HOCH₂CH₂NH₂
Gas sweetening and surfactant intermediate
Molecular Structure
Molecular Details
| Molecular Formula | HOCH₂CH₂NH₂ |
| Molecular Weight | 61.08 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Ethylene Oxide, Ammonia
➡️ Outputs (Products): Gas Sweetening, Detergents
Chemistry & Engineering
| Reaction Equation | EO + NH₃ → MEA |
| Thermodynamics | Exothermic |
| Catalyst System | Water/Zeolite |
| Reactor Class | Tubular reactor |
| Process Considerations | CO2 scrubber choice. |
Extraterrestrial Production Pattern
- Ethylene oxide + NH₃ → ethanolamines mixture
- Excess ammonia favors MEA over DEA/TEA
- Operating at 40-80°C and 30-100 bar
- Distillation to separate MEA, DEA, TEA
Applications
- CO₂ and H₂S scrubbing (gas treatment)
- Surfactant production
- Cement grinding aids
- Metalworking fluids
Reaction Diagram
Overall Reaction: C2H4O + NH3 -> HOCH2CH2NH2
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | EO/Ammonia Mixing | Mix ethylene oxide with excess ammonia |
| 2 | Amination | React at 40-100°C, 30-150 bar |
| 3 | Ammonia Recovery | Flash and distill to recover NH₃ |
| 4 | MEA Distillation | Distill to separate MEA from DEA/TEA |
| 5 | Dehydration | Remove water traces |
| 6 | Product Storage | Store under nitrogen |
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 Monoethanolamine -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="MEA_PLANT_CELL">
<Description>Process cell for Monoethanolamine production</Description>
<Unit ID="MEA_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="MIXER">
<Description>Mixer</Description>
</EquipmentModule>
<EquipmentModule ID="REACTOR">
<Description>Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="FLASH">
<Description>Flash</Description>
</EquipmentModule>
<EquipmentModule ID="MEA_COLUMN">
<Description>Mea Column</Description>
</EquipmentModule>
<EquipmentModule ID="DRYER">
<Description>Dryer</Description>
</EquipmentModule>
<EquipmentModule ID="STORAGE">
<Description>Storage</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="MEA_PLANT_RECIPE">
<Description>Master recipe for Monoethanolamine</Description>
<ProductID>MONOETHANOLAMINE</ProductID>
<UnitProcedure ID="MEA_PLANT_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="AMINATE">
<Description>Aminate 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_NH3">
<Description>Recover Nh3 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="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>
<Operation ID="OP_05">
<Description>Operation 5</Description>
<Phase ID="DEHYDRATE">
<Description>Dehydrate 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="STORE">
<Description>Store 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.