C₆H₅OH
Precursor to resins, bisphenol A, and pharmaceuticals
Molecular Structure
Molecular Details
| Molecular Formula | C₆H₅OH |
| Molecular Weight | 94.11 g/mol |
| State | Solid/Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Cumene, Oxygen (Feedstock)
➡️ Outputs (Products): Bisphenol A, Caprolactam, Phenolic Resins, Cyclohexanone
Chemistry & Engineering
| Reaction Equation | Cumene + O₂ → Cumene Hydroperoxide → Phenol + Acetone |
| Thermodynamics | Autoxidation is exothermic; Cleavage is strongly exothermic |
| Catalyst System | Sulfuric acid for cleavage |
| Reactor Class | Oxidation tower followed by acid cleavage unit |
| Process Considerations | The Hock process couples Phenol and Acetone production efficiently. |
Extraterrestrial Production Pattern
- Benzene + propylene → cumene (alkylation)
- Cumene oxidation → cumene hydroperoxide
- Acid-catalyzed cleavage → phenol + acetone
- Distillation for separation and purification
Applications
- Bisphenol A for polycarbonate and epoxy
- Phenolic resins (Bakelite)
- Caprolactam (for nylon 6)
- Pharmaceuticals and disinfectants
Reaction Diagram
Overall Reaction: C6H5CH(CH3)2 + O2 -> C6H5OH + CH3COCH3
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Cumene Oxidation | Bubble air through cumene at 80-130°C to form CHP |
| 2 | Concentration | Concentrate cumene hydroperoxide to 80% |
| 3 | Acid Cleavage | Decompose CHP with H₂SO₄ at 60-80°C |
| 4 | Neutralization | Neutralize acid with NaOH or phenol |
| 5 | Crude Separation | Separate phenol/acetone from α-methylstyrene |
| 6 | Phenol Purification | Distill to >99.9% phenol purity |
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 Phenol -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="PHENOL_CUMENE_CELL">
<Description>Process cell for Phenol production</Description>
<Unit ID="PHENOL_CUMENE">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="OXIDIZER">
<Description>Oxidizer</Description>
</EquipmentModule>
<EquipmentModule ID="CONCENTRATOR">
<Description>Concentrator</Description>
</EquipmentModule>
<EquipmentModule ID="CLEAVAGE_REACTOR">
<Description>Cleavage Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="NEUTRALIZER">
<Description>Neutralizer</Description>
</EquipmentModule>
<EquipmentModule ID="SEPARATOR">
<Description>Separator</Description>
</EquipmentModule>
<EquipmentModule ID="COLUMN">
<Description>Column</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="PHENOL_CUMENE_RECIPE">
<Description>Master recipe for Phenol</Description>
<ProductID>PHENOL</ProductID>
<UnitProcedure ID="PHENOL_CUMENE_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="OXIDIZE">
<Description>Oxidize 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="CONCENTRATE">
<Description>Concentrate 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="CLEAVE">
<Description>Cleave 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="NEUTRALIZE">
<Description>Neutralize 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="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_06">
<Description>Operation 6</Description>
<Phase ID="PURIFY">
<Description>Purify 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.