C₃H₆
Second most important olefin, precursor to polypropylene and acrylics
Molecular Structure
Molecular Details
| Molecular Formula | C₃H₆ |
| Molecular Weight | 42.08 g/mol |
| State | Gas at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Methanol
➡️ Outputs (Products): Polypropylene, Propylene Oxide, Acrylonitrile, Acrylic Acid, Cumene, Isopropanol, Butanol
Chemistry & Engineering
| Reaction Equation | 3CH₃OH → C₃H₆ + 3H₂O |
| Thermodynamics | Exothermic overall from methanol (-50 kJ/mol) |
| Catalyst System | SAPO-34 (small pore zeolite) maximizes propylene selectivity |
| Reactor Class | Fluidized bed reactor (400-500°C) with continuous catalyst regeneration |
| Process Considerations | Primary byproduct of MTO process. Ratio of C2:C3 can be tuned by catalyst acidity and temperature. |
Extraterrestrial Production Pattern
- Produce methanol from CO₂ + H₂
- MTO conversion over zeolite catalyst (ZSM-5 or SAPO-34)
- Separation and purification of propylene fraction
- Alternative: Direct FT synthesis with selective catalysts
Applications
- Polypropylene production
- Propylene oxide
- Acrylonitrile synthesis
- Cumene and phenol production
Reaction Diagram
Overall Reaction: CH3OH -> C3H6 + H2O (MTO)
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Methanol Vaporization | Vaporize liquid methanol feed |
| 2 | MTO Reaction | Fluidized-bed reactor with SAPO-34 zeolite at 450-550°C |
| 3 | Quenching | Cool reactor effluent with water spray |
| 4 | Compression | Compress product gas |
| 5 | Separation | Cryogenic separation of C₂/C₃ olefins |
| 6 | C3 Splitter | Separate propylene from propane |
S88 Batch Control Model
This module follows the ISA-88 (S88) batch control standard. Below is a simplified BatchML schema for educational purposes:
<?xml version="1.0" encoding="UTF-8"?>
<!-- ISA-88 Batch Control Model for Propylene -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="PROPYLENE_MTO_CELL">
<Description>Process cell for Propylene production</Description>
<Unit ID="PROPYLENE_MTO">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="VAPORIZER">
<Description>Vaporizer</Description>
</EquipmentModule>
<EquipmentModule ID="REACTOR">
<Description>Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="QUENCH_TOWER">
<Description>Quench Tower</Description>
</EquipmentModule>
<EquipmentModule ID="COMPRESSOR">
<Description>Compressor</Description>
</EquipmentModule>
<EquipmentModule ID="COLD_BOX">
<Description>Cold Box</Description>
</EquipmentModule>
<EquipmentModule ID="SPLITTER">
<Description>Splitter</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="PROPYLENE_MTO_RECIPE">
<Description>Master recipe for Propylene</Description>
<ProductID>PROPYLENE</ProductID>
<UnitProcedure ID="PROPYLENE_MTO_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="VAPORIZE">
<Description>Vaporize phase</Description>
<PhaseLogic>
<Step ID="STEP_1"><Action>Initialize</Action></Step>
<Step ID="STEP_2"><Action>Execute</Action></Step>
<Step ID="STEP_3"><Action>Complete</Action></Step>
</PhaseLogic>
</Phase>
</Operation>
<Operation ID="OP_02">
<Description>Operation 2</Description>
<Phase ID="REACT">
<Description>React phase</Description>
<PhaseLogic>
<Step ID="STEP_1"><Action>Initialize</Action></Step>
<Step ID="STEP_2"><Action>Execute</Action></Step>
<Step ID="STEP_3"><Action>Complete</Action></Step>
</PhaseLogic>
</Phase>
</Operation>
<Operation ID="OP_03">
<Description>Operation 3</Description>
<Phase ID="QUENCH">
<Description>Quench phase</Description>
<PhaseLogic>
<Step ID="STEP_1"><Action>Initialize</Action></Step>
<Step ID="STEP_2"><Action>Execute</Action></Step>
<Step ID="STEP_3"><Action>Complete</Action></Step>
</PhaseLogic>
</Phase>
</Operation>
<Operation ID="OP_04">
<Description>Operation 4</Description>
<Phase ID="COMPRESS">
<Description>Compress phase</Description>
<PhaseLogic>
<Step ID="STEP_1"><Action>Initialize</Action></Step>
<Step ID="STEP_2"><Action>Execute</Action></Step>
<Step ID="STEP_3"><Action>Complete</Action></Step>
</PhaseLogic>
</Phase>
</Operation>
<Operation ID="OP_05">
<Description>Operation 5</Description>
<Phase ID="SEPARATE">
<Description>Separate phase</Description>
<PhaseLogic>
<Step ID="STEP_1"><Action>Initialize</Action></Step>
<Step ID="STEP_2"><Action>Execute</Action></Step>
<Step ID="STEP_3"><Action>Complete</Action></Step>
</PhaseLogic>
</Phase>
</Operation>
<Operation ID="OP_06">
<Description>Operation 6</Description>
<Phase ID="SPLIT">
<Description>Split phase</Description>
<PhaseLogic>
<Step ID="STEP_1"><Action>Initialize</Action></Step>
<Step ID="STEP_2"><Action>Execute</Action></Step>
<Step ID="STEP_3"><Action>Complete</Action></Step>
</PhaseLogic>
</Phase>
</Operation>
</UnitProcedure>
</MasterRecipe>
</BatchML>
**Key S88 Concepts:**
- **Process Cell**: The physical grouping containing all equipment for this process
- **Unit**: The major equipment that performs the synthesis
- **Equipment Modules**: Individual pieces of equipment (reactors, columns, etc.)
- **Unit Procedure**: The sequence of operations to produce the product
- **Phases**: The lowest level of procedural control (e.g., REACT, SEPARATE, PURIFY)
Key S88 Concepts:
• Process Cell: Physical grouping containing all equipment
• Unit: Major equipment performing synthesis
• Equipment Modules: Individual pieces (reactors, columns, etc.)
• Phases: Lowest level of procedural control (REACT, SEPARATE, etc.)
This Synthesis Module is part of the 100chemicals Olefinverbund — an integrated chemical production network designed for extraterrestrial civilization on Moon and Mars.