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Supported by:
Aspen HYSYS Training
Final Exercise: Methanol Process
Tutor:
M. Ersharry Yunashtanto
Zayyanatun Zulfa
Ikha Muliawati
Mada Harahap
Flowsheet
• Components: CO2, Hydrogen, Methanol, H2O
• Fluid Packages: SRK
• Reaction: CO2 + 3 H2 ↔ CH3OH+ H2O
• Reaction Type: Kinetic
• Reaction Phase: Vapour Phase
• Forward Reaction Parameter: A: 1.04e22 ; E: 1.7e5
• Reverse Reaction Parameter: A’: 2.6e28 ; E’: 2.2e5
Components and Reaction
Components and Reaction
Equipment and Stream Data
Composition:
CO2 : 0.25 (mole fraction)
H2 : 0.75 (mole fraction)
Condition:
Temperature: 40 °C
Pressure: 4000 kPa
Mass Flow: 1000 kg/h
Composition:
CO2 : 0.25 (mole fraction)
H2 : 0.75 (mole fraction)
Condition:
Temperature: 40 °C
Pressure: 4000 kPa
Molar Flow: 200 kgmole/h
T: 200 °C
∆P: 50 kPa
Defined the reaction
Diameter: 10 m
Height: 10 m
∆P: 50 kPa
T: 200 °C T: 40 °C
Molar Flow: 200 kgmole/hP: 4000 kPa
Thank You
M. Ersharry Yunashtanto
Zayyanatun Zulfa
Ikha Muliawati
Mada Harahap

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Final Exercise - Methanol Process

  • 1. Supported by: Aspen HYSYS Training Final Exercise: Methanol Process Tutor: M. Ersharry Yunashtanto Zayyanatun Zulfa Ikha Muliawati Mada Harahap
  • 3. • Components: CO2, Hydrogen, Methanol, H2O • Fluid Packages: SRK • Reaction: CO2 + 3 H2 ↔ CH3OH+ H2O • Reaction Type: Kinetic • Reaction Phase: Vapour Phase • Forward Reaction Parameter: A: 1.04e22 ; E: 1.7e5 • Reverse Reaction Parameter: A’: 2.6e28 ; E’: 2.2e5 Components and Reaction
  • 5. Equipment and Stream Data Composition: CO2 : 0.25 (mole fraction) H2 : 0.75 (mole fraction) Condition: Temperature: 40 °C Pressure: 4000 kPa Mass Flow: 1000 kg/h Composition: CO2 : 0.25 (mole fraction) H2 : 0.75 (mole fraction) Condition: Temperature: 40 °C Pressure: 4000 kPa Molar Flow: 200 kgmole/h T: 200 °C ∆P: 50 kPa Defined the reaction Diameter: 10 m Height: 10 m ∆P: 50 kPa T: 200 °C T: 40 °C Molar Flow: 200 kgmole/hP: 4000 kPa
  • 6. Thank You M. Ersharry Yunashtanto Zayyanatun Zulfa Ikha Muliawati Mada Harahap