![Page 1: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/1.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Process Intensification for AutothermalReaction
Manal Moftah Saleh
University of Wollongong
November, 2015
![Page 2: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/2.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Presentation Outline
1 Introduction
2 Objectives of the research
3 work done so farModel equationsThe required feed temperature for 90 % conversion in R1Steady-state solutions
4 Conclusion
5 Thanks
![Page 3: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/3.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Motivation
The world is currently facing critical challenges:
Future energy requirements.
Greenhouse emissions.
Rising oil prices and “peak” oil resources
Possible solutions:
natural gas → syngas → liquid fuels/H2.
Aim: develop mathematical models for autothermal processesto maximize product concentration.
![Page 4: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/4.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Motivation
The world is currently facing critical challenges:
Future energy requirements.
Greenhouse emissions.
Rising oil prices and “peak” oil resources
Possible solutions:
natural gas → syngas → liquid fuels/H2.
Aim: develop mathematical models for autothermal processesto maximize product concentration.
![Page 5: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/5.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Models based on CSTR. Advantages are:
Operated continuously.
Reduces running costs.
Relatively easy to maintain temperature control.
Control of the equipment and grade of final product issimplified.
Single or cascade.
![Page 6: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/6.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Models based on CSTR. Advantages are:
Operated continuously.
Reduces running costs.
Relatively easy to maintain temperature control.
Control of the equipment and grade of final product issimplified.
Single or cascade.
![Page 7: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/7.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Models based on CSTR. Advantages are:
Operated continuously.
Reduces running costs.
Relatively easy to maintain temperature control.
Control of the equipment and grade of final product issimplified.
Single or cascade.
![Page 8: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/8.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Models based on CSTR. Advantages are:
Operated continuously.
Reduces running costs.
Relatively easy to maintain temperature control.
Control of the equipment and grade of final product issimplified.
Single or cascade.
![Page 9: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/9.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Models based on CSTR. Advantages are:
Operated continuously.
Reduces running costs.
Relatively easy to maintain temperature control.
Control of the equipment and grade of final product issimplified.
Single or cascade.
![Page 10: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/10.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Models based on CSTR. Advantages are:
Operated continuously.
Reduces running costs.
Relatively easy to maintain temperature control.
Control of the equipment and grade of final product issimplified.
Single or cascade.
![Page 11: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/11.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Autothermal reactor
What is an autothermalreactor?
![Page 12: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/12.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Presentation Outline
1 Introduction
2 Objectives of the research
3 work done so farModel equationsThe required feed temperature for 90 % conversion in R1Steady-state solutions
4 Conclusion
5 Thanks
![Page 13: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/13.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Objectives of the research
Investigate the chemical mechanism
AQ1<0−−−→k1
BQ2>0−−−→k2
C·
where ki = ai exp[−EiRTi
]i = 1, 2.
Maximize the product concentration (C ).
![Page 14: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/14.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Presentation Outline
1 Introduction
2 Objectives of the research
3 work done so farModel equationsThe required feed temperature for 90 % conversion in R1Steady-state solutions
4 Conclusion
5 Thanks
![Page 15: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/15.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Diabatic CSTR
A diabatic process is a process that occurs with the transfer ofheat between a system and its surroundings.
T1,Catalyst 1 T2,Catalyst 2- - -
T(a,1) T(a,2)
q,T0,A0 A2,B2,C2A1,B1
![Page 16: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/16.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Characteristic Temperature Tc
Normally reaction terms written as
a exp
[E
RT
].
The pre-exponential factor in the studied model is written as
a =Eα
RT 2c
exp
[E
RTc
].
