CH₃COOH
Fundamental organic acid for vinyl acetate and acetate esters
Molecular Structure
Molecular Details
| Molecular Formula | CH₃COOH |
| Molecular Weight | 60.05 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Methanol, Carbon Monoxide
➡️ Outputs (Products): Vinyl Acetate, Ethyl Acetate, Butyl Acetate, Terephthalic Acid, Cellulose Acetate
Chemistry & Engineering
| Reaction Equation | CH₃OH + CO → CH₃COOH (Cativa Process) |
| Thermodynamics | Exothermic carbonylation |
| Catalyst System | Iridium/Ruthenium (Cativa) or Rhodium (Monsanto) |
| Reactor Class | Stirred tank reactor at 30-60 bar |
| Process Considerations | Corrosive environment requires Hastelloy or Zirconium equipment. |
Extraterrestrial Production Pattern
- Methanol + CO carbonylation over Rh or Ir catalyst
- Operating at 150-200°C and 30-60 bar
- Homogeneous catalysis with iodide promoter
- Distillation and purification
Applications
- Vinyl acetate monomer (VAM)
- Acetate esters (ethyl acetate, butyl acetate)
- Cellulose acetate fibers
- Food preservative (vinegar)
Reaction Diagram
Overall Reaction: CH3OH + CO -> CH3COOH
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Methanol Feed | Pump methanol to reactor pressure (30-60 bar) |
| 2 | CO Compression | Compress carbon monoxide to reaction pressure |
| 3 | Carbonylation | Rh-catalyzed reaction at 150-200°C (Monsanto/Cativa) |
| 4 | Flash Separation | Flash to remove light ends and recycle catalyst |
| 5 | Dehydration | Remove water from crude acetic acid |
| 6 | Purification | Distill to glacial acetic acid (>99.5%) |
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 Acetic Acid -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="ACETIC_ACID_PLANT_CELL">
<Description>Process cell for Acetic Acid production</Description>
<Unit ID="ACETIC_ACID_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="PUMP">
<Description>Pump</Description>
</EquipmentModule>
<EquipmentModule ID="COMPRESSOR">
<Description>Compressor</Description>
</EquipmentModule>
<EquipmentModule ID="REACTOR">
<Description>Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="FLASH_DRUM">
<Description>Flash Drum</Description>
</EquipmentModule>
<EquipmentModule ID="DRYING_COLUMN">
<Description>Drying Column</Description>
</EquipmentModule>
<EquipmentModule ID="PRODUCT_COLUMN">
<Description>Product Column</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="ACETIC_ACID_PLANT_RECIPE">
<Description>Master recipe for Acetic Acid</Description>
<ProductID>ACETIC_ACID</ProductID>
<UnitProcedure ID="ACETIC_ACID_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="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="FLASH">
<Description>Flash 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="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_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.