Calculate the volume using simple numerical methods like simpsons 3/8 rule or combined with 1/3 rule the PDE for PFR and CSTR.

The gas-phase reversible reaction AB is carried out under high pressure in a packed-bed reactor with pressure drop. The feed consists of both inerts I and Species A with the ratio of inerts to the species A being 2 to 1 . The entering molar flow apter 11 Questions and Problems 535 rate of A is 5mol/min at a temperature of 300K and a concentration of 2mol/dm3. Work this problem in terms of volume. Hint: V=W/a,rA=BrA. Additional information: FA0=5.0mol/minT0=300KCA0=2mol/dm3TI=300KC1=2CA0k1=0.1min1at300KCP1=18cal/mol/KUa=150cal/dm3/min/KCPA=160cal/mol/KTao=300KE=10,000cal/molV=40dm3HRx=20,000cal/molb=0.02dm3KC=1,000at300KCoolantCPB=160cal/mol/KmC=50mol/minB=1.2kg/dm3CPCoxl=20cal/mol/K The gas-phase reversible reaction AB is carried out under high pressure in a packed-bed reactor with pressure drop. The feed consists of both inerts I and Species A with the ratio of inerts to the species A being 2 to 1 . The entering molar flow apter 11 Questions and Problems 535 rate of A is 5mol/min at a temperature of 300K and a concentration of 2mol/dm3. Work this problem in terms of volume. Hint: V=W/a,rA=BrA. Additional information: FA0=5.0mol/minT0=300KCA0=2mol/dm3TI=300KC1=2CA0k1=0.1min1at300KCP1=18cal/mol/KUa=150cal/dm3/min/KCPA=160cal/mol/KTao=300KE=10,000cal/molV=40dm3HRx=20,000cal/molb=0.02dm3KC=1,000at300KCoolantCPB=160cal/mol/KmC=50mol/minB=1.2kg/dm3CPCoxl=20cal/mol/K