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From Figure 3.6, it can also be seen that the highest power input is required for compression of the purge gas from 5400 kPa to 5500 kPa: the purge gas compressor consumes up to 53% of the total energy required for process operation. Figure 3.7 shows the variation of the total energy requirement in terms of energy ratio shown in Equation (3.14). The energy ratio is defined as the ratio of total energy required for the operation of the purification process to combustion potential of the product. The product collection in the denominator is varied by changing the feed and collection times, while the total energy required in the numerator remains unaffected with any change in these times, as the energy required is a function of the monolith mass, temperature swing and the purge stage time. Ratio EDeso ESens EHTF,recir Epurge Energy PurityCH4 M prod LHV (3.14) Figure 3.7. Variation of energy ratio plotted with process capacity for variable feed times. 81PDF Image | TEMPERATURE SWING ADSORPTION PROCESSES FOR GAS SEPARATION
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