Cl₂
Disinfectant and key reagent for chlorinated compounds
Molecular Structure
Molecular Details
| Molecular Formula | Cl₂ |
| Molecular Weight | 70.90 g/mol |
| State | Gas at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Sodium Chloride (Feedstock)
➡️ Outputs (Products): Vinyl Chloride, Phosgene, Epichlorohydrin, Hydrogen Chloride, Methyl Chloride
Chemistry & Engineering
| Reaction Equation | 2NaCl + 2H₂O → Cl₂ + H₂ + 2NaOH |
| Thermodynamics | Electrolysis (Electrical Energy input) |
| Catalyst System | Dimensionally Stable Anodes (DSA) |
| Reactor Class | Membrane Cell Electrolyzer |
| Process Considerations | Energy intensive (approx 2500 kWh/ton). Co-produces Caustic Soda. |
Extraterrestrial Production Pattern
- Electrolysis of NaCl brine (membrane or diaphragm cell)
- Anode reaction: 2Cl⁻ → Cl₂ + 2e⁻
- Collection and compression of chlorine gas
- Liquefaction for storage and transport
Applications
- Water and wastewater disinfection
- PVC production (via EDC and VCM)
- Bleaching agents (hypochlorite)
- Chlorinated solvents
Reaction Diagram
Overall Reaction: 2NaCl + 2H2O -> Cl2 + 2NaOH + H2
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Brine Preparation | Dissolve NaCl to saturation, remove Ca/Mg |
| 2 | Electrolysis | Membrane cell at 2-4 V, 3-5 kA/m² |
| 3 | Chlorine Drying | Dry Cl₂ with H₂SO₄ |
| 4 | Compression | Compress Cl₂ for liquefaction |
| 5 | Liquefaction | Cool to -35°C at 6-8 bar |
| 6 | Hydrogen Treatment | Purify H₂ for sale or fuel |
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 Chlorine -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="CHLOR_ALKALI_CELL">
<Description>Process cell for Chlorine production</Description>
<Unit ID="CHLOR_ALKALI">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="BRINE_TANK">
<Description>Brine Tank</Description>
</EquipmentModule>
<EquipmentModule ID="ELECTROLYZER">
<Description>Electrolyzer</Description>
</EquipmentModule>
<EquipmentModule ID="DRYER">
<Description>Dryer</Description>
</EquipmentModule>
<EquipmentModule ID="COMPRESSOR">
<Description>Compressor</Description>
</EquipmentModule>
<EquipmentModule ID="CONDENSER">
<Description>Condenser</Description>
</EquipmentModule>
<EquipmentModule ID="H2_PURIFIER">
<Description>H2 Purifier</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="CHLOR_ALKALI_RECIPE">
<Description>Master recipe for Chlorine</Description>
<ProductID>CHLORINE</ProductID>
<UnitProcedure ID="CHLOR_ALKALI_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="BRINE_PREP">
<Description>Brine Prep 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="ELECTROLYZE">
<Description>Electrolyze 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="DRY">
<Description>Dry 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="COMPRESS">
<Description>Compress 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="LIQUEFY">
<Description>Liquefy 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="H2_TREATMENT">
<Description>H2 Treatment 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.