HCN
Precursor to acrylics, nylon, and specialty chemicals
Molecular Structure
Molecular Details
| Molecular Formula | HCN |
| Molecular Weight | 27.03 g/mol |
| State | Liquid/Gas at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Methane (Feedstock), Ammonia, Oxygen (Feedstock)
➡️ Outputs (Products): Adiponitrile, Acetone Cyanohydrin (MMA), Sodium Cyanide
Chemistry & Engineering
| Reaction Equation | CH₄ + NH₃ + 1.5 O₂ → HCN + 3H₂O (Andrussow) |
| Thermodynamics | Exothermic (Andrussow) vs Endothermic (BMA) |
| Catalyst System | Pt-Rh gauze |
| Reactor Class | Combustion gauze reactor |
| Process Considerations | Extreme toxicity. On-site immediate consumption. |
Extraterrestrial Production Pattern
- Andrussow: CH₄ + NH₃ + O₂ → HCN + H₂O (Pt-Rh catalyst)
- BMA process: CH₄ + NH₃ → HCN + H₂ (no oxygen)
- Operating at 1000-1200°C
- Rapid quenching to prevent decomposition
Applications
- Methyl methacrylate (acetone cyanohydrin route)
- Adiponitrile for nylon 6,6
- Sodium cyanide for gold extraction
- Chelating agents (EDTA)
Reaction Diagram
Overall Reaction: CH4 + NH3 -> HCN + 3H2 (Andrussow process)
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Feed Mixing | Mix CH₄, NH₃, and air in proper ratios |
| 2 | Andrussow Reaction | Pt-Rh gauze at 1000-1200°C |
| 3 | Quenching | Rapid quench to prevent decomposition |
| 4 | Absorption | Absorb HCN in water or NaOH |
| 5 | Stripping | Strip HCN from absorbent |
| 6 | Stabilization | Add H₂SO₄ stabilizer for storage |
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 Hydrogen Cyanide -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="HCN_ANDRUSSOW_CELL">
<Description>Process cell for Hydrogen Cyanide production</Description>
<Unit ID="HCN_ANDRUSSOW">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="MIXER">
<Description>Mixer</Description>
</EquipmentModule>
<EquipmentModule ID="REACTOR">
<Description>Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="QUENCHER">
<Description>Quencher</Description>
</EquipmentModule>
<EquipmentModule ID="ABSORBER">
<Description>Absorber</Description>
</EquipmentModule>
<EquipmentModule ID="STRIPPER">
<Description>Stripper</Description>
</EquipmentModule>
<EquipmentModule ID="STORAGE">
<Description>Storage</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="HCN_ANDRUSSOW_RECIPE">
<Description>Master recipe for Hydrogen Cyanide</Description>
<ProductID>HYDROGEN_CYANIDE</ProductID>
<UnitProcedure ID="HCN_ANDRUSSOW_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="QUENCH">
<Description>Quench 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="ABSORB">
<Description>Absorb 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="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_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.