Example 1: The decomposition of hydrazine over a packed bed of alumina-supported iridium catalyst is of interest . In a proposed study, a 2% hydrazine in 98% helium mixture is to be passed over a...


Example 1:<br>The decomposition of hydrazine over a packed bed of alumina-supported iridium<br>catalyst is of interest . In a proposed study, a 2% hydrazine in 98% helium mixture is<br>to be passed over a packed bed of cylindrical particles 0.25 cm in diameter and 0.5<br>cm in length at a gas-phase velocity of 15 m/s and a temperature of 750 K. The<br>kinematic viscosity of helium at this temperature is 4.5 104 m² /s. The hydrazine<br>decomposition reaction is believed to be externally mass transfer–limited under these<br>conditions. If the packed bed is 0.05 m in length, what conversion can be expected?<br>Assume isothermal operation.<br>Additional information<br>0.69 × 10-4 m²/s at 298 K<br>EER<br>DAB<br>Bed porosity: 30%<br>

Extracted text: Example 1: The decomposition of hydrazine over a packed bed of alumina-supported iridium catalyst is of interest . In a proposed study, a 2% hydrazine in 98% helium mixture is to be passed over a packed bed of cylindrical particles 0.25 cm in diameter and 0.5 cm in length at a gas-phase velocity of 15 m/s and a temperature of 750 K. The kinematic viscosity of helium at this temperature is 4.5 104 m² /s. The hydrazine decomposition reaction is believed to be externally mass transfer–limited under these conditions. If the packed bed is 0.05 m in length, what conversion can be expected? Assume isothermal operation. Additional information 0.69 × 10-4 m²/s at 298 K EER DAB Bed porosity: 30%

Jun 07, 2022
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