2015
DOI: 10.1016/j.jallcom.2014.12.272
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Performance analysis of cylindrical metal hydride beds with various heat exchange options

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Cited by 61 publications
(18 citation statements)
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“…Modelling of heat transfer performance of MH beds on the basis of the AB 5 -type alloys showed that externally heated and cooled cylindrical beds with a high length-to-diameter ratio is an optimal solution due to (i) high heat exchange area between the MH and the heating/cooling fluid, (ii) simplicity and lower cost and (iii) less pronounced reduction of hydrogen storage capacity at the same dimensions as compared to the solutions with internal heat exchangers [21]. According to the modelling results verified by experiments [22], the externally heated and cooled cylindrical stainless steel containers, about 20 mm in the internal diameter and about 800 mm in the length, filled by the selected AB 5 -type materials, are characterised by satisfactory H 2 absorption/desorption (H 2 charge/discharge times shorter than 20 min), if averaged heat transfer coefficient between the MH container walls and the heating/cooling fluid is about 500 W m −2 K and higher.…”
Section: Metal Hydride Bed and Hydrogen Compression Modulementioning
confidence: 99%
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“…Modelling of heat transfer performance of MH beds on the basis of the AB 5 -type alloys showed that externally heated and cooled cylindrical beds with a high length-to-diameter ratio is an optimal solution due to (i) high heat exchange area between the MH and the heating/cooling fluid, (ii) simplicity and lower cost and (iii) less pronounced reduction of hydrogen storage capacity at the same dimensions as compared to the solutions with internal heat exchangers [21]. According to the modelling results verified by experiments [22], the externally heated and cooled cylindrical stainless steel containers, about 20 mm in the internal diameter and about 800 mm in the length, filled by the selected AB 5 -type materials, are characterised by satisfactory H 2 absorption/desorption (H 2 charge/discharge times shorter than 20 min), if averaged heat transfer coefficient between the MH container walls and the heating/cooling fluid is about 500 W m −2 K and higher.…”
Section: Metal Hydride Bed and Hydrogen Compression Modulementioning
confidence: 99%
“…This work summarises the results of joint development, by SKTBE and IPCP, and long-term operation of two models of two-stage metal hydride hydrogen compressors, TSC1-3.5/150 and TSC2-3.5/150. Further details have been published in [16][17][18][19][20][21][22].…”
Section: Introductionmentioning
confidence: 99%
“…Whereas, increasing effective thermal conductivity of MH facilitated substantial reduction in the absorption and desorption times. Satya Sekhar et al 37 numerically examined the performance of different heat exchanger options for a cylindrical metal hydride container filled with MmNi 4.6 Al 0.4 . Four different cooling arrangements were considered, namely internal straight tube, internal helical, external cooling channel and external cooling channel with internal transverse fins.…”
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%
“…For a tubular reactor, three designs (coolant channels with fins, helical coils, and shell-and-tube) have been optimized and compared [24]. Another study compared a straight channel with a helical coil for internal cooling and also investigated cooling performance improvements by the addition of external transversal fins [25]. A systematic optimization routine for internal fin design was performed to determine geometrical parameters [10].…”
Section: Introductionmentioning
confidence: 99%