Title: Prepregs Honeycomb
1Plantwide control structure design for an
acid-catalyzed process to produce biodiesel from
used palm oil
Adviser Dr. Soorathep Kheawhom
Presented by Teerapan Rujirachun
Department of Chemical Engineering Faculty of
Engineering, Chulalongkorn University Bangkok
10330, Thailand
2Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ? Conclusions
? Introduction
3(No Transcript)
4Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Theory
5Transesterification
Biodiesel
Catalyst
Vegetable oil or Animal fat
Alcohol
Glycerol
6Effect of Alkali-Catalyst
7Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Biodiesel plant
8Biodiesel Production
Prepare waste cooking oil and other chemical
Transesterification
Separate Biodiesel from Glycerol
Catalyst Removal
Biodiesel Purification
Glycerine Purification
9Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Steady State Simulation
10Biodiesel Production
Mixing
Transesterification
Biodiesel Purification
Water Washing
Acid Removal
Recycle Methanol
Heat Exchanger
Methanol Recovery
Glycerol Purification
CaO H2SO4 ? CaSO4 H2O
11Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Dynamic State Simulation
12Plantwide Control Procedure
Luyben Tyreus 1998
Establish control objectives
Determine control degrees of freedom
Establish energy management system
13Plantwide Control Procedure
Establish energy management system
14Plantwide Control Procedure
Set production rate
15Plantwide Control Procedure
Set production rate
16Plantwide Control Procedure
Set production rate
Control product quality and handle safety,
operational, and environmental constraints
17Plantwide Control Procedure
Control product quality
18Plantwide Control Procedure
Set production rate
Control product quality and handle safety,
operational, and environmental constraints
Fix a flow in every recycle loop and control
inventories
19Plantwide Control Procedure
Fix a flow in every recycle loop and control
inventories
20Plantwide Control Procedure
Check component balances
21Plantwide Control Procedure
Check component balances
Used palm oil
Methanol
Sulfuric acid
22Plantwide Control Procedure
Check component balances
Control individual unit operation
Optimize economic and improve dynamic
controllability
23Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Results and discussion
24Disturbance test
The control structure of Biodiesel production
process
25Disturbance test
Increase heat load disturbance of hot stream
26Disturbance test
Change in feedstock before inlet reactor
27Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Conclusions
28Conclusions
- The control structure of this process can control
purity of Biodiesel product greater than
99.65wt. and glycerine by-product greater than
92wt. (ASTM specifications) - The control structure can control to achieve the
control objective then change in load disturbance
and change in feedstock before inlet reactor for
transesterification.
29THANK YOU FOR YOUR ATTENTION