Figure 2:  Test Facility

 

 Compressed air is heated by the test facility to simulate the heat of compression of a hypothetical turbocompressor.  Hot day conditions of 50ºC at the compressor inlet are assumed for all data shown here.  The compressed air temperature is adjusted to simulate the projected compressor efficiency for the range of stack operating pressures.  As power demand increases, the compressor accelerates forcing higher mass flow through the cathode.  As flow increases, pressure and temperature are increased as shown in Table 1.  This table represents the conditions at Station 1 of Figure 1.

 

 

 Table 1:  Enthalpy Wheel Inlet Conditions (Hot Day)

 

Power (%)

25

50

100

Flow (SLPM)

658

1328

3019

Pressure (atm abs)

1.38

1.75

2.50

Temperature (ºC)

87

118

169

     

 

 A packed tower humidifier simulates a fuel cell cathode operating at a cathode exhaust condition of 80ºC saturated. (Station 3 of Figure 1)  The simulation also includes a mass flow reduction corresponding to a Stoichimetic ratio of 2.0 and a typical second order stack pressure drop of 0.21 atm (3.0 psid) at full flow conditions.

 

 

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Text Box: Experimental
 
 
The enthalpy wheel heat exchanger for this 50kW fuel cell engine simulation is approximately 431mm (17”) long and 165mm (6.5”) in diameter and weighs 7.8 kg (15 lbs.).  The cordierite/desiccant core is 142 mm (5.6”) in diameter by 152 mm (6”) long.  The core rotates at 60 rpm for all data shown here.  Figure 2 illustrates the enthalpy wheel installed in the test facility.
 
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 Figure 2:  Test Facility
 
 Compressed air is heated by the test facility to simulate the heat of compression of a hypothetical turbocompressor.  Hot day conditions of 50ºC at the compressor inlet are assumed for all data shown here.  The compressed air temperature is adjusted to simulate the projected compressor efficiency for the range of stack operating pressures.  As power demand increases, the compressor accelerates forcing higher mass flow through the cathode.  As flow increases, pressure and temperature are increased as shown in Table 1.  This table represents the conditions at Station 1 of Figure 1.
 
 
 Table 1:  Enthalpy Wheel Inlet Conditions (Hot Day)
 
Power (%)
25
50
100
Flow (SLPM)
658
1328
3019
Pressure (atm abs)
1.38
1.75
2.50
Temperature (ºC)
87
118
169
     
 
 A packed tower humidifier simulates a fuel cell cathode operating at a cathode exhaust condition of 80ºC saturated. (Station 3 of Figure 1)  The simulation also includes a mass flow reduction corresponding to a Stoichimetic ratio of 2.0 and a typical second order stack pressure drop of 0.21 atm (3.0 psid) at full flow conditions.
 
 
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