C₇H₈ (C₆H₅CH₃)
Solvent and precursor to TNT, polyurethanes, and other chemicals
Molecular Structure
Molecular Details
| Molecular Formula | C₇H₈ (C₆H₅CH₃) |
| Molecular Weight | 92.14 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Benzene, Methanol
➡️ Outputs (Products): Toluene Diisocyanate, Benzene, Xylene, TNT
Chemistry & Engineering
| Reaction Equation | C₆H₆ + CH₃OH → C₆H₅CH₃ + H₂O (Alkylation) |
| Thermodynamics | Exothermic alkylation |
| Catalyst System | Zeolite Y or ZSM-5 |
| Reactor Class | Liquid phase or vapor phase alkylation reactor |
| Process Considerations | Often produced in equilibrium with Benzene and Xylenes (BTX) in converting methanol/naphtha. |
Extraterrestrial Production Pattern
- Catalytic reforming of naphtha-range FT products
- Separation by extractive distillation
- Alternative: Alkylation of benzene with methanol
- Hydrodealkylation can convert toluene back to benzene
Applications
- Solvent for paints and coatings
- TDI (toluene diisocyanate) for polyurethanes
- Benzoic acid production
- Xylene production via disproportionation
Reaction Diagram
Overall Reaction: Naphtha reforming -> C6H5CH3 (from aromatics)
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Naphtha Hydrotreating | Remove S, N from naphtha |
| 2 | Catalytic Reforming | Pt/Re catalyst at 490-530°C |
| 3 | Aromatics Extraction | Sulfolane or Morpholine extraction |
| 4 | Toluene Column | Distill to separate toluene from benzene/xylenes |
| 5 | Clay Treatment | Remove olefins if needed |
| 6 | Storage | Store in floating-roof tanks |
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 Toluene -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="TOLUENE_EXTRACTION_CELL">
<Description>Process cell for Toluene production</Description>
<Unit ID="TOLUENE_EXTRACTION">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="HYDROTREATER">
<Description>Hydrotreater</Description>
</EquipmentModule>
<EquipmentModule ID="REFORMER">
<Description>Reformer</Description>
</EquipmentModule>
<EquipmentModule ID="EXTRACTOR">
<Description>Extractor</Description>
</EquipmentModule>
<EquipmentModule ID="COLUMN">
<Description>Column</Description>
</EquipmentModule>
<EquipmentModule ID="CLAY_TREATER">
<Description>Clay Treater</Description>
</EquipmentModule>
<EquipmentModule ID="STORAGE">
<Description>Storage</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="TOLUENE_EXTRACTION_RECIPE">
<Description>Master recipe for Toluene</Description>
<ProductID>TOLUENE</ProductID>
<UnitProcedure ID="TOLUENE_EXTRACTION_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="HYDROTREAT">
<Description>Hydrotreat 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="REFORM">
<Description>Reform 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="EXTRACT">
<Description>Extract 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="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_05">
<Description>Operation 5</Description>
<Phase ID="TREAT">
<Description>Treat 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="STORE">
<Description>Store 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.