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integration of solid oxide fuel cells and ... - Ea Energianalyse

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4. SYSTEM DESCRIPTION<br />

which increases system performance <strong>and</strong> therefore called Additional Air<br />

Preheating.<br />

Afterwards the air is preheated by high temperature exhaust gas by<br />

GGHEX3 to a temperature <strong>of</strong> 690 ◦ C before it enters the SOFC cathode<br />

inlet point 14.<br />

4.2.3 SOFC stack<br />

The specified cell area <strong>of</strong> 0,0228 m 2 makes the SOFC the only component<br />

in the model having a physical size. The number <strong>of</strong> <strong>cells</strong> per stack has<br />

been set to 60. However these value does not affect system efficiency or<br />

system size - the number <strong>of</strong> stacks in the system is variable <strong>and</strong> will depend<br />

on the enthalpy flow <strong>of</strong> the <strong>fuel</strong> input 7 . So the cell area <strong>and</strong> number<br />

<strong>of</strong> <strong>cells</strong> are only specified to have some kind <strong>of</strong> relation to real systems.<br />

The <strong>fuel</strong> utilization factor (U f ) is set 70% which is a typical value for <strong>fuel</strong><br />

cell systems [25]. Together with the <strong>fuel</strong> input <strong>of</strong> 100kW <strong>and</strong> recirculation<br />

factor <strong>of</strong> 0,62 this gives the current <strong>of</strong> the system. Instead <strong>of</strong> the <strong>fuel</strong> input<br />

<strong>of</strong> 100kW the current draw could have been specified, but when the <strong>fuel</strong><br />

input is kept constant, the cooling <strong>and</strong> heating powers become easier to<br />

evaluate during the parameter investigations in chapter5.3.<br />

The current density (i d ) is a parameter which determines how much<br />

the SOFC is loaded (regulation). The value <strong>of</strong> 3000 A/m 2 is an estimate<br />

based on data from TOFC. The <strong>fuel</strong> input determines the size <strong>of</strong> the system<br />

(100kW <strong>fuel</strong> input). These two factors give the number <strong>of</strong> stacks,<br />

which becomes 20,15. Instead <strong>of</strong> the current density the number <strong>of</strong> stacks<br />

n st ack ) could be specified, but it is impractical to have more than one extensive<br />

parameter.<br />

The two inlets at the SOFC are assumed to have equal temperature, <strong>and</strong><br />

the two outlets have the same temperature. ∆T min,SOFC determines the<br />

temperature increase from inlet (point 5 <strong>and</strong> 14) to the outlet (point 6<br />

<strong>and</strong> 15). ∆T min,SOFC has a value <strong>of</strong> 90 ◦ C which is a typical value <strong>of</strong> <strong>fuel</strong><br />

<strong>cells</strong> today [25]. It is important that the limits <strong>of</strong> minimum temperature<br />

at the inlet <strong>and</strong> maximum temperature at the outlet are not violated, as<br />

described in section 3.12 page 64.<br />

7 Alternatively the current draw could have be specified or the number <strong>of</strong> stacks<br />

(since the current density is also given)<br />

84

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