Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan
Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope f...
Ausführliche Beschreibung
Autor*in: |
Shaikh, Samrin S. [verfasserIn] |
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Englisch |
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2023 |
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© The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
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Übergeordnetes Werk: |
Enthalten in: Waste and biomass valorization - [Dordrecht] : Springer Netherlands, 2010, 14(2023), 12 vom: 11. Apr., Seite 4201-4214 |
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Übergeordnetes Werk: |
volume:14 ; year:2023 ; number:12 ; day:11 ; month:04 ; pages:4201-4214 |
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DOI / URN: |
10.1007/s12649-023-02127-2 |
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Katalog-ID: |
SPR053656113 |
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520 | |a Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope for its exploration which may prove to be economically beneficial to the society. Heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) to N-substituted aromatic heterocyclic furan derivatives is reported for the very first time. Cost effective and stable metal oxide catalysts were deployed for the transformation. Catalyst screening study showed that $ La_{2} %$ O_{3} $ was found to be an excellent catalyst for N-acetyl glucosamine (NAG) dehydration which mainly produced 3-acetamidofuran (3AF). Methods The physicochemical properties of the metal oxide catalyst were investigated by various techniques such as XRD, FTIR, MeOH-FTIR, TPD, SEM, $ N_{2} $ sorption studies and HR-TEM analysis for structure activity relationship. Results The effect of various reaction parameters such as catalyst concentration, reaction temperature, reaction time and solvent effect on dehydration of N-acetyl glucosamine has been studied in detail for higher yields. The results revealed that the presence of weak basic sites which are Brønsted in nature and nano pores present on the surface were responsible for improved dehydration of the chitin biomass to selectively yield 3-acetamidofuran (3AF). $ La_{2} %$ O_{3} $ catalyst showed optimum 50% 3AF yield from N-acetyl glucosamine at 180 °C in 3 h. Conclusion Efficacious exploitation of marine biomass to value added chemicals using heterogeneous catalysts can be extensively exploited. Separation of N-substituted heterocyclic aromatics is the most innovative aspect of the current study. Thus, utilization of heterogeneous catalyst and renewable biomass as a raw material indicates a transition towards more sustainable and greener approach. Graphical Abstract With reference to valorization of biomass waste towards sustainability. We report for the first time heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) over $ La_{2} %$ O_{3} $ catalyst to yield 50% 3-acetamido furan (3AF) and 20% 3-acetamido-5-acetylfuran with 100% NAG conversion. The superior performance of $ La_{2} %$ O_{3} $ catalyst was attributed to the presence of brønsted basicity and nanopores present at catalysts surface. | ||
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10.1007/s12649-023-02127-2 doi (DE-627)SPR053656113 (SPR)s12649-023-02127-2-e DE-627 ger DE-627 rakwb eng Shaikh, Samrin S. verfasserin aut Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan 2023 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope for its exploration which may prove to be economically beneficial to the society. Heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) to N-substituted aromatic heterocyclic furan derivatives is reported for the very first time. Cost effective and stable metal oxide catalysts were deployed for the transformation. Catalyst screening study showed that $ La_{2} %$ O_{3} $ was found to be an excellent catalyst for N-acetyl glucosamine (NAG) dehydration which mainly produced 3-acetamidofuran (3AF). Methods The physicochemical properties of the metal oxide catalyst were investigated by various techniques such as XRD, FTIR, MeOH-FTIR, TPD, SEM, $ N_{2} $ sorption studies and HR-TEM analysis for structure activity relationship. Results The effect of various reaction parameters such as catalyst concentration, reaction temperature, reaction time and solvent effect on dehydration of N-acetyl glucosamine has been studied in detail for higher yields. The results revealed that the presence of weak basic sites which are Brønsted in nature and nano pores present on the surface were responsible for improved dehydration of the chitin biomass to selectively yield 3-acetamidofuran (3AF). $ La_{2} %$ O_{3} $ catalyst showed optimum 50% 3AF yield from N-acetyl glucosamine at 180 °C in 3 h. Conclusion