H₂N(CH₂)₆NH₂
Co-monomer for nylon 6,6
Molecular Structure
Molecular Details
| Molecular Formula | H₂N(CH₂)₆NH₂ |
| Molecular Weight | 116.21 g/mol |
| State | Solid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Adiponitrile
➡️ Outputs (Products): Nylon 6,6, Isocyanates
Chemistry & Engineering
| Reaction Equation | NC(CH₂)₄CN + 4H₂ → H₂N(CH₂)₆NH₂ |
| Thermodynamics | Exothermic hydrogenation |
| Catalyst System | Raney Nickel or Cobalt |
| Reactor Class | High pressure trickle bed |
| Process Considerations | Intermediate for the strongest nylon polymer. |
Extraterrestrial Production Pattern
- Butadiene hydrocyanation → adiponitrile (Invista process)
- Alternative: acrylonitrile electrodimerization
- Adiponitrile hydrogenation over Raney Ni or Co catalyst
- Distillation under reduced pressure
Applications
- Nylon 6,6 production
- Epoxy curing agents
- Corrosion inhibitors
- Chelating agents
Reaction Diagram
Overall Reaction: NC(CH2)4CN + 4H2 -> H2N(CH2)6NH2
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Adiponitrile Feed | Pump ADN to hydrogenation reactor |
| 2 | Catalytic Hydrogenation | Co or Ni catalyst at 100-150°C, 30 bar |
| 3 | Ammonia Removal | Strip NH₃ from crude product |
| 4 | Distillation | Vacuum distillation for purification |
| 5 | Stabilization | Add antioxidant for stability |
| 6 | Handling | Handle under nitrogen due to reactivity |
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 Hexamethylenediamine -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="HMDA_PLANT_CELL">
<Description>Process cell for Hexamethylenediamine production</Description>
<Unit ID="HMDA_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="PUMP">
<Description>Pump</Description>
</EquipmentModule>
<EquipmentModule ID="HYDROGENATOR">
<Description>Hydrogenator</Description>
</EquipmentModule>
<EquipmentModule ID="STRIPPER">
<Description>Stripper</Description>
</EquipmentModule>
<EquipmentModule ID="VACUUM_COLUMN">
<Description>Vacuum Column</Description>
</EquipmentModule>
<EquipmentModule ID="STABILIZER">
<Description>Stabilizer</Description>
</EquipmentModule>
<EquipmentModule ID="PACKAGING">
<Description>Packaging</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="HMDA_PLANT_RECIPE">
<Description>Master recipe for Hexamethylenediamine</Description>
<ProductID>HEXAMETHYLENEDIAMINE</ProductID>
<UnitProcedure ID="HMDA_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="HYDROGENATE">
<Description>Hydrogenate 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="STRIP_NH3">
<Description>Strip Nh3 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="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>
<Operation ID="OP_06">
<Description>Operation 6</Description>
<Phase ID="HANDLE">
<Description>Handle 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.