1. L15-1 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. L15: Nonisothermal Reactor Example Problems

2. L15-2 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. Review: Multiple Steady States in CSTR Plot of X A,EB vs T and X A,MB vs T Intersections are the T and X A that satisfy both mass balance (MB) & energy balance (EB) equations Each intersection is a steady state (temperature & conversion) Multiple sets of conditions are possible for the same reaction in the same reactor with the same inlet conditions! X A,MB

3. L15-3 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. T R(T) Increase T 0 T R(T) Increase  T0T0 TaTa  = 0  = ∞ For T a < T 0 Review: Heat Removal Term R(T) & T 0 Heat removed: R(T)Heat generated G(T) When T 0 increases, slope stays same & line shifts to right R(T) line has slope of C P0 (1+  ) When  increases from lowering F A0 or increasing heat exchange, slope and x-intercept moves T a <T 0 : x-intercept shifts left as  ↑ T a >T 0 : x-intercept shifts right as  ↑  =0, then T C =T 0  = ∞, then T C =T a

4. L15-4 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. Review: CSTR Stability 1 2 3 R(T) > G(T) → T falls to T=SS 1 G(T) > R(T) → T rises to T=SS 3 G(T) > R(T) → T rises to T=SS 1 R(T) > G(T) → T falls to T=SS 3 Magnitude of G(T) to R(T) curve determines if reactor T will rise or fall G(T) = R(T) intersection, equal rate of heat generation & removal, no change in T G(T) > R(T) (G(T) line above R(T) on graph): rate of heat generation > heat removal, so reactor heats up until a steady state is reached R(T) > G(T) (R(T) line above G(T) on graph): rate of heat generation < heat removal, so reactor cools off until a steady state is reached Heat generated G(T) Heat removed: R(T)

5. L15-5 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Extra info: liquid phase rxn C pA =C pB =15 cal/molK C pC = 30 cal/mol E = 10,000 cal/mol  H A °(273K)= -20 kcal/mol  H B °(273K)= -15 kcal/mol  H C °(273K)= -41 kcal/mol 1.Mole balance 2.Rate Law 3.Stoichiometry 4.Combine rate law & stoichiometry 5.Energy balance 6.Solve Strategy: 6a. Solve CSTR i.Use EB to find T as a function of X A ii.Calculate V using the CSTR design eq with k calculated at that T 6b. Solve PFR i.Use EB to construct table of T as a function of X A ii.Use k = Ae -E/RT to construct table of k as function of T & therefore X A iii.Calculate -r A as a function of T & X A iv.Calculate F A0 /-r A for each T v.Use numeric technique to calculate V

6. L15-6 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Mole balance CSTRPFR Rate law Extra info: C pA =C pB =15 cal/molK C pC = 30 cal/mol E = 10,000 cal/mol  H A °(273K)= -20 kcal/mol  H B °(273K)= -15 kcal/mol  H C °(273K)= -41 kcal/mol Stoichiometry Combine:

7. L15-7 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Combine MB, rate law & stoichiometry for CSTR: CSTR Extra info: C pA =C pB =15 cal/molK C pC = 30 cal/mol E = 10,000 cal/mol  H A °(273K)= -20 kcal/mol  H B °(273K)= -15 kcal/mol  H C °(273K)= -41 kcal/mol

8. L15-8 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Energy balance Extra info: C pA =C pB =15 cal/molK C pC = 30 cal/mol E = 10,000 cal/mol  H A °(273K)= -20 kcal/mol  H B °(273K)= -15 kcal/mol  H C °(273K)= -41 kcal/mol 0 0 Solve for T: Substitute: Multiply out quantities in brackets, bring T to 1 side of equation, factor out T, divide by quantity in bracket: Evaluate  C p :

9. L15-9 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Energy balance Extra info: C pA =C pB =15 cal/molK C pC = 30 cal/mol E = 10,000 cal/mol  H A °(273K)= -20 kcal/mol  H B °(273K)= -15 kcal/mol  H C °(273K)= -41 kcal/mol Evaluate  i C p : Evaluate  H° RX (T R ): Simplify EB:

10. L15-10 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Solve for CSTR volume: use EB to find T when X A =0.85 Extra info: C pA =C pB =15 cal/molK C pC = 30 cal/mol E = 10,000 cal/mol  H A °(273K)= -20 kcal/mol  H B °(273K)= -15 kcal/mol  H C °(273K)= -41 kcal/mol

