Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid
Monosilane ($ SiH_{4} $) is a common precursor for the production of high-purity silicon for solar PV applications. As an alternative to carbothermic reduction of silica to produce metallurgical grade silicon with subsequent conversion to silane, an alternative route over magnesiothermic reduction o...
Ausführliche Beschreibung
Autor*in: |
Rasouli, Azam [verfasserIn] Kuhn, Raphael [verfasserIn] Lai, Samson Yuxiu [verfasserIn] Safarian, Jafar [verfasserIn] Tranell, Gabriella [verfasserIn] |
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E-Artikel |
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Sprache: |
Englisch |
Erschienen: |
2024 |
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Schlagwörter: |
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Anmerkung: |
© The Author(s) 2024 |
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Übergeordnetes Werk: |
Enthalten in: Journal of sustainable metallurgy - Springer International Publishing, 2015, 10(2024), 2 vom: 17. Apr., Seite 687-698 |
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Übergeordnetes Werk: |
volume:10 ; year:2024 ; number:2 ; day:17 ; month:04 ; pages:687-698 |
Links: |
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DOI / URN: |
10.1007/s40831-024-00817-2 |
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Katalog-ID: |
SPR056162022 |
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520 | |a Monosilane ($ SiH_{4} $) is a common precursor for the production of high-purity silicon for solar PV applications. As an alternative to carbothermic reduction of silica to produce metallurgical grade silicon with subsequent conversion to silane, an alternative route over magnesiothermic reduction of silica to $ Mg_{2} $Si has been explored in our earlier work. In the current work, silane gas production through hydrolysis of $ Mg_{2} $Si in HCl acid solution was studied. Two sources of $ Mg_{2} $Si were chosen: a commercial $ Mg_{2} $Si source and a $ Mg_{2} $Si source produced through magnesiothermic reduction of high-purity natural quartz. Effects of various parameters on the hydrolysis of $ Mg_{2} $Si, including different experimental setups, temperature of the acid solution, acid concentration, reaction time, and relative amounts of reactants were studied. The evolution of produced gases was determined by two different methods: firstly, by passing the produced gas through a KOH solution to capture Si with subsequent analysis of the Si content in the KOH solution by inductively coupled plasma mass spectrometry and secondly, on-line gas analysis by GC–MS. The silane distribution between different silane species with reaction time was evaluated and the activation energy of silane formation was calculated. The results indicated comparable silane yields obtained from the on-line GC–MS method and KOH solution analysis method, as well as for commercial $ Mg_{2} $Si and the $ Mg_{2} $Si–MgO mixture produced through magnesiothermic reduction. Furthermore, adding HCl acid to $ Mg_{2} $Si in water led to higher $ SiH_{4} $ formation yield than adding $ Mg_{2} $Si to acid. However, the total silane yield for the two methods was similar at approximately 32%. Graphical Abstract | ||
650 | 4 | |a Silane formation |7 (dpeaa)DE-He213 | |
650 | 4 | |a Hydrolysis of Mg |7 (dpeaa)DE-He213 | |
650 | 4 | |a Si |7 (dpeaa)DE-He213 | |
650 | 4 | |a Silane yield |7 (dpeaa)DE-He213 | |
650 | 4 | |a Silane distribution |7 (dpeaa)DE-He213 | |
700 | 1 | |a Kuhn, Raphael |e verfasserin |4 aut | |
700 | 1 | |a Lai, Samson Yuxiu |e verfasserin |4 aut | |
700 | 1 | |a Safarian, Jafar |e verfasserin |4 aut | |
700 | 1 | |a Tranell, Gabriella |e verfasserin |4 aut | |
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10.1007/s40831-024-00817-2 doi (DE-627)SPR056162022 (SPR)s40831-024-00817-2-e DE-627 ger DE-627 rakwb eng 540 VZ 540 VZ Rasouli, Azam verfasserin (orcid)0000-0002-8520-3813 aut Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid 2024 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s) 2024 Monosilane ($ SiH_{4} $) is a common precursor for the production of high-purity silicon for solar PV applications. As an alternative to carbothermic reduction of silica to produce metallurgical grade silicon with subsequent conversion to silane, an alternative route over magnesiothermic reduction of silica to $ Mg_{2} $Si has been explored in our earlier work. In