should capture some biomass during fermentation. After harvesting the suspended biomass, intermediate cleaning was performed using a cleaning device. The biomass retained on the sporulation support went through the sporulation phase. The spores were subsequently used as inocula for the next batch. The reason for this approach was that the retained pellets could otherwise cause problems (e.g., overgrowth on sensors) in subsequent batches because the fungus would then show undesirable hyphal growth. Various sporulation supports were tested for sufficient biomass fixation to start the next batch. A reproducible spore concentration within the range of the requirements could be achieved by adjusting the sporulation support (design and construction material), and an intermediate cleaning adapted to this.
650		4	\|a bioreactor internals
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650		4	\|a sporulation conditions
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912			\|a GBV_ILN_110
912			\|a GBV_ILN_120
912			\|a GBV_ILN_138
912			\|a GBV_ILN_151
912			\|a GBV_ILN_161
912			\|a GBV_ILN_170
912			\|a GBV_ILN_171
912			\|a GBV_ILN_213
912			\|a GBV_ILN_224
912			\|a GBV_ILN_230
912			\|a GBV_ILN_266
912			\|a GBV_ILN_285
912			\|a GBV_ILN_293
912			\|a GBV_ILN_602
912			\|a GBV_ILN_636
912			\|a GBV_ILN_702
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allfields	10.1002/elsc.202100094 doi (DE-627)DOAJ036065900 (DE-599)DOAJc1491132795f44cc968c3eaabd04f0e3 DE-627 ger DE-627 rakwb eng TP248.13-248.65 Winda Soerjawinata verfasserin aut Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract This study introduced an automated long‐term fermentation process for fungals grown in pellet form. The goal was to reduce the overgrowth of bioreactor internals and sensors while better rheological properties in the fermentation broth, such as oxygen transfer and mixing time, can be achieved. Because this could not be accomplished with continuous culture and fed‐batch fermentation, repeated‐batch fermentation was implemented with the help of additional bioreactor internals (“sporulation supports”). This should capture some biomass during fermentation. After harvesting the suspended biomass, intermediate cleaning was performed using a cleaning device. The biomass retained on the sporulation support went through the sporulation phase. The spores were subsequently used as inocula for the next batch. The reason for this approach was that the retained pellets could otherwise cause problems (e.g., overgrowth on sensors) in subsequent batches because the fungus would then show undesirable hyphal growth. Various sporulation supports were tested for sufficient biomass fixation to start the next batch. A reproducible spore concentration within the range of the requirements could be achieved by adjusting the sporulation support (design and construction material), and an intermediate cleaning adapted to this. bioreactor internals fungal growth fungal pellets repeated‐batch fermentation sporulation conditions Biotechnology Isabelle Kockler verfasserin aut Lars Wommer verfasserin aut Robert Frank verfasserin aut Anja Schüffler verfasserin aut Tanja Schirmeister verfasserin aut Roland Ulber verfasserin aut Percy Kampeis verfasserin aut In Engineering in Life Sciences Wiley-VCH, 2020 22(2022), 7, Seite 474-483 (DE-627)341913782 (DE-600)2071199-2 16182863 nnns volume:22 year:2022 number:7 pages:474-483 https://doi.org/10.1002/elsc.202100094 kostenfrei https://doaj.org/article/c1491132795f44cc968c3eaabd04f0e3 kostenfrei https://doi.org/10.1002/elsc.202100094 kostenfrei https://doaj.org/toc/1618-0240 Journal toc kostenfrei https://doaj.org/toc/1618-2863 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_266 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2360 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4012 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4249 GBV_ILN_4251 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_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 22 2022 7 474-483
spelling	10.1002/elsc.202100094 doi (DE-627)DOAJ036065900 (DE-599)DOAJc1491132795f44cc968c3eaabd04f0e3 DE-627 ger DE-627 rakwb eng TP248.13-248.65 Winda Soerjawinata verfasserin aut Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract This study introduced an automated long‐term fermentation process for fungals grown in pellet form. The goal was to reduce the overgrowth of bioreactor internals and sensors while better rheological properties in the fermentation broth, such as oxygen transfer and mixing time, can be achieved. Because this could not be accomplished with continuous culture and fed‐batch fermentation, repeated‐batch fermentation was implemented with the help of additional bioreactor internals (“sporulation supports”). This should capture some biomass during fermentation. After harvesting the suspended biomass, intermediate cleaning was performed using a cleaning device. The biomass retained on the sporulation support went through the sporulation phase. The spores were subsequently used as inocula for the next batch. The reason for this approach was that the retained pellets could otherwise cause problems (e.g., overgrowth on sensors) in subsequent batches because the fungus would then show undesirable hyphal growth. Various sporulation supports were tested for sufficient biomass fixation to start the next batch. A reproducible spore concentration within the range of the requirements could be achieved by adjusting the sporulation