C₆H₄(CO)₂O
Precursor for plasticizers and alkyd resins
Molecular Structure
Molecular Details
| Molecular Formula | C₆H₄(CO)₂O |
| Molecular Weight | 148.12 g/mol |
| State | Solid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Xylene, Oxygen (Feedstock)
➡️ Outputs (Products): Plasticizers, Resins
Chemistry & Engineering
| Reaction Equation | o-Xylene + 3O₂ → Phthalic Anhydride + 3H₂O |
| Thermodynamics | Highly exothermic |
| Catalyst System | Vanadium Pentoxide on Titania |
| Reactor Class | Multitubular fixed bed molten salt cooled |
| Process Considerations | Switchable with Naphthalene feedstock. |
Extraterrestrial Production Pattern
- o-Xylene + O₂ → phthalic anhydride (V₂O₅/TiO₂ catalyst)
- Fixed-bed reactor at 360-400°C
- Sublimation and condensation for recovery
- Alternative: naphthalene oxidation
Applications
- Phthalate plasticizers (DOP, DBP)
- Alkyd resins for paints
- Unsaturated polyester resins
- Dyes and pigments
Reaction Diagram
Overall Reaction: C8H10 + 3O2 -> C8H4O3 + 3H2O (or naphthalene oxidation)
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | o-Xylene Feed | Vaporize and mix with air |
| 2 | Oxidation | V₂O₅/TiO₂ catalyst at 340-400°C |
| 3 | Switch Condensers | Desublime crude PA on switch condenser tubes |
| 4 | Melting | Melt crude PA from condensers |
| 5 | Thermal Treatment | Heat to decompose maleic anhydride |
| 6 | Distillation | Vacuum distillation to >99.5% PA |
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 Phthalic Anhydride -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="PA_PLANT_CELL">
<Description>Process cell for Phthalic Anhydride production</Description>
<Unit ID="PA_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="VAPORIZER">
<Description>Vaporizer</Description>
</EquipmentModule>
<EquipmentModule ID="REACTOR">
<Description>Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="SWITCH_CONDENSER">
<Description>Switch Condenser</Description>
</EquipmentModule>
<EquipmentModule ID="MELTER">
<Description>Melter</Description>
</EquipmentModule>
<EquipmentModule ID="TREATMENT">
<Description>Treatment</Description>
</EquipmentModule>
<EquipmentModule ID="COLUMN">
<Description>Column</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="PA_PLANT_RECIPE">
<Description>Master recipe for Phthalic Anhydride</Description>
<ProductID>PHTHALIC_ANHYDRIDE</ProductID>
<UnitProcedure ID="PA_PLANT_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="VAPORIZE">
<Description>Vaporize 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="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_03">
<Description>Operation 3</Description>
<Phase ID="CONDENSE">
<Description>Condense 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="MELT">
<Description>Melt 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="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>
<Operation ID="OP_06">
<Description>Operation 6</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>
</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.