C₈H₈ (C₆H₅CH=CH₂)
Monomer for polystyrene and styrenic copolymers
Molecular Structure
Molecular Details
| Molecular Formula | C₈H₈ (C₆H₅CH=CH₂) |
| Molecular Weight | 104.15 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Ethylbenzene
➡️ Outputs (Products): Polystyrene, Synthetic Rubber, ABS
Chemistry & Engineering
| Reaction Equation | C₆H₅C₂H₅ → C₆H₅C₂H₃ + H₂ |
| Thermodynamics | Highly endothermic (ΔH = +125 kJ/mol) |
| Catalyst System | Iron oxide promoted with Potassium (Fe2O3-K2CO3) |
| Reactor Class | Adiabatic radial flow reactors in series with interstage heating (steam superheating) |
| Process Considerations | Vacuum operation favored to shift equilibrium. Steam prevents coking and supplies heat. |
Extraterrestrial Production Pattern
- Alkylation of benzene with ethylene → ethylbenzene
- Catalytic dehydrogenation at 600-650°C over Fe₂O₃/K₂O catalyst
- Steam dilution to shift equilibrium and prevent coking
- Vacuum distillation with polymerization inhibitor
Applications
- Polystyrene (packaging, insulation)
- ABS and SAN plastics
- Styrene-butadiene rubber
- Unsaturated polyester resins
Reaction Diagram
Overall Reaction: C6H5C2H5 -> C6H5CH=CH2 + H2
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Ethylbenzene Preheat | Heat EB feed to 550°C with steam |
| 2 | Dehydrogenation | Adiabatic reactor with Fe₂O₃/K₂O catalyst |
| 3 | Heat Recovery | Cool effluent against feed |
| 4 | Condensation | Condense styrene and separate from H₂ |
| 5 | Vacuum Distillation | Distill at 50-100 mbar to avoid polymerization |
| 6 | Inhibitor Addition | Add TBC inhibitor for storage stability |
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 Styrene -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="STYRENE_PLANT_CELL">
<Description>Process cell for Styrene production</Description>
<Unit ID="STYRENE_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="PREHEATER">
<Description>Preheater</Description>
</EquipmentModule>
<EquipmentModule ID="REACTOR">
<Description>Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="EXCHANGER">
<Description>Exchanger</Description>
</EquipmentModule>
<EquipmentModule ID="CONDENSER">
<Description>Condenser</Description>
</EquipmentModule>
<EquipmentModule ID="VACUUM_COLUMN">
<Description>Vacuum Column</Description>
</EquipmentModule>
<EquipmentModule ID="INHIBITOR_SYSTEM">
<Description>Inhibitor System</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="STYRENE_PLANT_RECIPE">
<Description>Master recipe for Styrene</Description>
<ProductID>STYRENE</ProductID>
<UnitProcedure ID="STYRENE_PLANT_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="PREHEAT">
<Description>Preheat 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="DEHYDROGENATE">
<Description>Dehydrogenate 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_HEAT">
<Description>Recover Heat 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="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.