HA (273K)= -15000cal/mol k = 0,01dm³/mols (310K) HB (273K)=-20000cal/mol E=10000cal/mol -TA-KCA R=1,987cal/molK CPA CPB CPinert=15cal/molk A → B first order liquid phase reaction takes place adiabatically in a piston flow reactor (PAR). The temperature of the supply current is 310K. The feed stream consists of 75% A and 25% inert material by mole. The molar flow rate of A is 3mol/s and its concentration is 0.1mol/dm3. Calculate the PAR volume for 75% conversion

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PAR =PFR

 

HA (273K)= -15000cal/mol
k = 0,01dm³/mols (310K)
HB (273K)=-20000cal/mol
E=10000cal/mol -TA-KCA R=1,987cal/molK
CPA CPB CPinert=15cal/molk
A → B first order liquid phase reaction takes place adiabatically in a piston flow reactor (PAR). The temperature of the supply
current is 310K. The feed stream consists of 75% A and 25% inert material by mole. The molar flow rate of A is 3mol/s and its
concentration is 0.1mol/dm3. Calculate the PAR volume for 75% conversion
Transcribed Image Text:HA (273K)= -15000cal/mol k = 0,01dm³/mols (310K) HB (273K)=-20000cal/mol E=10000cal/mol -TA-KCA R=1,987cal/molK CPA CPB CPinert=15cal/molk A → B first order liquid phase reaction takes place adiabatically in a piston flow reactor (PAR). The temperature of the supply current is 310K. The feed stream consists of 75% A and 25% inert material by mole. The molar flow rate of A is 3mol/s and its concentration is 0.1mol/dm3. Calculate the PAR volume for 75% conversion
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