P11-4A The elementary, irreversible, organic liquid-phase reaction boO con. h lo eno diw briong A +B→C Addia is carried out adiabatically in a flow reactor. An equal molar feed in A and B enters at 27°C, and the volu- metric flow rate is 2 dm³/s and CA0 = 0.1 kmol/m³. - 0tou1 Additional information: bas H (273 K) = - 20 kcal/mol, H (273 K) = -15 kcal/mol, HE(273 K) = -41 kcal/molq oldsT oostorl ni %3D STOUT 10 CP, = CP, = 15 cal/mol · K Cp. = 30 cal/mol · K %3D %3D B. dm3 mol ·s k = 0.01 at 300 K E = 10,000 cal/mol %3D %3D

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Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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What is the CSTR volume necessary to achieve 90% conversion?

P11-4A The elementary, irreversible, organic liquid-phase reaction boO con. h
lo eno diw briong
A +B→C
Addia
is carried out adiabatically in a flow reactor. An equal molar feed in A and B enters at 27°C, and the volu-
metric flow rate is 2 dm³/s and CA0 = 0.1 kmol/m³. -
0tou1 Additional information:
bas
H (273 K) = - 20 kcal/mol, H (273 K) = -15 kcal/mol,
HE(273 K) = -41 kcal/molq oldsT oostorl ni
%3D
STOUT 10
CP, = CP, = 15 cal/mol · K Cp. = 30 cal/mol · K
%3D
%3D
B.
dm3
mol ·s
k = 0.01
at 300 K E = 10,000 cal/mol
%3D
%3D
Transcribed Image Text:P11-4A The elementary, irreversible, organic liquid-phase reaction boO con. h lo eno diw briong A +B→C Addia is carried out adiabatically in a flow reactor. An equal molar feed in A and B enters at 27°C, and the volu- metric flow rate is 2 dm³/s and CA0 = 0.1 kmol/m³. - 0tou1 Additional information: bas H (273 K) = - 20 kcal/mol, H (273 K) = -15 kcal/mol, HE(273 K) = -41 kcal/molq oldsT oostorl ni %3D STOUT 10 CP, = CP, = 15 cal/mol · K Cp. = 30 cal/mol · K %3D %3D B. dm3 mol ·s k = 0.01 at 300 K E = 10,000 cal/mol %3D %3D
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