Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar
A novel technology termed as ‘grinding pyrolysis’ has been developed in response to the limitations hindering the commercialisation of existing fast pyrolysis technologies. Some of the features of this novel technology include capability of feeding biomass having a wide range of particle sizes in th...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Hasan, MD Mahmudul [verfasserIn] Wang, Xiao Shan [verfasserIn] Mourant, Daniel [verfasserIn] Gunawan, Richard [verfasserIn] Yu, Chunlong [verfasserIn] Hu, Xun [verfasserIn] Kadarwati, Sri [verfasserIn] Gholizadeh, Mortaza [verfasserIn] Wu, Hongwei [verfasserIn] Li, Bin [verfasserIn] Zhang, Lei [verfasserIn] Li, Chun-Zhu [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2017 |
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| Schlagwörter: |
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| Übergeordnetes Werk: |
Enthalten in: Fuel processing technology - New York, NY [u.a.] : Science Direct, 1977, 167, Seite 215-220 |
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| Übergeordnetes Werk: |
volume:167 ; pages:215-220 |
| DOI / URN: |
10.1016/j.fuproc.2017.07.004 |
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| Katalog-ID: |
ELV000446157 |
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| 520 | |a A novel technology termed as ‘grinding pyrolysis’ has been developed in response to the limitations hindering the commercialisation of existing fast pyrolysis technologies. Some of the features of this novel technology include capability of feeding biomass having a wide range of particle sizes in the same feedstock, simultaneous pyrolysis and grinding, no requirement for a fluidising gas and simplified requirement for cooling and condensing the pyrolysis products. A pilot plant was developed to study the effects of various operating conditions on the yields of bio-oil and biochar. Experiments have been done using mallee biomass grown in Western Australia. Feed particle sizes of up to a few centimetres have been used successfully. It was proved that the simultaneous grinding and pyrolysis helps liberating volatiles from a pyrolysing biomass particle and is capable of producing higher organic yields than pyrolysis without grinding. The effective size of a pyrolysing particle was significantly decreased by the simultaneous grinding activity. | ||
| 650 | 4 | |a Grinding pyrolysis | |
| 650 | 4 | |a Mallee wood | |
| 650 | 4 | |a Feeding rate | |
| 650 | 4 | |a Pyrolysis temperature | |
| 650 | 4 | |a Speed of rotation | |
| 700 | 1 | |a Wang, Xiao Shan |e verfasserin |4 aut | |
| 700 | 1 | |a Mourant, Daniel |e verfasserin |4 aut | |
| 700 | 1 | |a Gunawan, Richard |e verfasserin |4 aut | |
| 700 | 1 | |a Yu, Chunlong |e verfasserin |0 (orcid)0000-0002-6325-6973 |4 aut | |
| 700 | 1 | |a Hu, Xun |e verfasserin |4 aut | |
| 700 | 1 | |a Kadarwati, Sri |e verfasserin |4 aut | |
| 700 | 1 | |a Gholizadeh, Mortaza |e verfasserin |4 aut | |
| 700 | 1 | |a Wu, Hongwei |e verfasserin |4 aut | |
| 700 | 1 | |a Li, Bin |e verfasserin |4 aut | |
| 700 | 1 | |a Zhang, Lei |e verfasserin |4 aut | |
| 700 | 1 | |a Li, Chun-Zhu |e verfasserin |4 aut | |
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10.1016/j.fuproc.2017.07.004 doi (DE-627)ELV000446157 (ELSEVIER)S0378-3820(17)30788-9 DE-627 ger DE-627 rda eng 660 DE-600 58.21 bkl Hasan, MD Mahmudul verfasserin aut Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar 2017 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier A novel technology termed as ‘grinding pyrolysis’ has been developed in response to the limitations hindering the commercialisation of existing fast pyrolysis technologies. Some of the features of this novel technology include capability of feeding biomass having a wide range of particle sizes in the same feedstock, simultaneous pyrolysis and grinding, no requirement for a fluidising gas and simplified requirement for cooling and condensing the pyrolysis products. A pilot plant was developed to study the effects of various operating conditions on the yields of bio-oil and biochar. Experiments have been done using mallee biomass grown in Western Australia. Feed particle sizes of up to a few centimetres have been used successfully. It was proved that the simultaneous grinding and pyrolysis helps liberating volatiles from a pyrolysing biomass particle and is capable of producing higher organic yields