Question: The same reformer as in the previous problem has a problemthe 3.00 liters/s of H 2 is contaminated with 0.600 liters/minute of CO. Assume the

The same reformer as in the previous problem has a problem—the 3.00 liters/s of H₂ is contaminated with 0.600 liters/minute of CO. Assume the shift reactor removes this contaminant down to 10.0 ppm of CO. What is the final composition of gas?

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