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Prepregs Honeycomb

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Department of Chemical Engineering. Faculty of Engineering, Chulalongkorn University ... Prepare waste cooking oil and other chemical. Transesterification ... – PowerPoint PPT presentation

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Title: Prepregs Honeycomb


1
Plantwide 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
2
Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ? Conclusions
? Introduction
3
(No Transcript)
4
Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Theory
5
Transesterification
Biodiesel
Catalyst
Vegetable oil or Animal fat
Alcohol
Glycerol
6
Effect of Alkali-Catalyst
7
Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Biodiesel plant
8
Biodiesel Production
Prepare waste cooking oil and other chemical
Transesterification
Separate Biodiesel from Glycerol
Catalyst Removal
Biodiesel Purification
Glycerine Purification
9
Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Steady State Simulation
10
Biodiesel Production
Mixing
Transesterification
Biodiesel Purification
Water Washing
Acid Removal
Recycle Methanol
Heat Exchanger
Methanol Recovery
Glycerol Purification
CaO H2SO4 ? CaSO4 H2O
11
Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Dynamic State Simulation
12
Plantwide Control Procedure
Luyben Tyreus 1998
Establish control objectives
Determine control degrees of freedom
Establish energy management system
13
Plantwide Control Procedure
Establish energy management system
14
Plantwide Control Procedure
Set production rate
15
Plantwide Control Procedure
Set production rate
16
Plantwide Control Procedure
Set production rate
Control product quality and handle safety,
operational, and environmental constraints
17
Plantwide Control Procedure
Control product quality
18
Plantwide 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
19
Plantwide Control Procedure
Fix a flow in every recycle loop and control
inventories
20
Plantwide Control Procedure
Check component balances
21
Plantwide Control Procedure
Check component balances
Used palm oil
Methanol
Sulfuric acid
22
Plantwide Control Procedure
Check component balances
Control individual unit operation
Optimize economic and improve dynamic
controllability
23
Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Results and discussion
24
Disturbance test
The control structure of Biodiesel production
process
25
Disturbance test

Increase heat load disturbance of hot stream


26
Disturbance test

Change in feedstock before inlet reactor



27
Outline
? Introduction ? Theory ? Biodiesel plant ?
Steady State Simulation ? Dynamic State
Simulation ? Results and discussion ?
Conclusions
? Conclusions
28
Conclusions
  • 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.

29
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