than pyrolysis without grinding. The effective size of a pyrolysing particle was significantly decreased by the simultaneous grinding activity. Grinding pyrolysis Mallee wood Feeding rate Pyrolysis temperature Speed of rotation Wang, Xiao Shan verfasserin aut Mourant, Daniel verfasserin aut Gunawan, Richard verfasserin aut Yu, Chunlong verfasserin (orcid)0000-0002-6325-6973 aut Hu, Xun verfasserin aut Kadarwati, Sri verfasserin aut Gholizadeh, Mortaza verfasserin aut Wu, Hongwei verfasserin aut Li, Bin verfasserin aut Zhang, Lei verfasserin aut Li, Chun-Zhu verfasserin aut Enthalten in Fuel processing technology New York, NY [u.a.] : Science Direct, 1977 167, Seite 215-220 Online-Ressource (DE-627)300898681 (DE-600)1483666-X (DE-576)09618860X nnns volume:167 pages:215-220 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_150 GBV_ILN_151 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_370 GBV_ILN_602 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_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2098 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 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_2470 GBV_ILN_2507 GBV_ILN_2522 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_4338 GBV_ILN_4393 GBV_ILN_4700 58.21 Brennstoffe Kraftstoffe Explosivstoffe AR 167 215-220 |
| spelling |
10.1016/j.fuproc.2017.07.004 doi (DE-627)ELV000446157 (ELSEVIER)S0378-3820(17)30788-9 DE-627 ger DE-627 rda eng 660 DE-600 58.21 bkl Hasan, MD Mahmudul verfasserin aut Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar 2017 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier A novel technology termed as ‘grinding pyrolysis’ has been developed in response to the limitations hindering the commercialisation of existing fast pyrolysis technologies. Some of the features of this novel technology include capability of feeding biomass having a wide range of particle sizes in the same feedstock, simultaneous pyrolysis and grinding, no requirement for a fluidising gas and simplified requirement for cooling and condensing the pyrolysis products. A pilot plant was developed to study the effects of various operating conditions on the yields of bio-oil and biochar. Experiments have been done using mallee biomass grown in Western Australia. Feed particle sizes of up to a few centimetres have been used successfully. It was proved that the simultaneous grinding and pyrolysis helps liberating volatiles from a pyrolysing biomass particle and is capable of producing higher organic yields than pyrolysis without grinding. The effective size of a pyrolysing particle was significantly decreased by the simultaneous grinding activity. Grinding pyrolysis Mallee wood Feeding rate Pyrolysis temperature Speed of rotation Wang, Xiao Shan verfasserin aut Mourant, Daniel verfasserin aut Gunawan, Richard verfasserin aut Yu, Chunlong verfasserin (orcid)0000-0002-6325-6973 aut Hu, Xun verfasserin aut Kadarwati, Sri verfasserin aut Gholizadeh, Mortaza verfasserin aut Wu, Hongwei verfasserin aut Li, Bin verfasserin aut Zhang, Lei verfasserin aut Li, Chun-Zhu verfasserin aut Enthalten in Fuel processing technology New York, NY [u.a.] : Science Direct, 1977 167, Seite 215-220 Online-Ressource (DE-627)300898681 (DE-600)1483666-X (DE-576)09618860X nnns volume:167 pages:215-220 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_150 GBV_ILN_151 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_370 GBV_ILN_602 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_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2098 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 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_2470 GBV_ILN_2507 GBV_ILN_2522 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_4338 GBV_ILN_4393 GBV_ILN_4700 58.21 Brennstoffe Kraftstoffe Explosivstoffe AR 167 215-220 |