support (design and construction material), and an intermediate cleaning adapted to this. bioreactor internals fungal growth fungal pellets repeated‐batch fermentation sporulation conditions Biotechnology Isabelle Kockler verfasserin aut Lars Wommer verfasserin aut Robert Frank verfasserin aut Anja Schüffler verfasserin aut Tanja Schirmeister verfasserin aut Roland Ulber verfasserin aut Percy Kampeis verfasserin aut In Engineering in Life Sciences Wiley-VCH, 2020 22(2022), 7, Seite 474-483 (DE-627)341913782 (DE-600)2071199-2 16182863 nnns volume:22 year:2022 number:7 pages:474-483 https://doi.org/10.1002/elsc.202100094 kostenfrei https://doaj.org/article/c1491132795f44cc968c3eaabd04f0e3 kostenfrei https://doi.org/10.1002/elsc.202100094 kostenfrei https://doaj.org/toc/1618-0240 Journal toc kostenfrei https://doaj.org/toc/1618-2863 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_266 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2360 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4012 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4249 GBV_ILN_4251 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_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 22 2022 7 474-483
allfields_unstemmed	10.1002/elsc.202100094 doi (DE-627)DOAJ036065900 (DE-599)DOAJc1491132795f44cc968c3eaabd04f0e3 DE-627 ger DE-627 rakwb eng TP248.13-248.65 Winda Soerjawinata verfasserin aut Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract This study introduced an automated long‐term fermentation process for fungals grown in pellet form. The goal was to reduce the overgrowth of bioreactor internals and sensors while better rheological properties in the fermentation broth, such as oxygen transfer and mixing time, can be achieved. Because this could not be accomplished with continuous culture and fed‐batch fermentation, repeated‐batch fermentation was implemented with the help of additional bioreactor internals (“sporulation supports”). This should capture some biomass during fermentation. After harvesting the suspended biomass, intermediate cleaning was performed using a cleaning device. The biomass retained on the sporulation support went through the sporulation phase. The spores were subsequently used as inocula for the next batch. The reason for this approach was that the retained pellets could otherwise cause problems (e.g., overgrowth on sensors) in subsequent batches because the fungus would then show undesirable hyphal growth. Various sporulation supports were tested for sufficient biomass fixation to start the next batch. A reproducible spore concentration within the range of the requirements could be achieved by adjusting the sporulation support (design and construction material), and an intermediate cleaning adapted to this. bioreactor internals fungal growth fungal pellets repeated‐batch fermentation sporulation conditions Biotechnology Isabelle Kockler verfasserin aut Lars Wommer verfasserin aut Robert Frank verfasserin aut Anja Schüffler verfasserin aut Tanja Schirmeister verfasserin aut Roland Ulber verfasserin aut Percy Kampeis verfasserin aut In Engineering in Life Sciences Wiley-VCH, 2020 22(2022), 7, Seite 474-483 (DE-627)341913782 (DE-600)2071199-2 16182863 nnns volume:22 year:2022 number:7 pages:474-483 https://doi.org/10.1002/elsc.202100094 kostenfrei https://doaj.org/article/c1491132795f44cc968c3eaabd04f0e3 kostenfrei https://doi.org/10.1002/elsc.202100094 kostenfrei https://doaj.org/toc/1618-0240 Journal toc kostenfrei https://doaj.org/toc/1618-2863 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_266 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2360 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4012 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4249 GBV_ILN_4251 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_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 22 2022 7 474-483
allfieldsGer	10.1002/elsc.202100094 doi (DE-627)DOAJ036065900 (DE-599)DOAJc1491132795f44cc968c3eaabd04f0e3 DE-627 ger DE-627 rakwb eng TP248.13-248.65 Winda Soerjawinata verfasserin aut Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract This study introduced an automated long‐term fermentation process for fungals grown in pellet form. The goal was to reduce the overgrowth of bioreactor internals and sensors while better rheological properties in the fermentation broth, such as oxygen transfer and mixing time, can be achieved. Because this could not be accomplished with continuous culture and fed‐batch fermentation, repeated‐batch fermentation was implemented with the help of additional bioreactor internals (“sporulation supports”). This should capture some biomass during fermentation. After harvesting the suspended biomass, intermediate cleaning was performed using a cleaning device. The biomass retained on the sporulation support went through the sporulation phase. The spores were subsequently used as inocula for the next batch. The reason for this approach was that the retained pellets could otherwise cause problems (e.g., overgrowth on sensors) in subsequent batches because the fungus would then show undesirable hyphal growth. Various sporulation supports were tested for sufficient biomass fixation to start the next batch. A reproducible spore concentration within the range of the requirements could be achieved by adjusting the sporulation support (design and construction material), and an intermediate cleaning adapted to this. bioreactor internals fungal growth fungal pellets repeated‐batch