Efficacious exploitation of marine biomass to value added chemicals using heterogeneous catalysts can be extensively exploited. Separation of N-substituted heterocyclic aromatics is the most innovative aspect of the current study. Thus, utilization of heterogeneous catalyst and renewable biomass as a raw material indicates a transition towards more sustainable and greener approach. Graphical Abstract With reference to valorization of biomass waste towards sustainability. We report for the first time heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) over $ La_{2} %$ O_{3} $ catalyst to yield 50% 3-acetamido furan (3AF) and 20% 3-acetamido-5-acetylfuran with 100% NAG conversion. The superior performance of $ La_{2} %$ O_{3} $ catalyst was attributed to the presence of brønsted basicity and nanopores present at catalysts surface. Lanthanum oxide (dpeaa)DE-He213 N-acetyl-D-glucosamine (dpeaa)DE-He213 Heterogeneous catalysis (dpeaa)DE-He213 Dehydration (dpeaa)DE-He213 Renewable feedstock (dpeaa)DE-He213 3-acetamidofuran (dpeaa)DE-He213 3-acetamido-5-acetylfuran (dpeaa)DE-He213 Patil, Chetana R. aut Lucas, Nishita aut Bokade, Vijay V. aut Rode, Chandrashekhar V. (orcid)0000-0002-2093-2708 aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 14(2023), 12 vom: 11. Apr., Seite 4201-4214 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:14 year:2023 number:12 day:11 month:04 pages:4201-4214 https://dx.doi.org/10.1007/s12649-023-02127-2 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 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_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 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_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 14 2023 12 11 04 4201-4214 |
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10.1007/s12649-023-02127-2 doi (DE-627)SPR053656113 (SPR)s12649-023-02127-2-e DE-627 ger DE-627 rakwb eng Shaikh, Samrin S. verfasserin aut Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan 2023 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope for its exploration which may prove to be economically beneficial to the society. Heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) to N-substituted aromatic heterocyclic furan derivatives is reported for the very first time. Cost effective and stable metal oxide catalysts were deployed for the transformation. Catalyst screening study showed that $ La_{2} %$ O_{3} $ was found to be an excellent catalyst for N-acetyl glucosamine (NAG) dehydration which mainly produced 3-acetamidofuran (3AF). Methods The physicochemical properties of the metal oxide catalyst were investigated by various techniques such as XRD, FTIR, MeOH-FTIR, TPD, SEM, $ N_{2} $ sorption studies and HR-TEM analysis for structure activity relationship. Results The effect of various reaction parameters such as catalyst concentration, reaction temperature, reaction time and solvent effect on dehydration of N-acetyl glucosamine has been studied in detail for higher yields. The results revealed that the presence of weak basic sites which are Brønsted in nature and nano pores present on the surface were responsible for improved dehydration of the chitin biomass to selectively yield 3-acetamidofuran (3AF). $ La_{2} %$ O_{3} $ catalyst showed optimum 50% 3AF yield from N-acetyl glucosamine at 180 °C in 3 h. Conclusion Efficacious exploitation of marine biomass to value added chemicals using heterogeneous catalysts can be extensively exploited. Separation of N-substituted heterocyclic aromatics is the most innovative aspect of the current study. Thus, utilization of heterogeneous catalyst and renewable biomass as a raw material indicates a transition towards more sustainable and greener approach. Graphical Abstract With reference to valorization of biomass waste towards sustainability. We report for the first time heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) over $ La_{2} %$ O_{3} $ catalyst to yield 50% 3-acetamido furan (3AF) and 20% 3-acetamido-5-acetylfuran with 100% NAG conversion. The superior performance of $ La_{2} %$ O_{3} $ catalyst was attributed to the presence of brønsted basicity and nanopores present at catalysts surface. Lanthanum oxide (dpeaa)DE-He213 N-acetyl-D-glucosamine (dpeaa)DE-He213 Heterogeneous catalysis (dpeaa)DE-He213 Dehydration (dpeaa)DE-He213 Renewable feedstock (dpeaa)DE-He213 3-acetamidofuran (dpeaa)DE-He213 3-acetamido-5-acetylfuran (dpeaa)DE-He213 Patil, Chetana R. aut Lucas, Nishita aut Bokade, Vijay V. aut Rode, Chandrashekhar V. (orcid)0000-0002-2093-2708 aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 14(2023), 12 vom: 11. Apr., Seite 4201-4214 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:14 year:2023 number:12 day:11 month:04 pages:4201-4214 https://dx.doi.org/10.1007/s12649-023-02127-2 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 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_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 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_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 14 2023 12 11 04 4201-4214 |