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10.1016/j.fuproc.2017.07.004 doi (DE-627)ELV000446157 (ELSEVIER)S0378-3820(17)30788-9 DE-627 ger DE-627 rda eng 660 DE-600 58.21 bkl Hasan, MD Mahmudul verfasserin aut Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar 2017 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier A novel technology termed as ‘grinding pyrolysis’ has been developed in response to the limitations hindering the commercialisation of existing fast pyrolysis technologies. Some of the features of this novel technology include capability of feeding biomass having a wide range of particle sizes in the same feedstock, simultaneous pyrolysis and grinding, no requirement for a fluidising gas and simplified requirement for cooling and condensing the pyrolysis products. A pilot plant was developed to study the effects of various operating conditions on the yields of bio-oil and biochar. Experiments have been done using mallee biomass grown in Western Australia. Feed particle sizes of up to a few centimetres have been used successfully. It was proved that the simultaneous grinding and pyrolysis helps liberating volatiles from a pyrolysing biomass particle and is capable of producing higher organic yields than pyrolysis without grinding. The effective size of a pyrolysing particle was significantly decreased by the simultaneous grinding activity. Grinding pyrolysis Mallee wood Feeding rate Pyrolysis temperature Speed of rotation Wang, Xiao Shan verfasserin aut Mourant, Daniel verfasserin aut Gunawan, Richard verfasserin aut Yu, Chunlong verfasserin (orcid)0000-0002-6325-6973 aut Hu, Xun verfasserin aut Kadarwati, Sri verfasserin aut Gholizadeh, Mortaza verfasserin aut Wu, Hongwei verfasserin aut Li, Bin verfasserin aut Zhang, Lei verfasserin aut Li, Chun-Zhu verfasserin aut Enthalten in Fuel processing technology New York, NY [u.a.] : Science Direct, 1977 167, Seite 215-220 Online-Ressource (DE-627)300898681 (DE-600)1483666-X (DE-576)09618860X nnns volume:167 pages:215-220 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_150 GBV_ILN_151 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_370 GBV_ILN_602 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_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2098 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 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_2470 GBV_ILN_2507 GBV_ILN_2522 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_4338 GBV_ILN_4393 GBV_ILN_4700 58.21 Brennstoffe Kraftstoffe Explosivstoffe AR 167 215-220 |
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10.1016/j.fuproc.2017.07.004 doi (DE-627)ELV000446157 (ELSEVIER)S0378-3820(17)30788-9 DE-627 ger DE-627 rda eng 660 DE-600 58.21 bkl Hasan, MD Mahmudul verfasserin aut Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar 2017 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier A novel technology termed as ‘grinding pyrolysis’ has been developed in response to the limitations hindering the commercialisation of existing fast pyrolysis technologies. Some of the features of this novel technology include capability of feeding biomass having a wide range of particle sizes in the same feedstock, simultaneous pyrolysis and grinding, no requirement for a fluidising gas and simplified requirement for cooling and condensing the pyrolysis products. A pilot plant was developed to study the effects of various operating conditions on the yields of bio-oil and biochar. Experiments have been done using mallee biomass grown in Western Australia. Feed particle sizes of up to a few centimetres have been used successfully. It was proved that the simultaneous grinding and pyrolysis helps liberating volatiles from a pyrolysing biomass particle and is capable of producing higher organic yields than pyrolysis without grinding. The effective size of a pyrolysing particle was significantly decreased by the simultaneous grinding activity. Grinding pyrolysis Mallee wood Feeding rate Pyrolysis temperature Speed of rotation Wang, Xiao Shan verfasserin aut Mourant, Daniel verfasserin aut Gunawan, Richard verfasserin aut Yu, Chunlong verfasserin (orcid)0000-0002-6325-6973 aut Hu, Xun verfasserin aut Kadarwati, Sri verfasserin aut Gholizadeh, Mortaza verfasserin aut Wu, Hongwei verfasserin aut Li, Bin verfasserin aut Zhang, Lei verfasserin aut Li, Chun-Zhu verfasserin aut Enthalten in Fuel processing technology New York, NY [u.a.] : Science Direct, 1977 167, Seite 215-220 Online-Ressource (DE-627)300898681 (DE-600)1483666-X (DE-576)09618860X nnns volume:167 pages:215-220 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_150 GBV_ILN_151 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_370 GBV_ILN_602 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_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2098 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 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_2470 GBV_ILN_2507 GBV_ILN_2522 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_4338 GBV_ILN_4393 GBV_ILN_4700 58.21 Brennstoffe Kraftstoffe Explosivstoffe AR 167 215-220 |