fermentation sporulation conditions Biotechnology Isabelle Kockler verfasserin aut Lars Wommer verfasserin aut Robert Frank verfasserin aut Anja Schüffler verfasserin aut Tanja Schirmeister verfasserin aut Roland Ulber verfasserin aut Percy Kampeis verfasserin aut In Engineering in Life Sciences Wiley-VCH, 2020 22(2022), 7, Seite 474-483 (DE-627)341913782 (DE-600)2071199-2 16182863 nnns volume:22 year:2022 number:7 pages:474-483 https://doi.org/10.1002/elsc.202100094 kostenfrei https://doaj.org/article/c1491132795f44cc968c3eaabd04f0e3 kostenfrei https://doi.org/10.1002/elsc.202100094 kostenfrei https://doaj.org/toc/1618-0240 Journal toc kostenfrei https://doaj.org/toc/1618-2863 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_266 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2360 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4012 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4249 GBV_ILN_4251 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_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 22 2022 7 474-483
allfieldsSound	10.1002/elsc.202100094 doi (DE-627)DOAJ036065900 (DE-599)DOAJc1491132795f44cc968c3eaabd04f0e3 DE-627 ger DE-627 rakwb eng TP248.13-248.65 Winda Soerjawinata verfasserin aut Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract This study introduced an automated long‐term fermentation process for fungals grown in pellet form. The goal was to reduce the overgrowth of bioreactor internals and sensors while better rheological properties in the fermentation broth, such as oxygen transfer and mixing time, can be achieved. Because this could not be accomplished with continuous culture and fed‐batch fermentation, repeated‐batch fermentation was implemented with the help of additional bioreactor internals (“sporulation supports”). This should capture some biomass during fermentation. After harvesting the suspended biomass, intermediate cleaning was performed using a cleaning device. The biomass retained on the sporulation support went through the sporulation phase. The spores were subsequently used as inocula for the next batch. The reason for this approach was that the retained pellets could otherwise cause problems (e.g., overgrowth on sensors) in subsequent batches because the fungus would then show undesirable hyphal growth. Various sporulation supports were tested for sufficient biomass fixation to start the next batch. A reproducible spore concentration within the range of the requirements could be achieved by adjusting the sporulation support (design and construction material), and an intermediate cleaning adapted to this. bioreactor internals fungal growth fungal pellets repeated‐batch fermentation sporulation conditions Biotechnology Isabelle Kockler verfasserin aut Lars Wommer verfasserin aut Robert Frank verfasserin aut Anja Schüffler verfasserin aut Tanja Schirmeister verfasserin aut Roland Ulber verfasserin aut Percy Kampeis verfasserin aut In Engineering in Life Sciences Wiley-VCH, 2020 22(2022), 7, Seite 474-483 (DE-627)341913782 (DE-600)2071199-2 16182863 nnns volume:22 year:2022 number:7 pages:474-483 https://doi.org/10.1002/elsc.202100094 kostenfrei https://doaj.org/article/c1491132795f44cc968c3eaabd04f0e3 kostenfrei https://doi.org/10.1002/elsc.202100094 kostenfrei https://doaj.org/toc/1618-0240 Journal toc kostenfrei https://doaj.org/toc/1618-2863 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_266 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2118 GBV_ILN_2122 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2360 GBV_ILN_2470 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_4012 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4249 GBV_ILN_4251 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_4326 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 22 2022 7 474-483
language	English
source	In Engineering in Life Sciences 22(2022), 7, Seite 474-483 volume:22 year:2022 number:7 pages:474-483
sourceStr	In Engineering in Life Sciences 22(2022), 7, Seite 474-483 volume:22 year:2022 number:7 pages:474-483
format_phy_str_mv	Article
institution	findex.gbv.de
topic_facet	bioreactor internals fungal growth fungal pellets repeated‐batch fermentation sporulation conditions Biotechnology
isfreeaccess_bool	true
container_title	Engineering in Life Sciences
authorswithroles_txt_mv	Winda Soerjawinata @@aut@@ Isabelle Kockler @@aut@@ Lars Wommer @@aut@@ Robert Frank @@aut@@ Anja Schüffler @@aut@@ Tanja Schirmeister @@aut@@ Roland Ulber @@aut@@ Percy Kampeis @@aut@@
publishDateDaySort_date	2022-01-01T00:00:00Z
hierarchy_top_id	341913782
id	DOAJ036065900
language_de	englisch
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callnumber-first	T - Technology
author	Winda Soerjawinata
spellingShingle	Winda Soerjawinata misc TP248.13-248.65 misc bioreactor internals misc fungal growth misc fungal pellets misc repeated‐batch fermentation misc sporulation conditions misc Biotechnology Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form
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topic_title	TP248.13-248.65 Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form bioreactor internals fungal growth fungal pellets repeated‐batch fermentation sporulation conditions
topic	misc TP248.13-248.65 misc bioreactor internals misc fungal growth misc fungal pellets misc repeated‐batch fermentation misc sporulation conditions misc Biotechnology
topic_unstemmed	misc TP248.13-248.65 misc bioreactor internals misc fungal growth misc fungal pellets misc repeated‐batch fermentation misc sporulation conditions misc Biotechnology
