(NH₂)₂CO
Largest-volume nitrogen fertilizer and resin precursor
Molecular Structure
Molecular Details
| Molecular Formula | (NH₂)₂CO |
| Molecular Weight | 60.06 g/mol |
| State | Solid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Ammonia, Carbon Dioxide (Feedstock)
➡️ Outputs (Products): Melamine, Fertilizers, Resins
Chemistry & Engineering
| Reaction Equation | 2NH₃ + CO₂ ⇌ NH₄CO₂NH₂ ⇌ (NH₂)₂CO + H₂O |
| Thermodynamics | First step exothermic, second step endothermic |
| Catalyst System | None |
| Reactor Class | High pressure stripper reactor (150 bar, 180°C) |
| Process Considerations | Corrosion is severe (ammonium carbamate). Biuret formation must be minimized. |
Extraterrestrial Production Pattern
- NH₃ + CO₂ → ammonium carbamate (fast reaction)
- Ammonium carbamate → urea + H₂O (slower, equilibrium limited)
- Operating at 140-210°C and 140-250 bar
- Stripping and recycling of unreacted materials
Applications
- Nitrogen fertilizer (46% N)
- Urea-formaldehyde resins
- AdBlue/DEF for diesel emissions
- Melamine production
Reaction Diagram
Overall Reaction: 2NH3 + CO2 -> (NH2)2CO + H2O
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Ammonia/CO₂ Mixing | Mix NH₃ and CO₂ at high pressure (140-250 bar) |
| 2 | Carbamate Formation | Exothermic reaction to ammonium carbamate |
| 3 | Urea Synthesis | Dehydration to urea at 180-210°C |
| 4 | Stripping | Steam strip unconverted carbamate |
| 5 | Concentration | Evaporate to 99.7% urea solution |
| 6 | Prilling/Granulation | Form solid urea prills or granules |
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 Urea -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="UREA_SYNTHESIS_CELL">
<Description>Process cell for Urea production</Description>
<Unit ID="UREA_SYNTHESIS">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="MIXER">
<Description>Mixer</Description>
</EquipmentModule>
<EquipmentModule ID="CARBAMATE_REACTOR">
<Description>Carbamate Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="UREA_REACTOR">
<Description>Urea Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="STRIPPER">
<Description>Stripper</Description>
</EquipmentModule>
<EquipmentModule ID="EVAPORATOR">
<Description>Evaporator</Description>
</EquipmentModule>
<EquipmentModule ID="PRILLING_TOWER">
<Description>Prilling Tower</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="UREA_SYNTHESIS_RECIPE">
<Description>Master recipe for Urea</Description>
<ProductID>UREA</ProductID>
<UnitProcedure ID="UREA_SYNTHESIS_UP">
<Description>Unit procedure for synthesis</Description>
<Operation ID="OP_01">
<Description>Operation 1</Description>
<Phase ID="MIX">
<Description>Mix 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="FORM_CARBAMATE">
<Description>Form Carbamate 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="SYNTHESIZE">
<Description>Synthesize 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="STRIP">
<Description>Strip 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="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_06">
<Description>Operation 6</Description>
<Phase ID="SOLIDIFY">
<Description>Solidify 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.