1955
DOI: 10.1021/ja01612a089
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The Sodium-Sodium Hydride-Hydrogen System at 500-600°1

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Cited by 47 publications
(23 citation statements)
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“…Fortuitously, sodium hydride has a large number of attributes that make it attractive as a hightemperature TES system for CSP. It has a respectable theoretical hydrogen storage capacity (4.2 wt% H 2 ), a high enthalpy of H 2 absorption (DH abs = -114 kJ mol -1 H 2 ) [41] and, from pressurecomposition isotherms, a wide and flat plateau with limited H 2 solubility [42]. In addition, a significant level of research into the sodium-hydrogen system has been driven by the use of liquid sodium as a coolant in liquidmetal fast-breeder reactors and, as a result, a large body of knowledge exists pertaining to the safe production, handling, containment and use of high-temperature sodium on an industrial scale [43].…”
Section: History Of Sodium and Sodium Hydridementioning
confidence: 99%
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“…Fortuitously, sodium hydride has a large number of attributes that make it attractive as a hightemperature TES system for CSP. It has a respectable theoretical hydrogen storage capacity (4.2 wt% H 2 ), a high enthalpy of H 2 absorption (DH abs = -114 kJ mol -1 H 2 ) [41] and, from pressurecomposition isotherms, a wide and flat plateau with limited H 2 solubility [42]. In addition, a significant level of research into the sodium-hydrogen system has been driven by the use of liquid sodium as a coolant in liquidmetal fast-breeder reactors and, as a result, a large body of knowledge exists pertaining to the safe production, handling, containment and use of high-temperature sodium on an industrial scale [43].…”
Section: History Of Sodium and Sodium Hydridementioning
confidence: 99%
“…Again, this technique is unsuitable when considering Na/NaH as part of a TES system that operates above 400°C due to the temperature limitations of hydrocarbons [32]. A further complication of Category II SBHs is the high vapour pressure of molten sodium metal that causes its distillation at the temperatures relevant for TES [41,42]. This problem was solved by sealing NaH within thin walled iron tubes that are permeable to H 2 but not to sodium vapour [7,41,42].…”
Section: History Of Sodium and Sodium Hydridementioning
confidence: 99%
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“…Measurements of the heat capacity of silicon have been reported by Russell [ 37 ] (-191°to 46°C) , Dewar [9] (20°to 80°K) , Nernst and Schwers [33] Kelley and King [20], using the data reported by Anderson [l], Nernst and Schwers [33], and Pearlman and Keesom [34] > calculated SRgg = 4*51 ±0.05 eu. Flubacher, Leadbetter, and Morrison [12] calculated 0°^,^= 4*497 ±0.009 eu from their data.…”
Section: Beryllium-titanium Systemmentioning
confidence: 99%
“…The decomposition pressure data of Banus, et al [37] a Sellers and Crenshaw [38], combined with appropriate entropy data, yi AHf = -12.5 and -12.6 kcal, respectively.…”
Section: Nah(c)mentioning
confidence: 99%