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A Life Cycle Assessment of the PureCell Stationary Fuel Cell System ...

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Electricity Generation<br />

The input <strong>of</strong> natural gas and <strong>the</strong> emissions caused by <strong>the</strong> steam reforming process are<br />

taken into account here. Table 4-24 gives <strong>the</strong> natural gas input and <strong>the</strong> emissions for <strong>the</strong><br />

production <strong>of</strong> 200 kWh, which is equal to running <strong>the</strong> <strong>Pure<strong>Cell</strong></strong> system for one hour.<br />

These data are given to show which calculations were used to determine <strong>the</strong> emissions.<br />

Thereafter <strong>the</strong>se data are scaled up to <strong>the</strong> <strong>Pure<strong>Cell</strong></strong> system lifetime <strong>of</strong> 85,000 hrs in<br />

order to provide <strong>the</strong> inventory data which are needed to describe <strong>the</strong> <strong>Pure<strong>Cell</strong></strong> system’s<br />

total life cycle.<br />

Products Amount Unit<br />

Generated electricity, 480 Volt, 60 Hz 200 kWh<br />

Produced heat at 140 F 271.025 kWh<br />

Materials/fuels<br />

Natural gas FAL (Franklin) 2050 cuft<br />

3<br />

Emissions to air<br />

NOx 0.0032 lb<br />

CO 0.0046 lb<br />

CO2 112.2 kg<br />

non-methane hydrocarbon (NMHC) 0.000072 lb<br />

Table 4-24: 200 kWh electricity generation inventory data<br />

The natural gas input and <strong>the</strong> emission <strong>of</strong> NO , CO and NMHC are data measured by<br />

UTC Power [21]. The CO<br />

2<br />

emissions however are calculated, since no measured data<br />

are available. The calculations are based on <strong>the</strong> assumption that natural gas is<br />

100% CH 4<br />

. In practice, this is usually around 95%, with <strong>the</strong> o<strong>the</strong>r 5% mainly including<br />

ethane, nitrogen, and higher order hydrocarbons. Ano<strong>the</strong>r assumption is that all <strong>the</strong><br />

carbon input results in CO<br />

2<br />

output, <strong>the</strong>reby neglecting <strong>the</strong> CO and NMHC emissions.<br />

The calculations are based on <strong>the</strong> steam reforming and low shift reactions:<br />

CH + +<br />

(steam reforming)<br />

4<br />

H<br />

2O<br />

→ CO 3H<br />

2<br />

CO + H +<br />

(shift reaction)<br />

2O<br />

→ CO2<br />

H<br />

2<br />

This results in <strong>the</strong> following overall reaction:<br />

CH 2 + H<br />

4<br />

+ H<br />

2O<br />

→ CO2<br />

4<br />

2<br />

x<br />

3 cuft = cubic feet<br />

41

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