HNO₃
Essential for fertilizers, explosives, and metal processing
Molecular Structure
Molecular Details
| Molecular Formula | HNO₃ |
| Molecular Weight | 63.01 g/mol |
| State | Liquid at standard conditions |
Olefinverbund Integration
⬅️ Inputs (Starting Materials): Ammonia, Oxygen (Feedstock), Water (Feedstock)
➡️ Outputs (Products): Ammonium Nitrate, Adipic Acid, Nitrobenzene, TDI
Chemistry & Engineering
| Reaction Equation | NH₃ + O₂ → NO; NO + O₂ → NO₂; NO₂ + H₂O → HNO₃ |
| Thermodynamics | Exothermic oxidation |
| Catalyst System | Platinum-Rhodium gauze |
| Reactor Class | Burner at 900°C followed by absorption columns |
| Process Considerations | Ostwald process. Noble metal catalyst loss is a key operating cost. |
Extraterrestrial Production Pattern
- Ammonia oxidation over Pt-Rh gauze catalyst at 850-950°C
- Cooling and oxidation of NO to NO₂
- Absorption in water to form nitric acid
- Concentration by distillation or extractive methods
Applications
- Ammonium nitrate fertilizer
- Explosives manufacturing
- Metal etching and pickling
- Nitration reactions for organics
Reaction Diagram
Overall Reaction: 4NH3 + 5O2 -> 4NO + 6H2O; 2NO + O2 -> 2NO2; 3NO2 + H2O -> 2HNO3 + NO
Unit Operations
Process steps following chemical engineering unit operation principles:
| Step | Operation | Description |
|---|---|---|
| 1 | Ammonia/Air Mixing | Mix NH₃ with filtered air (10-12% NH₃) |
| 2 | Catalytic Oxidation | Pt-Rh gauze at 850-950°C, 1-10 bar |
| 3 | Gas Cooling | Cool NO gas and oxidize to NO₂ |
| 4 | Absorption | Absorb NO₂ in water in absorption tower |
| 5 | Tail Gas Treatment | Catalytic reduction of residual NOx |
| 6 | Concentration | Concentrate to 60-68% HNO₃ by distillation |
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 Nitric Acid -->
<!-- Educational schema - simplified for demonstration -->
<BatchML xmlns="http://www.wbf.org/xml/B2MML-V0600">
<ProcessCell ID="NITRIC_ACID_PLANT_CELL">
<Description>Process cell for Nitric Acid production</Description>
<Unit ID="NITRIC_ACID_PLANT">
<Description>Main synthesis unit</Description>
<!-- Equipment Modules -->
<EquipmentModule ID="MIXER">
<Description>Mixer</Description>
</EquipmentModule>
<EquipmentModule ID="BURNER">
<Description>Burner</Description>
</EquipmentModule>
<EquipmentModule ID="COOLER">
<Description>Cooler</Description>
</EquipmentModule>
<EquipmentModule ID="ABSORBER">
<Description>Absorber</Description>
</EquipmentModule>
<EquipmentModule ID="SCR_REACTOR">
<Description>Scr Reactor</Description>
</EquipmentModule>
<EquipmentModule ID="CONCENTRATOR">
<Description>Concentrator</Description>
</EquipmentModule>
</Unit>
</ProcessCell>
<MasterRecipe ID="NITRIC_ACID_PLANT_RECIPE">
<Description>Master recipe for Nitric Acid</Description>
<ProductID>NITRIC_ACID</ProductID>
<UnitProcedure ID="NITRIC_ACID_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="OXIDIZE_NH3">
<Description>Oxidize 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_03">
<Description>Operation 3</Description>
<Phase ID="COOL">
<Description>Cool 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="ABSORB">
<Description>Absorb 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_TAILGAS">
<Description>Treat Tailgas 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="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>
</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.