the current work, silane gas production through hydrolysis of $ Mg_{2} $Si in HCl acid solution was studied. Two sources of $ Mg_{2} $Si were chosen: a commercial $ Mg_{2} $Si source and a $ Mg_{2} $Si source produced through magnesiothermic reduction of high-purity natural quartz. Effects of various parameters on the hydrolysis of $ Mg_{2} $Si, including different experimental setups, temperature of the acid solution, acid concentration, reaction time, and relative amounts of reactants were studied. The evolution of produced gases was determined by two different methods: firstly, by passing the produced gas through a KOH solution to capture Si with subsequent analysis of the Si content in the KOH solution by inductively coupled plasma mass spectrometry and secondly, on-line gas analysis by GC–MS. The silane distribution between different silane species with reaction time was evaluated and the activation energy of silane formation was calculated. The results indicated comparable silane yields obtained from the on-line GC–MS method and KOH solution analysis method, as well as for commercial $ Mg_{2} $Si and the $ Mg_{2} $Si–MgO mixture produced through magnesiothermic reduction. Furthermore, adding HCl acid to $ Mg_{2} $Si in water led to higher $ SiH_{4} $ formation yield than adding $ Mg_{2} $Si to acid. However, the total silane yield for the two methods was similar at approximately 32%. Graphical Abstract Silane formation (dpeaa)DE-He213 Hydrolysis of Mg (dpeaa)DE-He213 Si (dpeaa)DE-He213 Silane yield (dpeaa)DE-He213 Silane distribution (dpeaa)DE-He213 Kuhn, Raphael verfasserin aut Lai, Samson Yuxiu verfasserin aut Safarian, Jafar verfasserin aut Tranell, Gabriella verfasserin aut Enthalten in Journal of sustainable metallurgy Springer International Publishing, 2015 10(2024), 2 vom: 17. Apr., Seite 687-698 (DE-627)817362541 (DE-600)2808817-7 2199-3831 nnns volume:10 year:2024 number:2 day:17 month:04 pages:687-698 https://dx.doi.org/10.1007/s40831-024-00817-2 X:SPRINGER Resolving-System kostenfrei Volltext SYSFLAG_0 GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_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_101 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_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_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 10 2024 2 17 04 687-698 |
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10.1007/s40831-024-00817-2 doi (DE-627)SPR056162022 (SPR)s40831-024-00817-2-e DE-627 ger DE-627 rakwb eng 540 VZ 540 VZ Rasouli, Azam verfasserin (orcid)0000-0002-8520-3813 aut Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid 2024 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s) 2024 Monosilane ($ SiH_{4} $) is a common precursor for the production of high-purity silicon for solar PV applications. As an alternative to carbothermic reduction of silica to produce metallurgical grade silicon with subsequent conversion to silane, an alternative route over magnesiothermic reduction of silica to $ Mg_{2} $Si has been explored in our earlier work. In the current work, silane gas production through hydrolysis of $ Mg_{2} $Si in HCl acid solution was studied. Two sources of $ Mg_{2} $Si were chosen: a commercial $ Mg_{2} $Si source and a $ Mg_{2} $Si source produced through magnesiothermic reduction of high-purity natural quartz. Effects of various parameters on the hydrolysis of $ Mg_{2} $Si, including different experimental setups, temperature of the acid solution, acid concentration, reaction time, and relative amounts of reactants were studied. The evolution of produced gases was determined by two different methods: firstly, by passing the produced gas through a KOH solution to capture Si with subsequent analysis of the Si content in the KOH solution by inductively coupled plasma mass spectrometry and secondly, on-line gas analysis by GC–MS. The silane distribution between different silane species with reaction time was evaluated and the activation energy of silane formation was calculated. The results indicated comparable silane yields obtained from the on-line GC–MS method and KOH solution analysis method, as well as for commercial $ Mg_{2} $Si and the $ Mg_{2} $Si–MgO mixture produced through magnesiothermic reduction. Furthermore, adding HCl acid to $ Mg_{2} $Si in water led to higher $ SiH_{4} $ formation yield than adding $ Mg_{2} $Si to acid. However, the total silane yield for the two methods was similar at