C₃H₅ClO
Precursor for epoxy resins and glycerol
Molecular Structure
Molecular Details
| Molecular Formula | C₃H₅ClO |
| Molecular Weight | 92.52 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Propylene, Chlorine
➡️ Outputs (Products): Epoxy Resin, Glycerol
Chemistry & Engineering
| Reaction Equation | Allyl Chloride route or Glycerol-to-Epiclorohydrin (GTE) |
| Thermodynamics | Exothermic steps |
| Catalyst System | Carboxylic acid for GTE |
| Reactor Class | Chlorination reactor |
| Process Considerations | GTE route (reverse of historic) possible if glycerol is abundant. |
Extraterrestrial Production Pattern
- Propylene chlorination → allyl chloride
- Allyl chloride + HOCl → dichlorohydrin
- Dehydrochlorination with base → epichlorohydrin
- Alternative: glycerol + HCl (bio-based route)
Applications
- Epoxy resin production
- Synthetic glycerol
- Water treatment chemicals
- Ion exchange resins
Reaction Diagram
Overall Reaction: CH2=CHCH2Cl + HOCl -> ClCH2CH(OH)CH2Cl -> C3H5ClO
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Allyl Chloride Production | Chlorinate propylene at 500°C |
| 2 | Chlorohydrination | React allyl chloride with HOCl |
| 3 | Dehydrochlorination | Ca(OH)₂ treatment to form epoxide ring |
| 4 | Phase Separation | Separate organic from aqueous phase |
| 5 | Distillation | Distill to >99% epichlorohydrin |
| 6 | Waste Treatment | Treat chlorinated byproduct streams |
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 Epichlorohydrin -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="EPICHLOROHYDRIN_PLANT_CELL">
<Description>Process cell for Epichlorohydrin production</Description>
<Unit ID="EPICHLOROHYDRIN_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="CHLORINATOR">
<Description>Chlorinator</Description>
</EquipmentModule>
<EquipmentModule ID="CHLOROHYDRINATOR">
<Description>Chlorohydrinator</Description>
</EquipmentModule>
<EquipmentModule ID="LIME_REACTOR">
<Description>Lime Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="DECANTER">
<Description>Decanter</Description>
</EquipmentModule>
<EquipmentModule ID="COLUMN">
<Description>Column</Description>
</EquipmentModule>
<EquipmentModule ID="WASTE_TREATMENT">
<Description>Waste Treatment</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="EPICHLOROHYDRIN_PLANT_RECIPE">
<Description>Master recipe for Epichlorohydrin</Description>
<ProductID>EPICHLOROHYDRIN</ProductID>
<UnitProcedure ID="EPICHLOROHYDRIN_PLANT_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="CHLORINATE">
<Description>Chlorinate 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="CHLOROHYDRINATE">
<Description>Chlorohydrinate 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="DEHYDROCHLOR">
<Description>Dehydrochlor 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="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_05">
<Description>Operation 5</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_06">
<Description>Operation 6</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>
</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.
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