C₂H₅OC₂H₅
Solvent and extraction medium
Molecular Structure
Molecular Details
| Molecular Formula | C₂H₅OC₂H₅ |
| Molecular Weight | 74.12 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Ethanol
➡️ Outputs (Products): Solvent
Chemistry & Engineering
| Reaction Equation | 2 C₂H₅OH → (C₂H₅)₂O + H₂O |
| Thermodynamics | Endothermic dehydration |
| Catalyst System | Sulfuric acid or Alumina |
| Reactor Class | Dehydration reactor |
| Process Considerations | Historical anesthetic; byproduct of ethanol hydration. |
Extraterrestrial Production Pattern
- Ethanol dehydration over H₂SO₄ or solid acid at 140°C
- Vapor-phase process over Al₂O₃ catalyst
- Distillation and drying
- Peroxide inhibitor addition for storage
Applications
- Laboratory solvent
- Extraction medium
- Starting fluid for engines
- Historical anesthetic
Reaction Diagram
Overall Reaction: 2 C2H5OH -> (C2H5)2O + H2O
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Ethanol Feed | Pump ethanol to dehydration reactor |
| 2 | Dehydration | Al₂O₃ or H₂SO₄ catalyst at 130-140°C |
| 3 | Neutralization | Neutralize residual acid if used |
| 4 | Water Separation | Phase separate or distill water |
| 5 | Ether Distillation | Distill to >99.5% ether |
| 6 | Peroxide Removal | Remove peroxides before storage |
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 Diethyl Ether -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="DIETHYL_ETHER_PLANT_CELL">
<Description>Process cell for Diethyl Ether production</Description>
<Unit ID="DIETHYL_ETHER_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="PUMP">
<Description>Pump</Description>
</EquipmentModule>
<EquipmentModule ID="REACTOR">
<Description>Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="NEUTRALIZER">
<Description>Neutralizer</Description>
</EquipmentModule>
<EquipmentModule ID="DECANTER">
<Description>Decanter</Description>
</EquipmentModule>
<EquipmentModule ID="COLUMN">
<Description>Column</Description>
</EquipmentModule>
<EquipmentModule ID="TREATMENT_SYSTEM">
<Description>Treatment System</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="DIETHYL_ETHER_PLANT_RECIPE">
<Description>Master recipe for Diethyl Ether</Description>
<ProductID>DIETHYL_ETHER</ProductID>
<UnitProcedure ID="DIETHYL_ETHER_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="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_03">
<Description>Operation 3</Description>
<Phase ID="NEUTRALIZE">
<Description>Neutralize 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="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_05">
<Description>Operation 5</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_06">
<Description>Operation 6</Description>
<Phase ID="TREAT">
<Description>Treat 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.