approximately 32%. Graphical Abstract Silane formation (dpeaa)DE-He213 Hydrolysis of Mg (dpeaa)DE-He213 Si (dpeaa)DE-He213 Silane yield (dpeaa)DE-He213 Silane distribution (dpeaa)DE-He213 Kuhn, Raphael verfasserin aut Lai, Samson Yuxiu verfasserin aut Safarian, Jafar verfasserin aut Tranell, Gabriella verfasserin aut Enthalten in Journal of sustainable metallurgy Springer International Publishing, 2015 10(2024), 2 vom: 17. Apr., Seite 687-698 (DE-627)817362541 (DE-600)2808817-7 2199-3831 nnns volume:10 year:2024 number:2 day:17 month:04 pages:687-698 https://dx.doi.org/10.1007/s40831-024-00817-2 X:SPRINGER Resolving-System kostenfrei Volltext SYSFLAG_0 GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_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_101 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_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_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 10 2024 2 17 04 687-698 |
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10.1007/s40831-024-00817-2 doi (DE-627)SPR056162022 (SPR)s40831-024-00817-2-e DE-627 ger DE-627 rakwb eng 540 VZ 540 VZ Rasouli, Azam verfasserin (orcid)0000-0002-8520-3813 aut Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid 2024 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s) 2024 Monosilane ($ SiH_{4} $) is a common precursor for the production of high-purity silicon for solar PV applications. As an alternative to carbothermic reduction of silica to produce metallurgical grade silicon with subsequent conversion to silane, an alternative route over magnesiothermic reduction of silica to $ Mg_{2} $Si has been explored in our earlier work. In the current work, silane gas production through hydrolysis of $ Mg_{2} $Si in HCl acid solution was studied. Two sources of $ Mg_{2} $Si were chosen: a commercial $ Mg_{2} $Si source and a $ Mg_{2} $Si source produced through magnesiothermic reduction of high-purity natural quartz. Effects of various parameters on the hydrolysis of $ Mg_{2} $Si, including different experimental setups, temperature of the acid solution, acid concentration, reaction time, and relative amounts of reactants were studied. The evolution of produced gases was determined by two different methods: firstly, by passing the produced gas through a KOH solution to capture Si with subsequent analysis of the Si content in the KOH solution by inductively coupled plasma mass spectrometry and secondly, on-line gas analysis by GC–MS. The silane distribution between different silane species with reaction time was evaluated and the activation energy of silane formation was calculated. The results indicated comparable silane yields obtained from the on-line GC–MS method and KOH solution analysis method, as well as for commercial $ Mg_{2} $Si and the $ Mg_{2} $Si–MgO mixture produced through magnesiothermic reduction. Furthermore, adding HCl acid to $ Mg_{2} $Si in water led to higher $ SiH_{4} $ formation yield than adding $ Mg_{2} $Si to acid. However, the total silane yield for the two methods was similar at approximately 32%. Graphical Abstract Silane formation (dpeaa)DE-He213 Hydrolysis of Mg (dpeaa)DE-He213 Si (dpeaa)DE-He213 Silane yield (dpeaa)DE-He213 Silane distribution (dpeaa)DE-He213 Kuhn, Raphael verfasserin aut Lai, Samson Yuxiu verfasserin aut Safarian, Jafar verfasserin aut Tranell, Gabriella verfasserin aut Enthalten in Journal of sustainable metallurgy Springer International Publishing, 2015 10(2024), 2 vom: 17. Apr., Seite 687-698 (DE-627)817362541 (DE-600)2808817-7 2199-3831 nnns volume:10 year:2024 number:2 day:17 month:04 pages:687-698 https://dx.doi.org/10.1007/s40831-024-00817-2 X:SPRINGER Resolving-System kostenfrei Volltext SYSFLAG_0 GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_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_101 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_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_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 10 2024 2 17 04 687-698 |
