C₆H₄(COOH)₂
Key monomer for PET polyester fibers and bottles
Molecular Structure
Molecular Details
| Molecular Formula | C₆H₄(COOH)₂ |
| Molecular Weight | 166.13 g/mol |
| State | Solid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Xylene, Acetic Acid, Oxygen (Feedstock)
➡️ Outputs (Products): Polyethylene Terephthalate
Chemistry & Engineering
| Reaction Equation | p-Xylene + O₂ → PTA |
| Thermodynamics | Exothermic oxidation |
| Catalyst System | Cobalt-Manganese-Bromide (Co-Mn-Br) |
| Reactor Class | Titanium-lined stirred tank (corrosive + high T/P) |
| Process Considerations | Crude TA must be hydrogenated to remove colored impurities (4-CBA) for bottle grade. |
Extraterrestrial Production Pattern
- p-Xylene oxidation with air
- Co-Mn-Br catalyst in acetic acid solvent
- Operating at 175-225°C and 15-30 bar
- Crystallization and hydrogenation purification
Applications
- PET fiber and film production
- PET bottle resin
- Polybutylene terephthalate (PBT)
- Unsaturated polyester resins
Reaction Diagram
Overall Reaction: C8H10 + 3O2 -> C8H6O4 + 2H2O
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | p-Xylene Oxidation | Air oxidation in acetic acid at 175-225°C |
| 2 | Co-Mn-Br Catalysis | Homogeneous catalyst system |
| 3 | Crystallization | Crystallize crude TPA from mother liquor |
| 4 | Hydrogenation | Purify by catalytic hydrogenation (PTA process) |
| 5 | Filtration | Filter and wash purified crystals |
| 6 | Drying | Dry to specification moisture content |
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 Terephthalic Acid -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="PTA_PLANT_CELL">
<Description>Process cell for Terephthalic Acid production</Description>
<Unit ID="PTA_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="OXIDATION_REACTOR">
<Description>Oxidation Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="CATALYST_SYSTEM">
<Description>Catalyst System</Description>
</EquipmentModule>
<EquipmentModule ID="CRYSTALLIZER">
<Description>Crystallizer</Description>
</EquipmentModule>
<EquipmentModule ID="HYDROGENATOR">
<Description>Hydrogenator</Description>
</EquipmentModule>
<EquipmentModule ID="FILTER">
<Description>Filter</Description>
</EquipmentModule>
<EquipmentModule ID="DRYER">
<Description>Dryer</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="PTA_PLANT_RECIPE">
<Description>Master recipe for Terephthalic Acid</Description>
<ProductID>TEREPHTHALIC_ACID</ProductID>
<UnitProcedure ID="PTA_PLANT_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="CATALYZE">
<Description>Catalyze 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="CRYSTALLIZE">
<Description>Crystallize 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="HYDROGENATE">
<Description>Hydrogenate 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="FILTER">
<Description>Filter 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="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>
</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.