topic_browse	misc TP248.13-248.65 misc bioreactor internals misc fungal growth misc fungal pellets misc repeated‐batch fermentation misc sporulation conditions misc Biotechnology
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title	Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form
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title_full	Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form
author_sort	Winda Soerjawinata
journal	Engineering in Life Sciences
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author_browse	Winda Soerjawinata Isabelle Kockler Lars Wommer Robert Frank Anja Schüffler Tanja Schirmeister Roland Ulber Percy Kampeis
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title_sort	novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form
callnumber	TP248.13-248.65
title_auth	Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form
abstract	Abstract This study introduced an automated long‐term fermentation process for fungals grown in pellet form. The goal was to reduce the overgrowth of bioreactor internals and sensors while better rheological properties in the fermentation broth, such as oxygen transfer and mixing time, can be achieved. Because this could not be accomplished with continuous culture and fed‐batch fermentation, repeated‐batch fermentation was implemented with the help of additional bioreactor internals (“sporulation supports”). This should capture some biomass during fermentation. After harvesting the suspended biomass, intermediate cleaning was performed using a cleaning device. The biomass retained on the sporulation support went through the sporulation phase. The spores were subsequently used as inocula for the next batch. The reason for this approach was that the retained pellets could otherwise cause problems (e.g., overgrowth on sensors) in subsequent batches because the fungus would then show undesirable hyphal growth. Various sporulation supports were tested for sufficient biomass fixation to start the next batch. A reproducible spore concentration within the range of the requirements could be achieved by adjusting the sporulation support (design and construction material), and an intermediate cleaning adapted to this.
abstractGer	Abstract This study introduced an automated long‐term fermentation process for fungals grown in pellet form. The goal was to reduce the overgrowth of bioreactor internals and sensors while better rheological properties in the fermentation broth, such as oxygen transfer and mixing time, can be achieved. Because this could not be accomplished with continuous culture and fed‐batch fermentation, repeated‐batch fermentation was implemented with the help of additional bioreactor internals (“sporulation supports”). This should capture some biomass during fermentation. After harvesting the suspended biomass, intermediate cleaning was performed using a cleaning device. The biomass retained on the sporulation support went through the sporulation phase. The spores were subsequently used as inocula for the next batch. The reason for this approach was that the retained pellets could otherwise cause problems (e.g., overgrowth on sensors) in subsequent batches because the fungus would then show undesirable hyphal growth. Various sporulation supports were tested for sufficient biomass fixation to start the next batch. A reproducible spore concentration within the range of the requirements could be achieved by adjusting the sporulation support (design and construction material), and an intermediate cleaning adapted to this.
abstract_unstemmed	Abstract This study introduced an automated long‐term fermentation process for fungals grown in pellet form. The goal was to reduce the overgrowth of bioreactor internals and sensors while better rheological properties in the fermentation broth, such as oxygen transfer and mixing time, can be achieved. Because this could not be accomplished with continuous culture and fed‐batch fermentation, repeated‐batch fermentation was implemented with the help of additional bioreactor internals (“sporulation supports”). This should capture some biomass during fermentation. After harvesting the suspended biomass, intermediate cleaning was performed using a cleaning device. The biomass retained on the sporulation support went through the sporulation phase. The spores were subsequently used as inocula for the next batch. The reason for this approach was that the retained pellets could otherwise cause problems (e.g., overgrowth on sensors) in subsequent batches because the fungus would then show undesirable hyphal growth. Various sporulation supports were tested for sufficient biomass fixation to start the next batch. A reproducible spore concentration within the range of the requirements could be achieved by adjusting the sporulation support (design and construction material), and an intermediate cleaning adapted to this.
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title_short	Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form
url	https://doi.org/10.1002/elsc.202100094 https://doaj.org/article/c1491132795f44cc968c3eaabd04f0e3 https://doaj.org/toc/1618-0240 https://doaj.org/toc/1618-2863
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up_date	2024-07-03T18:29:29.467Z
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Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form

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