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10.1007/s40831-024-00817-2 doi (DE-627)SPR056162022 (SPR)s40831-024-00817-2-e DE-627 ger DE-627 rakwb eng 540 VZ 540 VZ Rasouli, Azam verfasserin (orcid)0000-0002-8520-3813 aut Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid 2024 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s) 2024 Monosilane ($ SiH_{4} $) is a common precursor for the production of high-purity silicon for solar PV applications. As an alternative to carbothermic reduction of silica to produce metallurgical grade silicon with subsequent conversion to silane, an alternative route over magnesiothermic reduction of silica to $ Mg_{2} $Si has been explored in our earlier work. In the current work, silane gas production through hydrolysis of $ Mg_{2} $Si in HCl acid solution was studied. Two sources of $ Mg_{2} $Si were chosen: a commercial $ Mg_{2} $Si source and a $ Mg_{2} $Si source produced through magnesiothermic reduction of high-purity natural quartz. Effects of various parameters on the hydrolysis of $ Mg_{2} $Si, including different experimental setups, temperature of the acid solution, acid concentration, reaction time, and relative amounts of reactants were studied. The evolution of produced gases was determined by two different methods: firstly, by passing the produced gas through a KOH solution to capture Si with subsequent analysis of the Si content in the KOH solution by inductively coupled plasma mass spectrometry and secondly, on-line gas analysis by GC–MS. The silane distribution between different silane species with reaction time was evaluated and the activation energy of silane formation was calculated. The results indicated comparable silane yields obtained from the on-line GC–MS method and KOH solution analysis method, as well as for commercial $ Mg_{2} $Si and the $ Mg_{2} $Si–MgO mixture produced through magnesiothermic reduction. Furthermore, adding HCl acid to $ Mg_{2} $Si in water led to higher $ SiH_{4} $ formation yield than adding $ Mg_{2} $Si to acid. However, the total silane yield for the two methods was similar at approximately 32%. Graphical Abstract Silane formation (dpeaa)DE-He213 Hydrolysis of Mg (dpeaa)DE-He213 Si (dpeaa)DE-He213 Silane yield (dpeaa)DE-He213 Silane distribution (dpeaa)DE-He213 Kuhn, Raphael verfasserin aut Lai, Samson Yuxiu verfasserin aut Safarian, Jafar verfasserin aut Tranell, Gabriella verfasserin aut Enthalten in Journal of sustainable metallurgy Springer International Publishing, 2015 10(2024), 2 vom: 17. Apr., Seite 687-698 (DE-627)817362541 (DE-600)2808817-7 2199-3831 nnns volume:10 year:2024 number:2 day:17 month:04 pages:687-698 https://dx.doi.org/10.1007/s40831-024-00817-2 X:SPRINGER Resolving-System kostenfrei Volltext SYSFLAG_0 GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_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_101 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_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_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 10 2024 2 17 04 687-698 |
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10.1007/s40831-024-00817-2 doi (DE-627)SPR056162022 (SPR)s40831-024-00817-2-e DE-627 ger DE-627 rakwb eng 540 VZ 540 VZ Rasouli, Azam verfasserin (orcid)0000-0002-8520-3813 aut Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid 2024 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © The Author(s) 2024 Monosilane ($ SiH_{4} $) is a common precursor for the production of high-purity silicon for solar PV applications. As an alternative to carbothermic reduction of silica to produce metallurgical grade silicon with subsequent conversion to silane, an alternative route over magnesiothermic reduction of silica to $ Mg_{2} $Si has been explored in our earlier work. In the current work, silane gas production through hydrolysis of $ Mg_{2} $Si in HCl acid solution was studied. Two sources of $ Mg_{2} $Si were chosen: a commercial $ Mg_{2} $Si source and a $ Mg_{2} $Si source produced through magnesiothermic reduction of high-purity natural quartz. Effects of various parameters on the hydrolysis of $ Mg_{2} $Si, including different experimental setups, temperature of the acid solution, acid concentration, reaction time, and relative amounts of reactants were studied. The evolution of produced gases was determined by two different methods: firstly, by passing the produced gas through a KOH solution to capture Si with subsequent analysis of the Si content in the KOH solution by inductively coupled plasma mass spectrometry and secondly, on-line gas analysis by GC–MS. The silane distribution between different silane species with reaction time was evaluated and the activation energy of silane formation was calculated. The results indicated comparable silane yields obtained from the on-line GC–MS method and KOH solution analysis method, as well as for commercial $ Mg_{2} $Si and the $ Mg_{2} $Si–MgO mixture produced through magnesiothermic reduction. Furthermore, adding HCl acid to $ Mg_{2} $Si in water led to higher $ SiH_{4} $ formation yield than adding $ Mg_{2} $Si to acid. However, the total silane yield for the two methods was similar at approximately 32%. Graphical Abstract Silane formation (dpeaa)DE-He213 Hydrolysis of Mg (dpeaa)DE-He213 Si (dpeaa)DE-He213 Silane yield (dpeaa)DE-He213 Silane distribution (dpeaa)DE-He213 Kuhn, Raphael verfasserin aut Lai, Samson Yuxiu verfasserin aut Safarian, Jafar verfasserin aut Tranell, Gabriella verfasserin aut Enthalten in Journal of sustainable metallurgy Springer International Publishing, 2015 10(2024), 2 vom: 17. Apr., Seite 687-698 (DE-627)817362541 (DE-600)2808817-7 2199-3831 nnns volume:10 year:2024 number:2 day:17 month:04 pages:687-698 https://dx.doi.org/10.1007/s40831-024-00817-2 X:SPRINGER Resolving-System kostenfrei Volltext SYSFLAG_0 GBV_SPRINGER SSG-OLC-PHA GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_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_101 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_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_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 10 2024 2 17 04 687-698 |
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Enthalten in Journal of sustainable metallurgy 10(2024), 2 vom: 17. Apr., Seite 687-698 volume:10 year:2024 number:2 day:17 month:04 pages:687-698 |
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Enthalten in Journal of sustainable metallurgy 10(2024), 2 vom: 17. Apr., Seite 687-698 volume:10 year:2024 number:2 day:17 month:04 pages:687-698 |
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Silane formation Hydrolysis of Mg Si Silane yield Silane distribution |
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Journal of sustainable metallurgy |
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Rasouli, Azam @@aut@@ Kuhn, Raphael @@aut@@ Lai, Samson Yuxiu @@aut@@ Safarian, Jafar @@aut@@ Tranell, Gabriella @@aut@@ |
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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">SPR056162022</controlfield><controlfield tag="003">DE-627</controlfield><controlfield tag="005">20240608064718.0</controlfield><controlfield tag="007">cr uuu---uuuuu</controlfield><controlfield tag="008">240608s2024 xx |||||o 00| ||eng c</controlfield><datafield tag="024" ind1="7" ind2=" "><subfield code="a">10.1007/s40831-024-00817-2</subfield><subfield code="2">doi</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(DE-627)SPR056162022</subfield></datafield><datafield tag="035" ind1=" " ind2=" "><subfield code="a">(SPR)s40831-024-00817-2-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="082" ind1="0" ind2="4"><subfield code="a">540</subfield><subfield code="q">VZ</subfield></datafield><datafield tag="082" ind1="0" ind2="4"><subfield code="a">540</subfield><subfield code="q">VZ</subfield></datafield><datafield tag="100" ind1="1" ind2=" "><subfield code="a">Rasouli, Azam</subfield><subfield code="e">verfasserin</subfield><subfield code="0">(orcid)0000-0002-8520-3813</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="0"><subfield code="a">Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2024</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) 2024</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Monosilane ($ SiH_{4} $) is a common precursor for the production of high-purity silicon for solar PV applications. As an alternative to carbothermic reduction of silica to produce metallurgical grade silicon with subsequent conversion to silane, an alternative route over magnesiothermic reduction of silica to $ Mg_{2} $Si has been explored in our earlier work. In the current work, silane gas production through hydrolysis of $ Mg_{2} $Si in HCl acid solution was studied. Two sources of $ Mg_{2} $Si were chosen: a commercial $ Mg_{2} $Si source and a $ Mg_{2} $Si source produced through magnesiothermic reduction of high-purity natural quartz. Effects of various parameters on the hydrolysis of $ Mg_{2} $Si, including different experimental setups, temperature of the acid solution, acid concentration, reaction time, and relative amounts of reactants were studied. The evolution of produced gases was determined by two different methods: firstly, by passing the produced gas through a KOH solution to capture Si with subsequent analysis of the Si