CH₃COOCH=CH₂
Monomer for PVA, adhesives, and coatings
Molecular Structure
Molecular Details
| Molecular Formula | CH₃COOCH=CH₂ |
| Molecular Weight | 86.09 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Ethylene, Acetic Acid, Oxygen (Feedstock)
➡️ Outputs (Products): PVA, Emulsions
Chemistry & Engineering
| Reaction Equation | C₂H₄ + CH₃COOH + 0.5 O₂ → VAM + H₂O |
| Thermodynamics | Exothermic acetoxylation |
| Catalyst System | Palladium-Gold on Silica |
| Reactor Class | Fixed bed gas phase |
| Process Considerations | Critical monomer for adhesives. |
Extraterrestrial Production Pattern
- Gas-phase reaction: ethylene + acetic acid + O₂
- Pd/Au on silica catalyst at 150-200°C
- Fixed-bed reactor with steam dilution
- Distillation and inhibitor addition
Applications
- Polyvinyl acetate (PVA) adhesives
- Polyvinyl alcohol (PVOH) films
- Ethylene-vinyl acetate (EVA) copolymers
- Coatings and paints
Reaction Diagram
Overall Reaction: C2H4 + CH3COOH + 1/2 O2 -> CH3COOCH=CH2 + H2O
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Feed Mixing | Mix ethylene, acetic acid, and oxygen |
| 2 | Oxidative Acetoxylation | Pd catalyst at 150-200°C, 5-10 bar |
| 3 | Separation | Separate VAM from reactor effluent |
| 4 | Acetic Acid Recovery | Recover unreacted acetic acid |
| 5 | Distillation | Distill to >99.9% VAM |
| 6 | Stabilization | Add hydroquinone inhibitor |
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 Vinyl Acetate -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="VAM_PLANT_CELL">
<Description>Process cell for Vinyl Acetate production</Description>
<Unit ID="VAM_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="MIXER">
<Description>Mixer</Description>
</EquipmentModule>
<EquipmentModule ID="REACTOR">
<Description>Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="SEPARATOR">
<Description>Separator</Description>
</EquipmentModule>
<EquipmentModule ID="AA_COLUMN">
<Description>Aa Column</Description>
</EquipmentModule>
<EquipmentModule ID="VAM_COLUMN">
<Description>Vam Column</Description>
</EquipmentModule>
<EquipmentModule ID="INHIBITOR_SYSTEM">
<Description>Inhibitor System</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="VAM_PLANT_RECIPE">
<Description>Master recipe for Vinyl Acetate</Description>
<ProductID>VINYL_ACETATE</ProductID>
<UnitProcedure ID="VAM_PLANT_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="MIX">
<Description>Mix 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="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_03">
<Description>Operation 3</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_04">
<Description>Operation 4</Description>
<Phase ID="RECOVER_AA">
<Description>Recover Aa 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="STABILIZE">
<Description>Stabilize 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.