11. L15-11 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. XAXA T (K)k (dm 3 /mol·s)-r A (mol/dm 3 ·s)F A0 /-r A (dm 3 ) 0 0.2 0.4 0.6 0.8 0.85 The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Solve for PFR: i.Use EB to construct table of T as a function of X A (We’re interested in range where X A = 0 to X A = 0.85) 300

12. L15-12 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. XAXA T (K)k (dm 3 /mol·s)-r A (mol/dm 3 ·s)F A0 /-r A (dm 3 ) 0300 0.2340 0.4380 0.6420 0.8460 0.85470 The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Solve for PFR: i.Use EB to construct table of T as a function of X A -Temperature range should cover X A = 0 to X A = 0.85 ii.Calculate k(T) for each T in the table

13. L15-13 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Solve for PFR: i.Use EB to construct table of T as a function of X A -Temperature range should cover X A = 0 to X A = 0.85 ii.Calculate k(T) for each T in the table XAXA T (K)k (dm 3 /mol·s)-r A (mol/dm 3 ·s)F A0 /-r A (dm 3 ) 03000.01 0.23400.072 0.43800.34 0.64201.21 0.84603.42 0.854704.31

14. L15-14 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Solve for PFR: i.Use EB to construct table of T as a function of X A -Temperature range should cover X A = 0 to X A = 0.85 XAXA T (K)k (dm 3 /mol·s)-r A (mol/dm 3 ·s)F A0 /-r A (dm 3 ) 03000.01 0.23400.072 0.43800.34 0.64201.21 0.84603.42 0.854704.31 iii.Calculate –r A each X A and k in the table ii.Calculate k(T)

15. L15-15 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Solve for PFR: i.Use EB to construct table of T as a function of X A -Temperature range should cover X A = 0 to X A = 0.85 XAXA T (K)k (dm 3 /mol·s)-r A (mol/dm 3 ·s)F A0 /-r A (dm 3 ) 03000.010.0001 0.23400.0720.00046 0.43800.340.00122 0.64201.210.00194 0.84603.420.0014 0.854704.310.00097 ii.Calculate k(T) iii.Calculate –r A each X A and k in the table

16. L15-16 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Solve for PFR: i.Use EB to construct table of T as a function of X A -Temperature range should cover X A = 0 to X A = 0.85 XAXA T (K)k (dm 3 /mol·s)-r A (mol/dm 3 ·s)F A0 /-r A (dm 3 ) 03000.010.0001 0.23400.0720.00046 0.43800.340.00122 0.64201.210.00194 0.84603.420.0014 0.854704.310.00097 ii.Calculate k(T) iii.Calculate F A0 /–r A for each X A in the table iii.Calculate –r A each X A and k in the table

17. L15-17 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Solve for PFR: i.Use EB to construct table of T as a function of X A -Temperature range should cover X A = 0 to X A = 0.85 XAXA T (K)k (dm 3 /mol·s)-r A (mol/dm 3 ·s)F A0 /-r A (dm 3 ) 03000.010.00012000 0.23400.0720.00046434.8 0.43800.340.00122163.9 0.64201.210.00194103.1 0.84603.420.0014142.9 0.854704.310.00097206.2 ii.Calculate k(T) iii.Calculate F A0 /–r A for each X A in the table iii.Calculate –r A each X A and k in the table

18. L15-18 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary irreversible reaction A + B → C is carried out adiabatically in a flow reactor with Ẇ S =0. An equal molar feed of A & B enters at 300K with  0 = 2 dm 3 /s and C A0 = 0.1 mol/dm 3. What is the PFR & CSTR volume required to achieve X A =0.85? Solve for PFR: XAXA T (K)k (dm 3 /mol·s)-r A (mol/dm 3 ·s)F A0 /-r A (dm 3 ) 03000.010.00012000 0.23400.0720.00046434.8 0.43800.340.00122163.9 0.64201.210.00194103.1 0.84603.420.00137146 0.854704.310.00097206.2 Numeric evaluation by parts: 5-point rule for X A interval 0 to 0.8, 2-point rule for X A interval from 0.8 to 0.85:

19. L15-19 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. For these conditions, what is the max T 0 that would keep T≤ 550K at complete conversion? T≤ 550K at complete conversion, X A =1: Max T 0 is 350K