content in the KOH solution by inductively coupled plasma mass spectrometry and secondly, on-line gas analysis by GC–MS. The silane distribution between different silane species with reaction time was evaluated and the activation energy of silane formation was calculated. The results indicated comparable silane yields obtained from the on-line GC–MS method and KOH solution analysis method, as well as for commercial $ Mg_{2} $Si and the $ Mg_{2} $Si–MgO mixture produced through magnesiothermic reduction. Furthermore, adding HCl acid to $ Mg_{2} $Si in water led to higher $ SiH_{4} $ formation yield than adding $ Mg_{2} $Si to acid. However, the total silane yield for the two methods was similar at approximately 32%. 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|
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Rasouli, Azam |
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Rasouli, Azam ddc 540 misc Silane formation misc Hydrolysis of Mg misc Si misc Silane yield misc Silane distribution Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid |
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540 VZ Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid Silane formation (dpeaa)DE-He213 Hydrolysis of Mg (dpeaa)DE-He213 Si (dpeaa)DE-He213 Silane yield (dpeaa)DE-He213 Silane distribution (dpeaa)DE-He213 |
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ddc 540 misc Silane formation misc Hydrolysis of Mg misc Si misc Silane yield misc Silane distribution |
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ddc 540 misc Silane formation misc Hydrolysis of Mg misc Si misc Silane yield misc Silane distribution |
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ddc 540 misc Silane formation misc Hydrolysis of Mg misc Si misc Silane yield misc Silane distribution |
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Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid |
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Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid |
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Rasouli, Azam |
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Journal of sustainable metallurgy |
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Rasouli, Azam Kuhn, Raphael Lai, Samson Yuxiu Safarian, Jafar Tranell, Gabriella |
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Elektronische Aufsätze |
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silane gas production through hydrolysis of magnesium silicide by hydrochloric acid |
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Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid |
abstract |
Monosilane ($ SiH_{4} $) is a common precursor for the production of high-purity silicon for solar PV applications. As an alternative to carbothermic reduction of silica to produce metallurgical grade silicon with subsequent conversion to silane, an alternative route over magnesiothermic reduction of silica to $ Mg_{2} $Si has been explored in our earlier work. In the current work, silane gas production through hydrolysis of $ Mg_{2} $Si in HCl acid solution was studied. Two sources of $ Mg_{2} $Si were chosen: a commercial $ Mg_{2} $Si source and a $ Mg_{2} $Si source produced through magnesiothermic reduction of high-purity natural quartz. Effects of various parameters on the hydrolysis of $ Mg_{2} $Si, including different experimental setups, temperature of the acid solution, acid concentration, reaction time, and relative amounts of reactants were studied. The evolution of produced gases was determined by two different methods: firstly, by passing the produced gas through a KOH solution to capture Si with subsequent analysis of the Si content in the KOH solution by inductively coupled plasma mass spectrometry and secondly, on-line gas analysis by GC–MS. The silane distribution between different silane species with reaction time was evaluated and the activation energy of silane formation was calculated. The results indicated comparable silane yields obtained from the on-line GC–MS method and KOH solution analysis method, as well as for commercial $ Mg_{2} $Si and the $ Mg_{2} $Si–MgO mixture produced through magnesiothermic reduction. Furthermore, adding HCl acid to $ Mg_{2} $Si in water led to higher $ SiH_{4} $ formation yield than adding $ Mg_{2} $Si to acid. However, the total silane yield for the two methods was similar at approximately 32%. Graphical Abstract © The Author(s) 2024 |