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10.1016/j.fuproc.2017.07.004 doi (DE-627)ELV000446157 (ELSEVIER)S0378-3820(17)30788-9 DE-627 ger DE-627 rda eng 660 DE-600 58.21 bkl Hasan, MD Mahmudul verfasserin aut Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar 2017 nicht spezifiziert zzz rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier A novel technology termed as ‘grinding pyrolysis’ has been developed in response to the limitations hindering the commercialisation of existing fast pyrolysis technologies. Some of the features of this novel technology include capability of feeding biomass having a wide range of particle sizes in the same feedstock, simultaneous pyrolysis and grinding, no requirement for a fluidising gas and simplified requirement for cooling and condensing the pyrolysis products. A pilot plant was developed to study the effects of various operating conditions on the yields of bio-oil and biochar. Experiments have been done using mallee biomass grown in Western Australia. Feed particle sizes of up to a few centimetres have been used successfully. It was proved that the simultaneous grinding and pyrolysis helps liberating volatiles from a pyrolysing biomass particle and is capable of producing higher organic yields than pyrolysis without grinding. The effective size of a pyrolysing particle was significantly decreased by the simultaneous grinding activity. Grinding pyrolysis Mallee wood Feeding rate Pyrolysis temperature Speed of rotation Wang, Xiao Shan verfasserin aut Mourant, Daniel verfasserin aut Gunawan, Richard verfasserin aut Yu, Chunlong verfasserin (orcid)0000-0002-6325-6973 aut Hu, Xun verfasserin aut Kadarwati, Sri verfasserin aut Gholizadeh, Mortaza verfasserin aut Wu, Hongwei verfasserin aut Li, Bin verfasserin aut Zhang, Lei verfasserin aut Li, Chun-Zhu verfasserin aut Enthalten in Fuel processing technology New York, NY [u.a.] : Science Direct, 1977 167, Seite 215-220 Online-Ressource (DE-627)300898681 (DE-600)1483666-X (DE-576)09618860X nnns volume:167 pages:215-220 GBV_USEFLAG_U SYSFLAG_U GBV_ELV SSG-OLC-PHA GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 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_150 GBV_ILN_151 GBV_ILN_187 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_370 GBV_ILN_602 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_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 GBV_ILN_2088 GBV_ILN_2098 GBV_ILN_2106 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2116 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_2470 GBV_ILN_2507 GBV_ILN_2522 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_4338 GBV_ILN_4393 GBV_ILN_4700 58.21 Brennstoffe Kraftstoffe Explosivstoffe AR 167 215-220 |
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Enthalten in Fuel processing technology 167, Seite 215-220 volume:167 pages:215-220 |
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Hasan, MD Mahmudul @@aut@@ Wang, Xiao Shan @@aut@@ Mourant, Daniel @@aut@@ Gunawan, Richard @@aut@@ Yu, Chunlong @@aut@@ Hu, Xun @@aut@@ Kadarwati, Sri @@aut@@ Gholizadeh, Mortaza @@aut@@ Wu, Hongwei @@aut@@ Li, Bin @@aut@@ Zhang, Lei @@aut@@ Li, Chun-Zhu @@aut@@ |
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| author |
Hasan, MD Mahmudul |
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Hasan, MD Mahmudul ddc 660 bkl 58.21 misc Grinding pyrolysis misc Mallee wood misc Feeding rate misc Pyrolysis temperature misc Speed of rotation Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar |
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660 DE-600 58.21 bkl Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar Grinding pyrolysis Mallee wood Feeding rate Pyrolysis temperature Speed of rotation |
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ddc 660 bkl 58.21 misc Grinding pyrolysis misc Mallee wood misc Feeding rate misc Pyrolysis temperature misc Speed of rotation |
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ddc 660 bkl 58.21 misc Grinding pyrolysis misc Mallee wood misc Feeding rate misc Pyrolysis temperature misc Speed of rotation |
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Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar |
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Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar |
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Hasan, MD Mahmudul |