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10.1007/s12649-023-02127-2 doi (DE-627)SPR053656113 (SPR)s12649-023-02127-2-e DE-627 ger DE-627 rakwb eng Shaikh, Samrin S. verfasserin aut Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan 2023 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope for its exploration which may prove to be economically beneficial to the society. Heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) to N-substituted aromatic heterocyclic furan derivatives is reported for the very first time. Cost effective and stable metal oxide catalysts were deployed for the transformation. Catalyst screening study showed that $ La_{2} %$ O_{3} $ was found to be an excellent catalyst for N-acetyl glucosamine (NAG) dehydration which mainly produced 3-acetamidofuran (3AF). Methods The physicochemical properties of the metal oxide catalyst were investigated by various techniques such as XRD, FTIR, MeOH-FTIR, TPD, SEM, $ N_{2} $ sorption studies and HR-TEM analysis for structure activity relationship. Results The effect of various reaction parameters such as catalyst concentration, reaction temperature, reaction time and solvent effect on dehydration of N-acetyl glucosamine has been studied in detail for higher yields. The results revealed that the presence of weak basic sites which are Brønsted in nature and nano pores present on the surface were responsible for improved dehydration of the chitin biomass to selectively yield 3-acetamidofuran (3AF). $ La_{2} %$ O_{3} $ catalyst showed optimum 50% 3AF yield from N-acetyl glucosamine at 180 °C in 3 h. Conclusion Efficacious exploitation of marine biomass to value added chemicals using heterogeneous catalysts can be extensively exploited. Separation of N-substituted heterocyclic aromatics is the most innovative aspect of the current study. Thus, utilization of heterogeneous catalyst and renewable biomass as a raw material indicates a transition towards more sustainable and greener approach. Graphical Abstract With reference to valorization of biomass waste towards sustainability. We report for the first time heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) over $ La_{2} %$ O_{3} $ catalyst to yield 50% 3-acetamido furan (3AF) and 20% 3-acetamido-5-acetylfuran with 100% NAG conversion. The superior performance of $ La_{2} %$ O_{3} $ catalyst was attributed to the presence of brønsted basicity and nanopores present at catalysts surface. Lanthanum oxide (dpeaa)DE-He213 N-acetyl-D-glucosamine (dpeaa)DE-He213 Heterogeneous catalysis (dpeaa)DE-He213 Dehydration (dpeaa)DE-He213 Renewable feedstock (dpeaa)DE-He213 3-acetamidofuran (dpeaa)DE-He213 3-acetamido-5-acetylfuran (dpeaa)DE-He213 Patil, Chetana R. aut Lucas, Nishita aut Bokade, Vijay V. aut Rode, Chandrashekhar V. (orcid)0000-0002-2093-2708 aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 14(2023), 12 vom: 11. Apr., Seite 4201-4214 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:14 year:2023 number:12 day:11 month:04 pages:4201-4214 https://dx.doi.org/10.1007/s12649-023-02127-2 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 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_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 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_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 14 2023 12 11 04 4201-4214 |
allfieldsGer |
10.1007/s12649-023-02127-2 doi (DE-627)SPR053656113 (SPR)s12649-023-02127-2-e DE-627 ger DE-627 rakwb eng Shaikh, Samrin S. verfasserin aut Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan 2023 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope for its exploration which may prove to be economically beneficial to the society. Heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) to N-substituted aromatic heterocyclic furan derivatives is reported for the very first time. Cost effective and stable metal oxide catalysts were deployed for the transformation. Catalyst screening study showed that $ La_{2} %$ O_{3} $ was found to be an excellent catalyst for N-acetyl glucosamine (NAG) dehydration which mainly produced 3-acetamidofuran (3AF). Methods The physicochemical properties of the metal oxide catalyst were investigated by various techniques such as XRD, FTIR, MeOH-FTIR, TPD, SEM, $ N_{2} $ sorption studies and HR-TEM analysis for structure activity relationship. Results The effect of various reaction parameters such as catalyst concentration, reaction temperature, reaction time and solvent effect on dehydration of N-acetyl glucosamine has been studied in