abstractGer |
Monosilane ($ SiH_{4} $) is a common precursor for the production of high-purity silicon for solar PV applications. As an alternative to carbothermic reduction of silica to produce metallurgical grade silicon with subsequent conversion to silane, an alternative route over magnesiothermic reduction of silica to $ Mg_{2} $Si has been explored in our earlier work. In the current work, silane gas production through hydrolysis of $ Mg_{2} $Si in HCl acid solution was studied. Two sources of $ Mg_{2} $Si were chosen: a commercial $ Mg_{2} $Si source and a $ Mg_{2} $Si source produced through magnesiothermic reduction of high-purity natural quartz. Effects of various parameters on the hydrolysis of $ Mg_{2} $Si, including different experimental setups, temperature of the acid solution, acid concentration, reaction time, and relative amounts of reactants were studied. The evolution of produced gases was determined by two different methods: firstly, by passing the produced gas through a KOH solution to capture Si with subsequent analysis of the Si content in the KOH solution by inductively coupled plasma mass spectrometry and secondly, on-line gas analysis by GC–MS. The silane distribution between different silane species with reaction time was evaluated and the activation energy of silane formation was calculated. The results indicated comparable silane yields obtained from the on-line GC–MS method and KOH solution analysis method, as well as for commercial $ Mg_{2} $Si and the $ Mg_{2} $Si–MgO mixture produced through magnesiothermic reduction. Furthermore, adding HCl acid to $ Mg_{2} $Si in water led to higher $ SiH_{4} $ formation yield than adding $ Mg_{2} $Si to acid. However, the total silane yield for the two methods was similar at approximately 32%. Graphical Abstract © The Author(s) 2024 |
abstract_unstemmed |
Monosilane ($ SiH_{4} $) is a common precursor for the production of high-purity silicon for solar PV applications. As an alternative to carbothermic reduction of silica to produce metallurgical grade silicon with subsequent conversion to silane, an alternative route over magnesiothermic reduction of silica to $ Mg_{2} $Si has been explored in our earlier work. In the current work, silane gas production through hydrolysis of $ Mg_{2} $Si in HCl acid solution was studied. Two sources of $ Mg_{2} $Si were chosen: a commercial $ Mg_{2} $Si source and a $ Mg_{2} $Si source produced through magnesiothermic reduction of high-purity natural quartz. Effects of various parameters on the hydrolysis of $ Mg_{2} $Si, including different experimental setups, temperature of the acid solution, acid concentration, reaction time, and relative amounts of reactants were studied. The evolution of produced gases was determined by two different methods: firstly, by passing the produced gas through a KOH solution to capture Si with subsequent analysis of the Si content in the KOH solution by inductively coupled plasma mass spectrometry and secondly, on-line gas analysis by GC–MS. The silane distribution between different silane species with reaction time was evaluated and the activation energy of silane formation was calculated. The results indicated comparable silane yields obtained from the on-line GC–MS method and KOH solution analysis method, as well as for commercial $ Mg_{2} $Si and the $ Mg_{2} $Si–MgO mixture produced through magnesiothermic reduction. Furthermore, adding HCl acid to $ Mg_{2} $Si in water led to higher $ SiH_{4} $ formation yield than adding $ Mg_{2} $Si to acid. However, the total silane yield for the two methods was similar at approximately 32%. Graphical Abstract © The Author(s) 2024 |
collection_details |
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container_issue |
2 |
title_short |
Silane Gas Production Through Hydrolysis of Magnesium Silicide by Hydrochloric Acid |
url |
https://dx.doi.org/10.1007/s40831-024-00817-2 |
remote_bool |
true |
author2 |
Kuhn, Raphael Lai, Samson Yuxiu Safarian, Jafar Tranell, Gabriella |
author2Str |
Kuhn, Raphael Lai, Samson Yuxiu Safarian, Jafar Tranell, Gabriella |
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817362541 |
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hochschulschrift_bool |
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doi_str |
10.1007/s40831-024-00817-2 |
up_date |
2024-07-03T20:36:46.334Z |
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score |
7.402276 |