Nitration Reactor Downward Flow Segmentation

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Solution Overview

Problem

Adiabatic nitration reactors face limitations in hydrostatic demands and plant layout due to vertical orientation, which can lead to reactant accumulation, coalescence, and reduced conversion efficiency, while horizontally oriented reactors suffer from slow drainage and reduced safety.

Innovation Solution

A plug-flow reactor design incorporating sections of downward flow, with a stability parameter (Φ) that ensures a dispersed or bubbly flow regime, allowing for efficient nitration of aromatic compounds while maintaining safety and high conversion efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If vertically oriented reactor sections are used, then nitric acid conversion efficiency is improved, but hydrostatic demands and plant layout complexity increase

Engineering Contradiction:
Improvenitric acid conversion efficiencyVSAvoidhydrostatic demands and plant layout
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The reactor is divided into multiple vertical sections (first vertically-oriented reactor section, second vertically-oriented reactor section) connected by connecting sections. This segmentation allows the reactor to maintain high conversion efficiency through vertical orientation while reducing overall hydrostatic demands by breaking the continuous vertical column into manageable segments.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent introduces horizontal or inclined connecting sections between vertical reactor sections, adding a horizontal dimension to the previously purely vertical flow path. This dimensional change reduces the hydrostatic head requirements while maintaining the benefits of vertical flow for conversion efficiency.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

2Speed

If downward flowpath is used, then drainage speed is improved, but flow regime stability may be compromised

Engineering Contradiction:
Improvedrainage speedVSAvoidflow regime stability
Core Design Contradiction:
SpeedVSStability of the object's composition

Solution Approach 1:

The patent carefully controls operating parameters (flow rates, reactor geometry, connecting section design) to maintain stable dispersed or bubbly flow regimes in the downward flowpath. By optimizing these parameters, the reactor achieves both rapid drainage and flow regime stability, preventing reactant accumulation and coalescence.

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

The reactor design overcomes hydrostatic and layout challenges, ensuring stable two-phase flow, quick drainage, and high nitric acid conversion efficiency, reducing byproduct formation and improving safety.

Implementation Method 1

operating conditions that produce a flow regime in the vertically-downward flowpath that is a dispersed flow regime or a bubbly flow regime

Methodology Applied
Scientific EffectTwo-phase flow: Two-Phase Flow

Implementation Method 2

a dispersed or bubbly flow regime

Methodology Applied
Scientific EffectDispersed flow:

Implementation Method 3

a dispersed or bubbly flow regime

Methodology Applied
Scientific EffectBubbly flow:

Implementation Method 4

vertically-downward flowpath for the nitration reactants

Methodology Applied
Scientific EffectGravitational flow: Gravitation

Data Source

PatentUS11819819B2Nitration reactor and method
Publication Date: 2023.11.21 NORAM ENG & CONSTRS
  • US11819819B2 patent drawing
  • US11819819B2 patent drawing
  • US11819819B2 patent drawing

AI summary

A nitration reactor (10) incorporating sections of downward flow for use in preparing nitrated organic compounds. It comprises a first vertically-oriented reactor section (12), a second vertically-oriented reactor section (14), a connecting section (16) between the two reactor sections, one or more inlets (20, 22) for introducing nitration reactants into the reactor, an outlet (24) for the removal of nitration reaction products, a vertically-downward flowpath (26) for the nitration reactants in one of the reactor sections or the connecting section, and operating conditions that produce a flow regime in the vertically-downward flowpath that is a dispersed flow regime or a bubbly flow regime. The invention overcomes the limitations of prior art nitration reactors of the type in which fluids flow largely in a vertically upward direction, with respect to hydrostatic demands and plant layout considerations.