C₆H₅CH(CH₃)₂
Intermediate for phenol and acetone production
Molecular Structure
Molecular Details
| Molecular Formula | C₆H₅CH(CH₃)₂ |
| Molecular Weight | 120.19 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
Chemistry & Engineering
| Reaction Equation | C₆H₆ + C₃H₆ → C₆H₅CH(CH₃)₂ |
| Thermodynamics | Exothermic (-113 kJ/mol) |
| Catalyst System | Solid Phosphoric Acid (SPA) or Zeolites (Beta, Y) |
| Reactor Class | Fixed bed reactor operating at 200-250°C, 20-40 bar |
| Process Considerations | Feedstock bond for the Hock process (Phenol/Acetone). |
Extraterrestrial Production Pattern
- Benzene + propylene → cumene
- Solid phosphoric acid or zeolite catalyst
- Vapor or liquid-phase process
- Distillation to remove di-isopropylbenzene
Applications
- Phenol and acetone production (cumene process)
- Aviation fuel component
- Solvent
Reaction Diagram
Overall Reaction: C6H6 + C3H6 -> C6H5CH(CH3)2
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Benzene/Propylene Feed | Pump and vaporize reactants |
| 2 | Alkylation | Zeolite or H₃PO₄/SiO₂ catalyst at 200-250°C |
| 3 | Transalkylation | Convert DIPB to cumene with benzene |
| 4 | Benzene Column | Recover unreacted benzene |
| 5 | Cumene Column | Distill cumene product |
| 6 | DIPB Column | Recover diisopropylbenzene for recycle |
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 Cumene -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="CUMENE_PLANT_CELL">
<Description>Process cell for Cumene production</Description>
<Unit ID="CUMENE_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="VAPORIZER">
<Description>Vaporizer</Description>
</EquipmentModule>
<EquipmentModule ID="ALKYLATION_REACTOR">
<Description>Alkylation Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="TRANSALKYLATION_REACTOR">
<Description>Transalkylation Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="BENZENE_COLUMN">
<Description>Benzene Column</Description>
</EquipmentModule>
<EquipmentModule ID="CUMENE_COLUMN">
<Description>Cumene Column</Description>
</EquipmentModule>
<EquipmentModule ID="DIPB_COLUMN">
<Description>Dipb Column</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="CUMENE_PLANT_RECIPE">
<Description>Master recipe for Cumene</Description>
<ProductID>CUMENE</ProductID>
<UnitProcedure ID="CUMENE_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="ALKYLATE">
<Description>Alkylate 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="TRANSALKYLATE">
<Description>Transalkylate 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="BENZENE_REC">
<Description>Benzene Rec 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="CUMENE_DIST">
<Description>Cumene Dist 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="DIPB_REC">
<Description>Dipb Rec 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.