2004
DOI: 10.1016/s0378-7753(03)00822-x
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Heat transfer characteristics of the metal hydride vessel based on the plate-fin type heat exchanger

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Cited by 67 publications
(26 citation statements)
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“…Therefore, internal heat transfer enhancements have become more attractive and can roughly divided in two ways: 1) Enhancement of the thermal conductivity of the metal hydride powder by insertion of aluminium foam [13][14][15], copper wire net structure [16] or by creating metal hydride compacts [17][18][19][20], 2) Integration of heat exchangers inside the bed such as embedded heat exchanger tubes [21][22][23], finned tube heat exchangers [24][25][26][27], spiral heat exchangers [28,29] or heat pipes [30].…”
Section: Introductionmentioning
confidence: 99%
“…Therefore, internal heat transfer enhancements have become more attractive and can roughly divided in two ways: 1) Enhancement of the thermal conductivity of the metal hydride powder by insertion of aluminium foam [13][14][15], copper wire net structure [16] or by creating metal hydride compacts [17][18][19][20], 2) Integration of heat exchangers inside the bed such as embedded heat exchanger tubes [21][22][23], finned tube heat exchangers [24][25][26][27], spiral heat exchangers [28,29] or heat pipes [30].…”
Section: Introductionmentioning
confidence: 99%
“…Coolant channels or heat transfer fins have been considered because they increase the heat transfer area without creating the aforementioned issues. Transverse or longitudinal cooling fins were used in tubular and box-shaped reactors [10,[23][24][25]. A plate-fin type heat exchanger in a rectangular reactor has been experimentally tested [23].…”
Section: Introductionmentioning
confidence: 99%
“…Transverse or longitudinal cooling fins were used in tubular and box-shaped reactors [10,[23][24][25]. A plate-fin type heat exchanger in a rectangular reactor has been experimentally tested [23]. For a tubular reactor, three designs (coolant channels with fins, helical coils, and shell-and-tube) have been optimized and compared [24].…”
Section: Introductionmentioning
confidence: 99%
“…control volume c p heat capacity, J kg À1 K À1 C sg hydride capacity, kg H 2 /kg hydride, e b C volumetric hydrogen storage capacity, kg H2 m À3 d average hydride particle size, m DH mass enthalpy of reaction, J kg À1 DH n molar enthalpy of reaction, J mol À1 DS n molar entropy of reaction, J mol À1 K À1 e total energy of control surface/volume, J kg À1 E Abs activation energy, J mol À1 E rea enthalpy of reaction per unit volume, J m À3 ε hydride porosity, e f FC constant proportional to fill criteria, e F heat conductive material fraction, e F volumetric flow, m 3 [41,42] [43e45] [46]*, [47] *Propose some sort of optimization.…”
Section: Introductionmentioning
confidence: 99%