C₂H₅OH
Solvent, fuel, and chemical intermediate
Molecular Structure
Molecular Details
| Molecular Formula | C₂H₅OH |
| Molecular Weight | 46.07 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Ethylene, Water (Feedstock)
➡️ Outputs (Products): Ethyl Acetate, Ethylene, Butadiene, Diethyl Ether
Chemistry & Engineering
| Reaction Equation | C₂H₄ + H₂O ⇄ C₂H₅OH |
| Thermodynamics | Exothermic (-45 kJ/mol) |
| Catalyst System | Phosphoric acid on silica support |
| Reactor Class | Fixed bed hydration reactor at 60-70 bar, 300°C |
| Process Considerations | Direct hydration of ethylene is more efficient than fermentation for initial synthetic chemistry loop. |
Extraterrestrial Production Pattern
- Catalytic hydration of ethylene over H₃PO₄/SiO₂ catalyst
- Operating at 300°C and 70 bar pressure
- Alternative: Direct CO₂ + H₂ synthesis over Cu-based catalysts
- Distillation and molecular sieve drying for anhydrous product
Applications
- Solvent for pharmaceuticals and chemicals
- Fuel and fuel additive
- Ethyl acetate production
- Disinfectant and sanitizer
Reaction Diagram
Overall Reaction: C6H12O6 -> 2 C2H5OH + 2 CO2 (fermentation)
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Mashing | Prepare fermentable sugar solution |
| 2 | Fermentation | Yeast fermentation at 30-35°C for 48-72h |
| 3 | Distillation | Beer still to 50% then rectification to 95% |
| 4 | Dehydration | Molecular sieve dehydration to >99.5% |
| 5 | Denaturing | Add denaturant for industrial grade |
| 6 | Storage | Store in SS or lined tanks |
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 Ethanol -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="ETHANOL_FERMENTATION_CELL">
<Description>Process cell for Ethanol production</Description>
<Unit ID="ETHANOL_FERMENTATION">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="MASH_TUN">
<Description>Mash Tun</Description>
</EquipmentModule>
<EquipmentModule ID="FERMENTER">
<Description>Fermenter</Description>
</EquipmentModule>
<EquipmentModule ID="DISTILLATION">
<Description>Distillation</Description>
</EquipmentModule>
<EquipmentModule ID="MOLECULAR_SIEVE">
<Description>Molecular Sieve</Description>
</EquipmentModule>
<EquipmentModule ID="BLEND_TANK">
<Description>Blend Tank</Description>
</EquipmentModule>
<EquipmentModule ID="STORAGE">
<Description>Storage</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="ETHANOL_FERMENTATION_RECIPE">
<Description>Master recipe for Ethanol</Description>
<ProductID>ETHANOL</ProductID>
<UnitProcedure ID="ETHANOL_FERMENTATION_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="MASH">
<Description>Mash 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="FERMENT">
<Description>Ferment 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="DISTILL">
<Description>Distill 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="DEHYDRATE">
<Description>Dehydrate 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="DENATURE">
<Description>Denature 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="STORE">
<Description>Store 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.