![Page 17: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/17.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Dimensional model equations: Reactor one
Concentration of reactant A
V1dA1
dt= q(A0 − A1)− V1a1 exp
[−E1
RT1
]A1. (1)
Concentration of intermediate B
V1dB1
dt= q(B0 − B1) + V1a1 exp
[−E1
RT1
]A1. (2)
Concentration of product C
V1dC1
dt= q(C0 − C1) + 0. (3)
![Page 18: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/18.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Temperature inside the reactor
cpgρgV1dT1
dt= qcpgρg (T0 − T1) -Q1V1a1 exp
[−E1
RT1
]A1
− J1χ1S1(T1 − Ta,1). (4)
The pre-exponential factor
a1 =E1α
RT 2c1
exp
[E1
RTc1
]. (5)
![Page 19: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/19.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Reactor two:
Concentration of reactant A
V2dA2
dt= q(A1 − A2) + 0. (6)
Concentration of reactant B
V2dB2
dt= q(B1 − B2)− V2a2 exp
[−E2
RT2
]B2. (7)
Concentration of reactant C
V2dC2
dt= q(C1 − C2) + V2a2 exp
[−E2
RT2
]B2. (8)
![Page 20: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/20.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Temperature inside the reactor
cpgρgV2dT2
dt= qcpgρg (T1 − T2)+Q2V2a2 exp
[−E2
RT2
]B2
− J2χ2S2(T2 − Ta,2). (9)
The pre-exponential factor
a2 =E2α
RT 2c2
exp
[E2
RTc2
]. (10)
![Page 21: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/21.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
A∗1 = 0.1
(a) Q1 = 205.8(KJ mol−1) (b) Q1 = 100(KJ mol−1)
![Page 22: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/22.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Steady-state diagrams (A∗1 = 0.1)
(c) Tc2 = 405(K). (d) Tc2 = 435(K).
![Page 23: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/23.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks (e) Tc2 = 442(K). (f) Tc2 = 448(K).
![Page 24: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/24.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks (g) Tc2 = 464(K). (h) Tc2 = 511(K).
![Page 25: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/25.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
LP unfolding diagram
![Page 26: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/26.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
LP unfolding diagram
![Page 27: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/27.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
LP unfolding diagram
![Page 28: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/28.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
LP unfolding diagram
![Page 29: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/29.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
LP unfolding diagram
![Page 30: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/30.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
LP unfolding diagram
![Page 31: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/31.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
LP unfolding diagram
![Page 32: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/32.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
The key idea
90 % conversion (C ∗2 = 0.9).
A∗1 < 0.1.
Six steady-state diagrams.
LPig < 298(K)
LP unfolding diagram.
![Page 33: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/33.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Presentation Outline
1 Introduction
2 Objectives of the research
3 work done so farModel equationsThe required feed temperature for 90 % conversion in R1Steady-state solutions
4 Conclusion
5 Thanks
![Page 34: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/34.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Conclusion
Reaction occurring in two reactors: endothermic in R1and exothermic in R2.
high conversion in R1 (low endothermicity).
Steady-state solutions.
Interesting results.
![Page 35: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/35.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Conclusion
Reaction occurring in two reactors: endothermic in R1and exothermic in R2.
high conversion in R1 (low endothermicity).
Steady-state solutions.
Interesting results.
![Page 36: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/36.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Conclusion
Reaction occurring in two reactors: endothermic in R1and exothermic in R2.
high conversion in R1 (low endothermicity).
Steady-state solutions.
Interesting results.
![Page 37: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/37.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Conclusion
Reaction occurring in two reactors: endothermic in R1and exothermic in R2.
high conversion in R1 (low endothermicity).
Steady-state solutions.
Interesting results.
![Page 38: Process Intensification for Autothermal Reaction · 2015-12-07 · Process Intensi cation for Autothermal Reaction Manal Moftah Saleh Introduction Objectives of the research work](https://reader034.vdocument.in/reader034/viewer/2022042914/5f4eb7ddd2918f3f434740a6/html5/thumbnails/38.jpg)
ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Presentation Outline
1 Introduction
2 Objectives of the research
3 work done so farModel equationsThe required feed temperature for 90 % conversion in R1Steady-state solutions
4 Conclusion
5 Thanks
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ProcessIntensification
forAutothermal
Reaction
Manal MoftahSaleh
Introduction
Objectives ofthe research
work done sofar
Model equations
The requiredfeed temperaturefor 90 %conversion in R1
Steady-statesolutions
Conclusion
Thanks
Acknowledgment
Libyan government through the awarding of a PhDscholarship.
Assoc Prof. Mark I Nelson and co-supervisors.
My family (husband) for preceding help and suitableenvironment.
The organiser of NSW ANZIAM meeting.