CH₃OH
Solvent, fuel, precursor
Molecular Structure
Molecular Details
| Molecular Formula | CH₃OH |
| Molecular Weight | 32.04 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Carbon Dioxide (Feedstock), Hydrogen (Feedstock)
➡️ Outputs (Products): Formaldehyde, Acetic Acid, Ethylene, Propylene, Dimethyl Ether, Methyl Methacrylate, Methyl Chloride
Chemistry & Engineering
| Reaction Equation | CO₂ + 3H₂ ⇄ CH₃OH + H₂O |
| Thermodynamics | Exothermic (-49 kJ/mol), favored by high pressure, low temp |
| Catalyst System | Cu/ZnO/Al₂O₃ |
| Reactor Class | Gas-cooled tubular reactor or Lurgi tube process at 50-100 bar, 250°C |
| Process Considerations | The ‚Universal Solvent‘ and carbon source for ISRU. Water byproduct must be recycled to electrolysis. |
Extraterrestrial Production Pattern
- Capture CO₂ from Martian atmosphere (95% CO₂) or other sources
- Generate H₂ via water electrolysis
- Catalytic hydrogenation: CO₂ + 3H₂ → CH₃OH + H₂O
- Distillation for purification
Applications
- Fuel and fuel additive
- Formaldehyde production
- Acetic acid synthesis
- Methanol-to-Olefins (MTO) process
- Solvent for chemical processes
Reaction Diagram
Overall Reaction: CO2 + 3H2 -> CH3OH + H2O
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Feed Mixing | Combine CO₂ and H₂ in stoichiometric ratio (1:3) |
| 2 | Compression | Compress mixed feed to 50-100 bar |
| 3 | Catalytic Reaction | Fixed-bed reactor with Cu/ZnO/Al₂O₃ catalyst at 200-300°C |
| 4 | Condensation | Cool reactor effluent to condense methanol and water |
| 5 | Distillation | Separate methanol from water and light ends |
| 6 | Purification | Final distillation to >99.5% methanol purity |
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 Methanol -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="METHANOL_SYNTHESIS_CELL">
<Description>Process cell for Methanol production</Description>
<Unit ID="METHANOL_SYNTHESIS">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="MIXER">
<Description>Mixer</Description>
</EquipmentModule>
<EquipmentModule ID="COMPRESSOR">
<Description>Compressor</Description>
</EquipmentModule>
<EquipmentModule ID="REACTOR">
<Description>Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="CONDENSER">
<Description>Condenser</Description>
</EquipmentModule>
<EquipmentModule ID="DISTILLATION_COLUMN">
<Description>Distillation Column</Description>
</EquipmentModule>
<EquipmentModule ID="STORAGE">
<Description>Storage</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="METHANOL_SYNTHESIS_RECIPE">
<Description>Master recipe for Methanol</Description>
<ProductID>METHANOL</ProductID>
<UnitProcedure ID="METHANOL_SYNTHESIS_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="MIX_FEED">
<Description>Mix 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="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_03">
<Description>Operation 3</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_04">
<Description>Operation 4</Description>
<Phase ID="CONDENSE">
<Description>Condense 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="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>
</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.