20. L15-20 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The first order irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains A and an inert liquid in equimolar amounts, where F A0 = 80 mol/min. What is the reactor temp when the inlet temp T 0 is 450K? UA= 8000 cal/min·K T a = 300K  H RX =-7500 cal/mol C pA = C pB =20 cal/mol·K C pi =30 cal/mol·K  =100 min E=40,000 cal/mol k=6.6 x 10 -3 min -1 at 350K Need to find where G(T)=R(T) for T 0 = 450K 1.Put R(T) & G(T) in terms of constants in the problem statement 2.Plot R(T) vs T and G(T) vs T on the same graph & find where they intersect

21. L15-21 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The first order irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains A and an inert liquid in equimolar amounts, where F A0 = 80 mol/min. What is the reactor temp when the inlet temp T 0 is 450K? UA= 8000 cal/min·K T a = 300K  H RX =-7500 cal/mol C pA = C pB =20 cal/mol·K C pi =30 cal/mol·K  =100 min E=40,000 cal/mol k=6.6 x 10 -3 min -1 at 350K Put  in terms of constants from the problem statement: I = inert Put R(T) in terms of constants in the problem statement, starting with C P0 : Put T C in terms of constants in the problem statement:

22. L15-22 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The first order irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains A and an inert liquid in equimolar amounts, where F A0 = 80 mol/min. What is the reactor temp when the inlet temp T 0 is 450K? UA= 8000 cal/min·K T a = 300K  H RX =-7500 cal/mol C pA = C pB =20 cal/mol·K C pi =30 cal/mol·K  =100 min E=40,000 cal/mol k=6.6 x 10 -3 min -1 at 350K Find steady state temp [G(T)=R(T) ] for T 0 = 450K I = inert Plug  and T c into R(T):

23. L15-23 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The first order irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains A and an inert liquid in equimolar amounts, where F A0 = 80 mol/min. What is the reactor temp when the inlet temp T 0 is 450K? UA= 8000 cal/min·K T a = 300K  H RX =-7500 cal/mol C pA = C pB =20 cal/mol·K C pi =30 cal/mol·K  =100 min E=40,000 cal/mol k=6.6 x 10 -3 min -1 at 350K Find steady state temp [G(T)=R(T) ] for T 0 = 450K I = inert Now put G(T) in terms of constants from the problem statement: Rate law:Stoichiometry: Combine:

24. L15-24 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The first order irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains A and an inert liquid in equimolar amounts, where F A0 = 80 mol/min. What is the reactor temp when the inlet temp T 0 is 450K? UA= 8000 cal/min·K T a = 300K  H RX =-7500 cal/mol C pA = C pB =20 cal/mol·K C pi =30 cal/mol·K  =100 min E=40,000 cal/mol k=6.6 x 10 -3 min -1 at 350K Find steady state temp [G(T)=R(T) ] for T 0 = 450K I = inert Plug rate law into G(T) & simplify:

25. L15-25 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The first order irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains A and an inert liquid in equimolar amounts, where F A0 = 80 mol/min. What is the reactor temp when the inlet temp T 0 is 450K? UA= 8000 cal/min·K T a = 300K  H RX =-7500 cal/mol C pA = C pB =20 cal/mol·K C pi =30 cal/mol·K  =100 min E=40,000 cal/mol k=6.6 x 10 -3 min -1 at 350K Steady state temp [G(T)=R(T) ] for T 0 = 450K I = inert Rearrange so can be solved with Polymath nonlinear equation solver: Use design equation to get X A as an explicit equation: Explicit equation for Polymath

26. L15-26 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. Enter in Polymath: VariableValuef(x) Initial Guess 1T399.9425-4.547E-12 400. ( 300. < T < 500. ) Calculated values of NLE variables If you want to see this graphically, click the Graph button above Select graph

27. L15-27 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. Format the graph Create a table, save it as a text file, import into Excel, & make a graph with correct labels

28. L15-28 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. Plot reactor temperature as a function of feed temperature, with T 0 between 350 and 450K C P0 and  do not depend on T 0, but T C does Do we need to change G(T) or R(T) when T 0 changes? G(T) does not depend on T 0 Need to re-run the Polymath program using various T 0 between 350 and 450K to find the new steady state reactor temperatures Enter equations into Polymath so that R(T) varies according to T 0, & run program with varied values of T 0 Run over and over again, varying T 0 from 350 K to 450 K In Excel, create a table of T vs T 0, and make a graph

29. L15-29 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. T 0 (K)T 1 (K)T 2 (K)T 3 (K) 350316.7 360320.15 370323.6357.16370.3 380327.3353.4375.1 390331.2350.1379.1 400336.3346382.8 410386 420389.8 430393.2 440396.6 450399.9 Steady state temperature as a function of T 0

30. L15-30 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary, irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains pure A, & it enters the reactor at 310 K, where F A0 = 60 mol/min and  0 = 300 L/min. Extra info: UA= 3200 cal/minK T a = 340 K ∆H RX (T R ) = -10,000 cal/mol C pA =15 cal/mol·K C pB =15 cal/mol·K  =120 min E =20,000 cal/mol k(400K) = 1 min -1 What is the value of the heat generated term (with units) when a disturbance causes the temperature in the reactor to drift to 360 K if –r A = 0.0015 mol/Lmin at 360K? (The reactor is NOT at the steady state.)

