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Chapter 4 Thermodynamic analysis In Figure 4.17 one can observe that there is a certain balance among the electrical efficiencies of the different configurations, thus confirming the prediction made in Section 2.4.2, i.e. that ICE and GT solutions would present comparable efficiencies. Obviously this is valid neglecting GT DIR REG that almost reaches 30%, i.e. the value achieved by the natural gas plant (indeed, there is practically no thermodynamic reason why this should not happen). ICE GAS efficiency is about 24%: this value could be predictable, as it is essentially the result of the product of electrical efficiency in case of natural gas feeding (30%) and gasifier cold gas efficiency (80%), since auxiliaries needs are limited. GT GAS REG almost reaches the same result, but only in the pressurised configuration. The ambient pressure one, in fact, is heavily penalised by power consumption of the syngas compressor, that passes from about 3 kWel to about 28 kWel, due to the larger mass flow rate to be supplied compared to the natural gas feeding: this nullifies the benefits related to the higher power output of the expander, which increases gross power output from 106 kWel to 124 kWel. In case of pressurised gasifier, instead, no fuel compressor is required anymore and consumption due to the air compressor required to feed the gasifier is lower (even if it is still considerable, 13 kWel). Moreover, it is recalled that pressurised conditions make the gasification process more efficient (in this case working pressure is 6.5 bar; for higher scale it reaches 20 bar). This is due to two different contributions. The first one is obviously the pressure itself (cold gas efficiency is an increasing function of this parameter), whereas the second one is related to the fact that air must be compressed: since compression is in general adiabatic, air temperature increases with the pressure ratio and this results in higher performance, same as in all combustion processes. Figures 4.19 and 4.20 graphically show the effects of these two thermodynamic parameters on gasifier cold gas efficiency. Cold gas efficiency of an ambient pressure gasifier as a function of air temperature is shown in the former, in order to investigate the pure effect of feeding this quantity, whereas in the latter the pressure effect is studied in two cases: in the first one it is investigated neglecting temperature, i.e. supposing to have a pressurised air source at ambient temperature, while in the second one a real configuration of pressurised gasifier fed by air compressed, and thus heated, by a compressor is being considered (the result is a sort of composition of the two previous curves). In these analyses, design data are obviously 154PDF Image | SMALL-SCALE BIOMASS POWER GENERATION
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