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In this work bed height, bed size and fluidization conditions have been varied and a correlating equation: is suggested as applying over the range Comparison is made with mass transfer data of several other authors, revealing considerable variance.
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Some rooms have outsize, hip-height beds, which are (and I'm 5ft 11in) awkward to get into.
In this experiment, the height of bed is set to 750 mm, which is an average value of beds using in the actual home-visit bathing service.
Water and juice is on the table next to the height-adjustable bed.
The breakthrough point decreased with decrease in bed height, and increase in bed height increased the breakthrough time; thus for the same influent MG concentration and fixed bed conditions, increased bed height resulted in longer distance for the mass transfer zone to reach the exit and therefore an increase in the breakthrough time.
Along with this the breakthrough time also increases with increase in bed height resulting prolonged saturation for higher bed height columns.
One is based on the bed height ratio (R h ), which means the ratio of the dense bed height to the initial bed height which can be regarded as the bed expansion coefficient.
These two equations are shown as follows, R_{h} = frac{H}{{H_{0} }} (3) R_{varepsilon } = frac{{varepsilon_{0} }}{{varepsilon_{text{s}} }} (4 where H means the dense bed height, m, and H 0 means the initial bed height, m.
If the static bed height is no more than 300 mm then the bed height has minimal effect on the fluidization characteristics.
The effect of the bed height is similar to this in that for longer bed heights, there is increased contact time and hence higher values of KYN.
From Fig. 6a, both the breakthrough times, t b and exhaustion time t e, were found to increase with increasing bed height, whereas the shape of the breakthrough was slightly different with the variation of bed height.
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com