31. L15-31 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary, irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains pure A, & it enters the reactor at 310 K, where F A0 = 60 mol/min and  0 = 300 L/min. Extra info: UA= 3200 cal/minK T a = 340 K ∆H RX (T R ) = -10,000 cal/mol C pA =15 cal/mol·K C pB =15 cal/mol·K  =120 min E =20,000 cal/mol k(400K) = 1 min -1 What is the value of the heat generated term (with units) when a disturbance causes the temperature in the reactor to drift to 360 K if –r A = 0.0015 mol/Lmin at 360K? (The reactor is NOT at the steady state.)

32. L15-32 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary, irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains pure A, & it enters the reactor at 310 K, where F A0 = 60 mol/min and  0 = 300 L/min. Extra info: UA= 3200 cal/minK T a = 340 K ∆H RX (T R ) = -10,000 cal/mol C pA =15 cal/mol·K C pB =15 cal/mol·K  =120 min E =20,000 cal/mol k(400K) = 1 min -1 What is the value of the heat generated term (with units) when a disturbance causes the temperature in the reactor to drift to 360 K if –r A = 0.0015 mol/Lmin at 360K? (The reactor is NOT at the steady state.)

33. L15-33 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary, irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains pure A, & it enters the reactor at 310 K, where F A0 = 60 mol/min and  0 = 300 L/min. Extra info: UA= 3200 cal/minK T a = 340 K ∆H RX (T R ) = -10,000 cal/mol C pA =15 cal/mol·K C pB =15 cal/mol·K  =120 min E =20,000 cal/mol k(400K) = 1 min -1 What is the value of the heat removal term (with units) when a disturbance causes the temperature in the reactor to drift to 360 K if –r A = 0.0015 mol/Lmin at 360K? (The reactor is NOT at the steady state.)

34. L15-34 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary, irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains pure A, & it enters the reactor at 310 K, where F A0 = 60 mol/min and  0 = 300 L/min. Extra info: UA= 3200 cal/minK T a = 340 K ∆H RX (T R ) = -10,000 cal/mol C pA =15 cal/mol·K C pB =15 cal/mol·K  =120 min E =20,000 cal/mol k(400K) = 1 min -1 What is the value of the heat removal term (with units) when a disturbance causes the temperature in the reactor to drift to 360 K if –r A = 0.0015 mol/Lmin at 360K? (The reactor is NOT at the steady state.)

35. L15-35 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary, irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains pure A, & it enters the reactor at 310 K, where F A0 = 60 mol/min and  0 = 300 L/min. Extra info: UA= 3200 cal/minK T a = 340 K ∆H RX (T R ) = -10,000 cal/mol C pA =15 cal/mol·K C pB =15 cal/mol·K  =120 min E =20,000 cal/mol k(400K) = 1 min -1 What is the value of the heat removal term (with units) when a disturbance causes the temperature in the reactor to drift to 360 K if –r A = 0.0015 mol/Lmin at 360K? (The reactor is NOT at the steady state.)

36. L15-36 Slides courtesy of Prof M L Kraft, Chemical & Biomolecular Engr Dept, University of Illinois, Urbana-Champaign. The elementary, irreversible reaction A(l) → B(l) is carried out in a jacketed CSTR. The feed contains pure A, & it enters the reactor at 310 K, where F A0 = 60 mol/min and  0 = 300 L/min. Extra info: UA= 3200 cal/minK T a = 340 K ∆H RX (T R ) = -10,000 cal/mol C pA =15 cal/mol·K C pB =15 cal/mol·K  =120 min E =20,000 cal/mol k(400K) = 1 min -1 When a disturbance causes the temperature in the reactor to drift to 360 K if –r A = 0.0015 mol/Lmin at 360K, Will the reactor temperature heat up, cool down, or stay at 360 K? G(T) > R(T) so the reactor will heat up