detail for higher yields. The results revealed that the presence of weak basic sites which are Brønsted in nature and nano pores present on the surface were responsible for improved dehydration of the chitin biomass to selectively yield 3-acetamidofuran (3AF). $ La_{2} %$ O_{3} $ catalyst showed optimum 50% 3AF yield from N-acetyl glucosamine at 180 °C in 3 h. Conclusion Efficacious exploitation of marine biomass to value added chemicals using heterogeneous catalysts can be extensively exploited. Separation of N-substituted heterocyclic aromatics is the most innovative aspect of the current study. Thus, utilization of heterogeneous catalyst and renewable biomass as a raw material indicates a transition towards more sustainable and greener approach. Graphical Abstract With reference to valorization of biomass waste towards sustainability. We report for the first time heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) over $ La_{2} %$ O_{3} $ catalyst to yield 50% 3-acetamido furan (3AF) and 20% 3-acetamido-5-acetylfuran with 100% NAG conversion. The superior performance of $ La_{2} %$ O_{3} $ catalyst was attributed to the presence of brønsted basicity and nanopores present at catalysts surface. Lanthanum oxide (dpeaa)DE-He213 N-acetyl-D-glucosamine (dpeaa)DE-He213 Heterogeneous catalysis (dpeaa)DE-He213 Dehydration (dpeaa)DE-He213 Renewable feedstock (dpeaa)DE-He213 3-acetamidofuran (dpeaa)DE-He213 3-acetamido-5-acetylfuran (dpeaa)DE-He213 Patil, Chetana R. aut Lucas, Nishita aut Bokade, Vijay V. aut Rode, Chandrashekhar V. (orcid)0000-0002-2093-2708 aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 14(2023), 12 vom: 11. Apr., Seite 4201-4214 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:14 year:2023 number:12 day:11 month:04 pages:4201-4214 https://dx.doi.org/10.1007/s12649-023-02127-2 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 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_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 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_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 14 2023 12 11 04 4201-4214 |
allfieldsSound |
10.1007/s12649-023-02127-2 doi (DE-627)SPR053656113 (SPR)s12649-023-02127-2-e DE-627 ger DE-627 rakwb eng Shaikh, Samrin S. verfasserin aut Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan 2023 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope for its exploration which may prove to be economically beneficial to the society. Heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) to N-substituted aromatic heterocyclic furan derivatives is reported for the very first time. Cost effective and stable metal oxide catalysts were deployed for the transformation. Catalyst screening study showed that $ La_{2} %$ O_{3} $ was found to be an excellent catalyst for N-acetyl glucosamine (NAG) dehydration which mainly produced 3-acetamidofuran (3AF). Methods The physicochemical properties of the metal oxide catalyst were investigated by various techniques such as XRD, FTIR, MeOH-FTIR, TPD, SEM, $ N_{2} $ sorption studies and HR-TEM analysis for structure activity relationship. Results The effect of various reaction parameters such as catalyst concentration, reaction temperature, reaction time and solvent effect on dehydration of N-acetyl glucosamine has been studied in detail for higher yields. The results revealed that the presence of weak basic sites which are Brønsted in nature and nano pores present on the surface were responsible for improved dehydration of the chitin biomass to selectively yield 3-acetamidofuran (3AF). $ La_{2} %$ O_{3} $ catalyst showed optimum 50% 3AF yield from N-acetyl glucosamine at 180 °C in 3 h. Conclusion Efficacious exploitation of marine biomass to value added chemicals using heterogeneous catalysts can be extensively exploited. Separation of N-substituted heterocyclic aromatics is the most innovative aspect of the current study. Thus, utilization of heterogeneous catalyst and renewable biomass as a raw material indicates a transition towards more sustainable and greener approach. Graphical Abstract With reference to valorization of biomass waste towards sustainability. We report for the first time heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) over $ La_{2} %$ O_{3} $ catalyst to yield 50% 3-acetamido furan (3AF) and 20% 3-acetamido-5-acetylfuran with 100% NAG conversion. The superior performance of $ La_{2} %$ O_{3} $ catalyst was attributed to the presence of brønsted basicity and nanopores present at catalysts surface. Lanthanum oxide (dpeaa)DE-He213 N-acetyl-D-glucosamine (dpeaa)DE-He213 Heterogeneous catalysis (dpeaa)DE-He213 Dehydration (dpeaa)DE-He213 Renewable feedstock (dpeaa)DE-He213 3-acetamidofuran (dpeaa)DE-He213 3-acetamido-5-acetylfuran (dpeaa)DE-He213 Patil, Chetana R. aut Lucas, Nishita aut