CH₃CH(OH)CH₂OH
Antifreeze, food additive, and pharmaceutical solvent
Molecular Structure
Molecular Details
| Molecular Formula | CH₃CH(OH)CH₂OH |
| Molecular Weight | 76.09 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Propylene Oxide, Water (Feedstock)
➡️ Outputs (Products): Polyesters, Food Additive
Chemistry & Engineering
| Reaction Equation | C₃H₆O + H₂O → C₃H₈O₂ |
| Thermodynamics | Exothermic hydration |
| Catalyst System | None/Thermal (high pressure) or Acid |
| Reactor Class | Liquid phase hydration reactor |
| Process Considerations | Food-safe antifreeze alternative. |
Extraterrestrial Production Pattern
- Propylene oxide + H₂O → propylene glycol
- Non-catalytic hydrolysis at 150-200°C
- Excess water to minimize dipropylene glycol
- Vacuum distillation for purification
Applications
- Food-grade antifreeze
- Pharmaceutical solvent
- E-cigarette liquid base
- Cosmetics humectant
Reaction Diagram
Overall Reaction: C3H6O + H2O -> CH3CH(OH)CH2OH
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | PO/Water Mixing | Mix propylene oxide with water (15:1 H₂O:PO) |
| 2 | Hydrolysis | Non-catalytic at 150-200°C, 15-20 bar |
| 3 | Dehydration | Multi-effect evaporation |
| 4 | MPG Distillation | Vacuum distill monopropylene glycol |
| 5 | DPG/TPG Recovery | Recover dipropylene and tripropylene glycol |
| 6 | Finishing | Final purification for USP grade |
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 Glycol -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="PG_PLANT_CELL">
<Description>Process cell for Propylene Glycol production</Description>
<Unit ID="PG_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="MIXER">
<Description>Mixer</Description>
</EquipmentModule>
<EquipmentModule ID="REACTOR">
<Description>Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="EVAPORATOR">
<Description>Evaporator</Description>
</EquipmentModule>
<EquipmentModule ID="MPG_COLUMN">
<Description>Mpg Column</Description>
</EquipmentModule>
<EquipmentModule ID="DPG_COLUMN">
<Description>Dpg Column</Description>
</EquipmentModule>
<EquipmentModule ID="FINISHING">
<Description>Finishing</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="PG_PLANT_RECIPE">
<Description>Master recipe for Propylene Glycol</Description>
<ProductID>PROPYLENE_GLYCOL</ProductID>
<UnitProcedure ID="PG_PLANT_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="MIX">
<Description>Mix 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="HYDROLYZE">
<Description>Hydrolyze 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="EVAPORATE">
<Description>Evaporate 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="DISTILL_MPG">
<Description>Distill Mpg 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="RECOVER_DPG">
<Description>Recover Dpg 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="FINISH">
<Description>Finish 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.