C₃H₆O
Intermediate for polyurethanes and propylene glycol
Molecular Structure
Molecular Details
| Molecular Formula | C₃H₆O |
| Molecular Weight | 58.08 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Propylene, Hydrogen Peroxide
➡️ Outputs (Products): Propylene Glycol, Polyols
Chemistry & Engineering
| Reaction Equation | Propylene + H₂O₂ → PO + H₂O (HPPO Process) |
| Thermodynamics | Exothermic |
| Catalyst System | Titanium Silicalite-1 (TS-1) |
| Reactor Class | Fixed bed or Slurry |
| Process Considerations | Avoids chorine/waste of older chlorohydrin process. Ideal for closed loops. |
Extraterrestrial Production Pattern
- HPPO process: propylene + H₂O₂ over TS-1 zeolite
- PO/SM process: ethylbenzene hydroperoxide route
- Chlorohydrin process (older, more waste)
- Distillation for purification
Applications
- Polyether polyols for polyurethanes
- Propylene glycol production
- Polyester resins
- Solvent and fuel additive
Reaction Diagram
Overall Reaction: C3H6 + H2O2 -> C3H6O + H2O (HPPO process)
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Propylene/H₂O₂ Feed | Mix propylene with H₂O₂ in methanol |
| 2 | Epoxidation | TS-1 zeolite catalyst at 40-60°C |
| 3 | PO Separation | Distill PO from methanol/water |
| 4 | Methanol Recovery | Recover and recycle methanol |
| 5 | PO Purification | Distill to >99.9% PO |
| 6 | Propylene Recycle | Return unreacted propylene |
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 Oxide -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="PO_HPPO_PLANT_CELL">
<Description>Process cell for Propylene Oxide production</Description>
<Unit ID="PO_HPPO_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="MIXER">
<Description>Mixer</Description>
</EquipmentModule>
<EquipmentModule ID="REACTOR">
<Description>Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="PO_COLUMN">
<Description>Po Column</Description>
</EquipmentModule>
<EquipmentModule ID="MEOH_COLUMN">
<Description>Meoh Column</Description>
</EquipmentModule>
<EquipmentModule ID="PURIFICATION">
<Description>Purification</Description>
</EquipmentModule>
<EquipmentModule ID="RECYCLE_SYSTEM">
<Description>Recycle System</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="PO_HPPO_PLANT_RECIPE">
<Description>Master recipe for Propylene Oxide</Description>
<ProductID>PROPYLENE_OXIDE</ProductID>
<UnitProcedure ID="PO_HPPO_PLANT_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="FEED">
<Description>Feed 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="EPOXIDIZE">
<Description>Epoxidize 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="SEPARATE_PO">
<Description>Separate Po 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="RECOVER_MEOH">
<Description>Recover Meoh 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="PURIFY">
<Description>Purify 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="RECYCLE">
<Description>Recycle 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.