Bokade, Vijay V. aut Rode, Chandrashekhar V. (orcid)0000-0002-2093-2708 aut Enthalten in Waste and biomass valorization [Dordrecht] : Springer Netherlands, 2010 14(2023), 12 vom: 11. Apr., Seite 4201-4214 (DE-627)620147245 (DE-600)2541900-6 1877-265X nnns volume:14 year:2023 number:12 day:11 month:04 pages:4201-4214 https://dx.doi.org/10.1007/s12649-023-02127-2 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 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_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 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_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 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_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 14 2023 12 11 04 4201-4214 |
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Enthalten in Waste and biomass valorization 14(2023), 12 vom: 11. Apr., Seite 4201-4214 volume:14 year:2023 number:12 day:11 month:04 pages:4201-4214 |
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Lanthanum oxide N-acetyl-D-glucosamine Heterogeneous catalysis Dehydration Renewable feedstock 3-acetamidofuran 3-acetamido-5-acetylfuran |
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Shaikh, Samrin S. @@aut@@ Patil, Chetana R. @@aut@@ Lucas, Nishita @@aut@@ Bokade, Vijay V. @@aut@@ Rode, Chandrashekhar V. @@aut@@ |
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SPR053656113 |
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englisch |
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<?xml version="1.0" encoding="UTF-8"?><collection xmlns="http://www.loc.gov/MARC21/slim"><record><leader>01000naa a22002652 4500</leader><controlfield tag="001">SPR053656113</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20231108064639.0</controlfield><controlfield tag="007">cr uuu---uuuuu</controlfield><controlfield tag="008">231108s2023 xx |||||o 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1007/s12649-023-02127-2</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)SPR053656113</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(SPR)s12649-023-02127-2-e</subfield></datafield><datafield tag="040" ind1=" " ind2=" "><subfield code="a">DE-627</subfield><subfield code="b">ger</subfield><subfield code="c">DE-627</subfield><subfield code="e">rakwb</subfield></datafield><datafield tag="041" ind1=" " ind2=" "><subfield code="a">eng</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Shaikh, Samrin S.</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2023</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">Computermedien</subfield><subfield code="b">c</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Online-Ressource</subfield><subfield code="b">cr</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="500" ind1=" " ind2=" "><subfield code="a">© The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law.</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope for its exploration which may prove to be economically beneficial to the society. Heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) to N-substituted aromatic heterocyclic furan derivatives is reported for the very first time. Cost effective and stable metal oxide catalysts were deployed for the transformation. Catalyst screening study showed that $ La_{2} %$ O_{3} $ was found to be an excellent catalyst for N-acetyl glucosamine (NAG) dehydration which mainly produced 3-acetamidofuran (3AF). Methods The physicochemical properties of the metal oxide catalyst were investigated by various techniques such as XRD, FTIR, MeOH-FTIR, TPD, SEM, $ N_{2} $ sorption studies and HR-TEM analysis for structure activity relationship. Results The effect of various reaction parameters such as catalyst concentration, reaction temperature, reaction time and solvent effect on dehydration of N-acetyl glucosamine has been studied in detail for higher yields. The results revealed that the presence of weak basic sites which are Brønsted in nature and nano pores present on the surface were responsible for improved dehydration of the chitin biomass to selectively yield 3-acetamidofuran (3AF). $ La_{2} %$ O_{3} $ catalyst showed optimum 50% 3AF yield from N-acetyl glucosamine at 180 °C in 3 h. Conclusion Efficacious exploitation of marine biomass to value added chemicals using heterogeneous catalysts can be extensively exploited. Separation of N-substituted heterocyclic aromatics is the most innovative aspect of the current study. Thus, utilization of heterogeneous catalyst and renewable biomass as a raw material indicates a transition towards more sustainable and greener approach. Graphical Abstract With reference to valorization of biomass waste towards sustainability. We report for the first time heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) over $ La_{2} %$ O_{3} $ catalyst to yield 50% 3-acetamido furan (3AF) and 20% 3-acetamido-5-acetylfuran with 100% NAG conversion. 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|
