C₉H₆N₂O₂
Precursor for flexible polyurethane foam
Molecular Structure
Molecular Details
| Molecular Formula | C₉H₆N₂O₂ |
| Molecular Weight | 174.16 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Toluene, Nitric Acid, Phosgene
➡️ Outputs (Products): Polyurethane Foam
Chemistry & Engineering
| Reaction Equation | Nitration -> Hydrogenation -> Phosgenation |
| Thermodynamics | Exothermic steps |
| Catalyst System | Ni (Hydrogenation) |
| Reactor Class | Multiple units |
| Process Considerations | Mixture of 2,4 and 2,6 isomers. |
Extraterrestrial Production Pattern
- Toluene → dinitrotoluene (nitration)
- Dinitrotoluene → toluenediamine (hydrogenation)
- TDA + phosgene → TDI + HCl
- Distillation for isomer separation
Applications
- Flexible polyurethane foam
- Coatings and elastomers
- Adhesives
Reaction Diagram
Overall Reaction: C6H3(CH3)(NH2)2 + 2COCl2 -> C6H3(CH3)(NCO)2 + 4HCl
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | TDA Production | Hydrogenate dinitrotoluene to toluenediamine |
| 2 | Phosgenation | React TDA with phosgene in chlorobenzene |
| 3 | Degassing | Remove HCl and excess phosgene |
| 4 | Solvent Stripping | Strip chlorobenzene solvent |
| 5 | Isomer Separation | Distill to separate 2,4- and 2,6-TDI |
| 6 | Blending | Blend 80/20 or 65/35 isomer ratios |
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 Diisocyanate -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="TDI_PLANT_CELL">
<Description>Process cell for Toluene Diisocyanate production</Description>
<Unit ID="TDI_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="HYDROGENATOR">
<Description>Hydrogenator</Description>
</EquipmentModule>
<EquipmentModule ID="PHOSGENE_REACTOR">
<Description>Phosgene Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="DEGASSER">
<Description>Degasser</Description>
</EquipmentModule>
<EquipmentModule ID="STRIPPER">
<Description>Stripper</Description>
</EquipmentModule>
<EquipmentModule ID="COLUMN">
<Description>Column</Description>
</EquipmentModule>
<EquipmentModule ID="BLENDER">
<Description>Blender</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="TDI_PLANT_RECIPE">
<Description>Master recipe for Toluene Diisocyanate</Description>
<ProductID>TOLUENE_DIISOCYANATE</ProductID>
<UnitProcedure ID="TDI_PLANT_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="TDA_PROD">
<Description>Tda Prod 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="PHOSGENATE">
<Description>Phosgenate 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="DEGAS">
<Description>Degas 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="STRIP">
<Description>Strip 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="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_06">
<Description>Operation 6</Description>
<Phase ID="BLEND">
<Description>Blend 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.