Propane Nitration Process Selectivity and Corrosion Control

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Solution Overview

Problem

Current processes for nitration of propane result in low yields and high waste production, with challenges in reactor corrosion, reaction exotherm control, and inefficient conversion of nitric acid, leading to economic and environmental concerns.

Innovation Solution

A process involving reacting propane with aqueous nitric acid at high pressure (at least 1000 psi) and controlled temperature (215-325°C) to achieve selective nitration, using a corrosion-resistant reactor and optimizing conditions for high conversion of nitric acid to 2-nitropropane and 2,2-dinitropropane, while minimizing by-products like nitromethane and aldehydes.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of operation

If vapor phase nitration is used for propane, then the process is simple to operate, but it produces a mixture of four nitroparaffin products with low selectivity

Engineering Contradiction:
Improveease of operationVSAvoidproduct selectivity
Core Design Contradiction:
Ease of operationVSManufacturing precision

Solution Approach 1:

The patent changes the physical state parameters of the reaction system from vapor phase to mixed vapor-liquid phase, operating at elevated pressures (100-500 atm) and temperatures (100-200°C). This parameter change fundamentally alters the reaction pathway to achieve selective production of 2-nitropropane while maintaining operational feasibility

Inventive Principle:
Principle #35Parameter changes

2Manufacturing precision

If mixed vapor-liquid phase nitration is used to improve selectivity, then 2-nitropropane can be produced selectively, but the conversion of nitric acid is low and waste disposal costs increase

Engineering Contradiction:
Improveproduct selectivityVSAvoidnitric acid conversion efficiency
Core Design Contradiction:
Manufacturing precisionVSLoss of substance

Solution Approach 1:

The patent employs extreme pressure conditions (100-500 atm) combined with moderate temperatures (100-200°C) to enhance nitric acid conversion efficiency. These parameter changes drive the reaction toward higher conversion while maintaining the selective mixed vapor-liquid phase regime that produces 2-nitropropane as the dominant product

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent implements continuous recycling of unreacted nitric acid and other process streams back into the reaction system. This periodic circulation allows multiple passes through the reactor, progressively converting nitric acid to product while maintaining high selectivity across multiple reaction cycles

Inventive Principle:
Principle #19Periodic action

3Productivity

If high pressure and temperature conditions are applied to improve conversion, then nitric acid conversion increases, but reactor corrosion and safety risks increase

Engineering Contradiction:
Improvenitric acid conversionVSAvoidreactor corrosion
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent optimizes the pressure-temperature parameter space by operating at very high pressures (100-500 atm) combined with moderate temperatures (100-200°C). This specific parameter combination achieves high conversion while avoiding the excessive temperatures that would accelerate corrosion and decomposition reactions

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs composite reactor materials and lining systems that combine corrosion-resistant alloys with protective ceramic or polymer linings. These composite structures provide the necessary mechanical strength to withstand high pressures while offering chemical resistance to nitric acid and reaction products

Inventive Principle:
Principle #40Composite materials

4Productivity

If conventional nitration processes are used, then production capacity is maintained, but economic costs increase due to low yields and waste disposal

Engineering Contradiction:
Improveproduction capacityVSAvoidfeedstock efficiency
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The patent implements comprehensive recycling loops for unreacted propane, nitric acid, and other valuable streams. These periodic recycling operations allow multiple utilization passes through the reactor system, dramatically improving overall feedstock efficiency while maintaining steady production capacity

Inventive Principle:
Principle #19Periodic action

Solution Approach 2:

The patent achieves superior reaction efficiency by operating in the mixed vapor-liquid phase regime at elevated pressures (100-500 atm) and temperatures (100-200°C). These parameter changes optimize both conversion and selectivity simultaneously, producing high yields of 2-nitropropane with minimal byproducts, thereby improving economic efficiency without sacrificing production capacity

Inventive Principle:
Principle #35Parameter changes

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This process significantly increases the conversion of nitric acid and propane to desired products, reduces by-product formation, and allows for efficient recovery of nitric oxide, making the process more economical and environmentally friendly by enabling high yields and viable biotreatment of waste streams.

Implementation Method 1

reacting propane with aqueous nitric acid at a pressure of at least about 1000 psi and a temperature of between about 215 and about 325 degrees Celsius

Methodology Applied
Scientific EffectNitration reaction: Chemical Bonding

Implementation Method 2

recovering the formed nitrated compounds

Methodology Applied
Scientific EffectPhase separation: Liquid-Liquid Extraction

Data Source

PatentUS8519199B2Process for the manufacture of nitropropanes
Publication Date: 2013.08.27 ADVANCION CORP

AI summary

Provided is a process for the formation of 2-nitropropane and/or 2,2-dinitropropane by the nitration of propane with dilute nitric acid.