C₈H₁₀ (C₆H₄(CH₃)₂)
Aromatic mixture (ortho, meta, para isomers) for PET and phthalates
Molecular Structure
Molecular Details
| Molecular Formula | C₈H₁₀ (C₆H₄(CH₃)₂) |
| Molecular Weight | 106.16 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Toluene
➡️ Outputs (Products): Terephthalic Acid, Phthalic Anhydride
Chemistry & Engineering
| Reaction Equation | 2 Toluene ⇄ Benzene + Xylene (Disproportionation) |
| Thermodynamics | Close to thermoneutral |
| Catalyst System | Zeolite mordenite or ZSM-5 |
| Reactor Class | Fixed bed transalkylation unit |
| Process Considerations | Mixture of isomers (ortho, meta, para). Para-xylene is crucial for PET; Ortho for phthalic anhydride. |
Extraterrestrial Production Pattern
- Catalytic reforming of naphtha produces mixed xylenes
- Toluene disproportionation over zeolite catalyst
- Isomerization to shift equilibrium toward p-xylene
- Adsorptive separation (Parex process) for pure p-xylene
Applications
- p-Xylene → terephthalic acid → PET polyester
- o-Xylene → phthalic anhydride
- Solvent applications
- Isophthalic acid production
Reaction Diagram
Overall Reaction: Naphtha reforming -> C8H10 isomers
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Reformate C8 Cut | Fractionate C8 aromatics from reformate |
| 2 | Xylene Isomerization | Isomerize to equilibrium mixture |
| 3 | p-Xylene Recovery | Adsorption (Parex) or crystallization |
| 4 | o-Xylene Recovery | Distillation of o-xylene |
| 5 | m-Xylene Recycle | Return m-xylene to isomerization |
| 6 | Product Finishing | Final distillation to specs |
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 Xylene -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="XYLENE_COMPLEX_CELL">
<Description>Process cell for Xylene production</Description>
<Unit ID="XYLENE_COMPLEX">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="SPLITTER">
<Description>Splitter</Description>
</EquipmentModule>
<EquipmentModule ID="ISOMERIZER">
<Description>Isomerizer</Description>
</EquipmentModule>
<EquipmentModule ID="PAREX_UNIT">
<Description>Parex Unit</Description>
</EquipmentModule>
<EquipmentModule ID="OX_COLUMN">
<Description>Ox Column</Description>
</EquipmentModule>
<EquipmentModule ID="RECYCLE_SYSTEM">
<Description>Recycle System</Description>
</EquipmentModule>
<EquipmentModule ID="PRODUCT_COLUMN">
<Description>Product Column</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="XYLENE_COMPLEX_RECIPE">
<Description>Master recipe for Xylene</Description>
<ProductID>XYLENE</ProductID>
<UnitProcedure ID="XYLENE_COMPLEX_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="FRACTIONATE">
<Description>Fractionate 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="ISOMERIZE">
<Description>Isomerize 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="RECOVER_PX">
<Description>Recover Px 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="RECOVER_OX">
<Description>Recover Ox 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="RECYCLE_MX">
<Description>Recycle Mx 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="FINISH">
<Description>Finish 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.