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Hasan, MD Mahmudul Wang, Xiao Shan Mourant, Daniel Gunawan, Richard Yu, Chunlong Hu, Xun Kadarwati, Sri Gholizadeh, Mortaza Wu, Hongwei Li, Bin Zhang, Lei Li, Chun-Zhu |
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10.1016/j.fuproc.2017.07.004 |
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grinding pyrolysis of mallee wood: effects of pyrolysis conditions on the yields of bio-oil and biochar |
| title_auth |
Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar |
| abstract |
A novel technology termed as ‘grinding pyrolysis’ has been developed in response to the limitations hindering the commercialisation of existing fast pyrolysis technologies. Some of the features of this novel technology include capability of feeding biomass having a wide range of particle sizes in the same feedstock, simultaneous pyrolysis and grinding, no requirement for a fluidising gas and simplified requirement for cooling and condensing the pyrolysis products. A pilot plant was developed to study the effects of various operating conditions on the yields of bio-oil and biochar. Experiments have been done using mallee biomass grown in Western Australia. Feed particle sizes of up to a few centimetres have been used successfully. It was proved that the simultaneous grinding and pyrolysis helps liberating volatiles from a pyrolysing biomass particle and is capable of producing higher organic yields than pyrolysis without grinding. The effective size of a pyrolysing particle was significantly decreased by the simultaneous grinding activity. |
| abstractGer |
A novel technology termed as ‘grinding pyrolysis’ has been developed in response to the limitations hindering the commercialisation of existing fast pyrolysis technologies. Some of the features of this novel technology include capability of feeding biomass having a wide range of particle sizes in the same feedstock, simultaneous pyrolysis and grinding, no requirement for a fluidising gas and simplified requirement for cooling and condensing the pyrolysis products. A pilot plant was developed to study the effects of various operating conditions on the yields of bio-oil and biochar. Experiments have been done using mallee biomass grown in Western Australia. Feed particle sizes of up to a few centimetres have been used successfully. It was proved that the simultaneous grinding and pyrolysis helps liberating volatiles from a pyrolysing biomass particle and is capable of producing higher organic yields than pyrolysis without grinding. The effective size of a pyrolysing particle was significantly decreased by the simultaneous grinding activity. |
| abstract_unstemmed |
A novel technology termed as ‘grinding pyrolysis’ has been developed in response to the limitations hindering the commercialisation of existing fast pyrolysis technologies. Some of the features of this novel technology include capability of feeding biomass having a wide range of particle sizes in the same feedstock, simultaneous pyrolysis and grinding, no requirement for a fluidising gas and simplified requirement for cooling and condensing the pyrolysis products. A pilot plant was developed to study the effects of various operating conditions on the yields of bio-oil and biochar. Experiments have been done using mallee biomass grown in Western Australia. Feed particle sizes of up to a few centimetres have been used successfully. It was proved that the simultaneous grinding and pyrolysis helps liberating volatiles from a pyrolysing biomass particle and is capable of producing higher organic yields than pyrolysis without grinding. The effective size of a pyrolysing particle was significantly decreased by the simultaneous grinding activity. |
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Grinding pyrolysis of Mallee wood: Effects of pyrolysis conditions on the yields of bio-oil and biochar |
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Wang, Xiao Shan Mourant, Daniel Gunawan, Richard Yu, Chunlong Hu, Xun Kadarwati, Sri Gholizadeh, Mortaza Wu, Hongwei Li, Bin Zhang, Lei Li, Chun-Zhu |
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Wang, Xiao Shan Mourant, Daniel Gunawan, Richard Yu, Chunlong Hu, Xun Kadarwati, Sri Gholizadeh, Mortaza Wu, Hongwei Li, Bin Zhang, Lei Li, Chun-Zhu |
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2024-07-06T17:59:55.432Z |
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