author |
Shaikh, Samrin S. |
spellingShingle |
Shaikh, Samrin S. misc Lanthanum oxide misc N-acetyl-D-glucosamine misc Heterogeneous catalysis misc Dehydration misc Renewable feedstock misc 3-acetamidofuran misc 3-acetamido-5-acetylfuran Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan |
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Shaikh, Samrin S. |
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topic_title |
Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan Lanthanum oxide (dpeaa)DE-He213 N-acetyl-D-glucosamine (dpeaa)DE-He213 Heterogeneous catalysis (dpeaa)DE-He213 Dehydration (dpeaa)DE-He213 Renewable feedstock (dpeaa)DE-He213 3-acetamidofuran (dpeaa)DE-He213 3-acetamido-5-acetylfuran (dpeaa)DE-He213 |
topic |
misc Lanthanum oxide misc N-acetyl-D-glucosamine misc Heterogeneous catalysis misc Dehydration misc Renewable feedstock misc 3-acetamidofuran misc 3-acetamido-5-acetylfuran |
topic_unstemmed |
misc Lanthanum oxide misc N-acetyl-D-glucosamine misc Heterogeneous catalysis misc Dehydration misc Renewable feedstock misc 3-acetamidofuran misc 3-acetamido-5-acetylfuran |
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misc Lanthanum oxide misc N-acetyl-D-glucosamine misc Heterogeneous catalysis misc Dehydration misc Renewable feedstock misc 3-acetamidofuran misc 3-acetamido-5-acetylfuran |
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Elektronische Aufsätze Aufsätze Elektronische Ressource |
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title |
Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan |
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Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan |
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Shaikh, Samrin S. Patil, Chetana R. Lucas, Nishita Bokade, Vijay V. Rode, Chandrashekhar V. |
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direct conversion of n-acetyl-d-glucosamine to n-containing heterocyclic compounds 3-acetamidofuran and 3-acetamido-5-acetyl furan |
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Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan |
abstract |
Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope for its exploration which may prove to be economically beneficial to the society. Heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) to N-substituted aromatic heterocyclic furan derivatives is reported for the very first time. Cost effective and stable metal oxide catalysts were deployed for the transformation. Catalyst screening study showed that $ La_{2} %$ O_{3} $ was found to be an excellent catalyst for N-acetyl glucosamine (NAG) dehydration which mainly produced 3-acetamidofuran (3AF). Methods The physicochemical properties of the metal oxide catalyst were investigated by various techniques such as XRD, FTIR, MeOH-FTIR, TPD, SEM, $ N_{2} $ sorption studies and HR-TEM analysis for structure activity relationship. Results The effect of various reaction parameters such as catalyst concentration, reaction temperature, reaction time and solvent effect on dehydration of N-acetyl glucosamine has been studied in detail for higher yields. The results revealed that the presence of weak basic sites which are Brønsted in nature and nano pores present on the surface were responsible for improved dehydration of the chitin biomass to selectively yield 3-acetamidofuran (3AF). $ La_{2} %$ O_{3} $ catalyst showed optimum 50% 3AF yield from N-acetyl glucosamine at 180 °C in 3 h. Conclusion Efficacious exploitation of marine biomass to value added chemicals using heterogeneous catalysts can be extensively exploited. Separation of N-substituted heterocyclic aromatics is the most innovative aspect of the current study. Thus, utilization of heterogeneous catalyst and renewable biomass as a raw material indicates a transition towards more sustainable and greener approach. Graphical Abstract With reference to valorization of biomass waste towards sustainability. We report for the first time heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) over $ La_{2} %$ O_{3} $ catalyst to yield 50% 3-acetamido furan (3AF) and 20% 3-acetamido-5-acetylfuran with 100% NAG conversion. The superior performance of $ La_{2} %$ O_{3} $ catalyst was attributed to the presence of brønsted basicity and nanopores present at catalysts surface. © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
abstractGer |
Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope for its exploration which may prove to be economically beneficial to the society. Heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) to N-substituted aromatic heterocyclic furan derivatives is reported for the very first time. Cost effective and stable metal oxide catalysts were deployed for the transformation. Catalyst screening study showed that $ La_{2} %$ O_{3} $ was found to be an excellent catalyst for N-acetyl glucosamine (NAG) dehydration which mainly produced 3-acetamidofuran (3AF). Methods The physicochemical properties of the metal oxide catalyst were investigated by various techniques such as XRD, FTIR, MeOH-FTIR, TPD, SEM, $ N_{2} $ sorption studies and HR-TEM analysis for structure activity relationship. Results The effect of various reaction parameters such as catalyst concentration, reaction temperature, reaction time and solvent effect on dehydration of N-acetyl glucosamine has been studied in detail for higher yields. The results revealed that the presence of weak basic sites which are Brønsted in nature and nano pores present on the surface were responsible for improved dehydration of the chitin biomass to selectively yield 3-acetamidofuran (3AF). $ La_{2} %$ O_{3} $ catalyst showed optimum 50% 3AF yield from N-acetyl glucosamine at 180 °C in 3 h. Conclusion Efficacious exploitation of marine biomass to value added chemicals using heterogeneous catalysts can be extensively exploited. Separation of N-substituted heterocyclic aromatics is the most innovative aspect of the current study. Thus, utilization of heterogeneous catalyst and renewable biomass as a raw material indicates a transition towards more sustainable and greener approach. Graphical Abstract With reference to valorization of biomass waste towards sustainability. We report for the first time heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) over $ La_{2} %$ O_{3} $ catalyst to yield 50% 3-acetamido furan (3AF) and 20% 3-acetamido-5-acetylfuran with 100% NAG conversion. The superior performance of $ La_{2} %$ O_{3} $ catalyst was attributed to the presence of brønsted basicity and nanopores present at catalysts surface. © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
abstract_unstemmed |
Purpose Effectual waste utilization from plant as well as marine biomass has gained tremendous importance with reference to sustainability. The valorization of marine biomass produces value added compounds containing not only C, H, O but also renewable N atom in the skeleton which widens the scope for its exploration which may prove to be economically beneficial to the society. Heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) to N-substituted aromatic heterocyclic furan derivatives is reported for the very first time. Cost effective and stable metal oxide catalysts were deployed for the transformation. Catalyst screening study showed that $ La_{2} %$ O_{3} $ was found to be an excellent catalyst for N-acetyl glucosamine (NAG) dehydration which mainly produced 3-acetamidofuran (3AF). Methods The physicochemical properties of the metal oxide catalyst were investigated by various techniques such as XRD, FTIR, MeOH-FTIR, TPD, SEM, $ N_{2} $ sorption studies and HR-TEM analysis for structure activity relationship. Results The effect of various reaction parameters such as catalyst concentration, reaction temperature, reaction time and solvent effect on dehydration of N-acetyl glucosamine has been studied in detail for higher yields. The results revealed that the presence of weak basic sites which are Brønsted in nature and nano pores present on the surface were responsible for improved dehydration of the chitin biomass to selectively yield 3-acetamidofuran (3AF). $ La_{2} %$ O_{3} $ catalyst showed optimum 50% 3AF yield from N-acetyl glucosamine at 180 °C in 3 h. Conclusion Efficacious exploitation of marine biomass to value added chemicals using heterogeneous catalysts can be extensively exploited. Separation of N-substituted heterocyclic aromatics is the most innovative aspect of the current study. Thus, utilization of heterogeneous catalyst and renewable biomass as a raw material indicates a transition towards more sustainable and greener approach. Graphical Abstract With reference to valorization of biomass waste towards sustainability. We report for the first time heterogeneous catalytic transformation of marine biomass i.e. N-acetyl glucosamine (NAG) over $ La_{2} %$ O_{3} $ catalyst to yield 50% 3-acetamido furan (3AF) and 20% 3-acetamido-5-acetylfuran with 100% NAG conversion. The superior performance of $ La_{2} %$ O_{3} $ catalyst was attributed to the presence of brønsted basicity and nanopores present at catalysts surface. © The Author(s), under exclusive licence to Springer Nature B.V. 2023. Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
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Direct Conversion of N-acetyl-d-glucosamine to N-containing Heterocyclic Compounds 3-Acetamidofuran and 3-Acetamido-5-acetyl Furan |
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score |
7.3990107 |