C₄H₉OH
Solvent and plasticizer alcohol
Molecular Structure
Molecular Details
| Molecular Formula | C₄H₉OH |
| Molecular Weight | 74.12 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Propylene, Carbon Monoxide, Hydrogen (Feedstock)
➡️ Outputs (Products): Butyl Acetate, Solvent
Chemistry & Engineering
| Reaction Equation | Propylene + CO + H₂ → Butyraldehyde → Butanol (Oxo Process) |
| Thermodynamics | Hydroformylation is exothermic |
| Catalyst System | Rhodium-phosphine complex (highly active/selective) |
| Reactor Class | Stirred tank or bubble column (liquid phase) |
| Process Considerations | Requires Syngas (CO/H2). Alternative: ABE fermentation if biomass is available. |
Extraterrestrial Production Pattern
- Hydroformylation of propylene with syngas (CO + H₂)
- Cobalt or rhodium catalyst at 100-200°C
- Hydrogenation of butyraldehyde intermediate
- Distillation to separate n-butanol and isobutanol
Applications
- Solvent for paints and coatings
- Plasticizer alcohols (2-EH via aldol)
- Butyl acrylate production
- Fuel additive
Reaction Diagram
Overall Reaction: CO + 2H2 + C3H6 -> C4H9OH
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Propylene Feed | Purify and compress propylene |
| 2 | Hydroformylation | Co or Rh catalyst at 100-180°C, 20-30 bar → butyraldehyde |
| 3 | Catalyst Separation | Recover catalyst from aldehyde product |
| 4 | Hydrogenation | Reduce aldehyde to alcohol with Ni catalyst |
| 5 | Distillation | Separate n-butanol from iso-butanol |
| 6 | Dehydration | Remove water by azeotropic distillation |
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 Butanol -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="BUTANOL_OXO_CELL">
<Description>Process cell for Butanol production</Description>
<Unit ID="BUTANOL_OXO">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="COMPRESSOR">
<Description>Compressor</Description>
</EquipmentModule>
<EquipmentModule ID="OXO_REACTOR">
<Description>Oxo Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="SEPARATOR">
<Description>Separator</Description>
</EquipmentModule>
<EquipmentModule ID="HYDROGENATOR">
<Description>Hydrogenator</Description>
</EquipmentModule>
<EquipmentModule ID="COLUMN">
<Description>Column</Description>
</EquipmentModule>
<EquipmentModule ID="DEHYDRATOR">
<Description>Dehydrator</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="BUTANOL_OXO_RECIPE">
<Description>Master recipe for Butanol</Description>
<ProductID>BUTANOL</ProductID>
<UnitProcedure ID="BUTANOL_OXO_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="HYDROFORMYLATE">
<Description>Hydroformylate 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="RECOVER_CAT">
<Description>Recover Cat 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="HYDROGENATE">
<Description>Hydrogenate 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="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>
</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.