DADPM Production via Gaseous HCl Absorption in Aniline

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

The production of poly-(diamino diphenyl methane) (DADPM) using gaseous hydrogen chloride as a catalyst faces challenges with catalyst solubility and equipment fouling, limiting commercial-scale operation efficiency and requiring additional water, which increases process complexity and equipment size.

Innovation Solution

Absorbing hydrogen chloride gas into aniline containing a controlled amount of water (0.1-7 wt%) to achieve the desired aniline/HCl ratio, allowing for efficient acid catalyzed condensation of aniline and formaldehyde, and utilizing the absorbed HCl in the process, thereby minimizing water usage and equipment modifications.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If gaseous hydrogen chloride is used as catalyst, then reaction rates increase, but catalyst solubility problems and equipment fouling occur

Engineering Contradiction:
Improvereaction rateVSAvoidcatalyst solubility
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

Water acts as an intermediary substance that facilitates the dissolution of gaseous HCl catalyst into the aniline reaction medium. By controlling water content at 0.1-7 wt%, the patent creates a soluble HCl-aniline-water complex that prevents catalyst precipitation and equipment fouling while maintaining high reaction rates.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Reliability

If additional water is added to prevent solids precipitation, then catalyst solubility improves, but process complexity and equipment size increase

Engineering Contradiction:
Improvecatalyst solubilityVSAvoidprocess complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The patent optimizes the water content parameter to a specific range (0.1-7 wt%) that simultaneously ensures catalyst solubility and prevents solids precipitation. This parameter optimization eliminates the need for additional water addition steps and complex separation equipment, simplifying the overall process while maintaining reliable catalyst performance.

Inventive Principle:
Principle #35Parameter changes

3Reliability

If aqueous hydrochloric acid is used instead of gaseous HCl, then catalyst solubility is maintained, but water content increases reducing reaction efficiency

Engineering Contradiction:
Improvecatalyst solubilityVSAvoidreaction rate
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The patent creates a localized optimal environment by controlling water content at 0.1-7 wt% specifically in the catalyst phase (aniline-HCl complex), while keeping the bulk reaction mixture at desired composition. This local quality control ensures catalyst solubility without unnecessarily increasing overall water content, thereby maintaining high reaction rates.

Inventive Principle:
Principle #3Local quality

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 approach enables efficient production of DADPM with reduced water content, increasing reaction rates, improving throughput, and simplifying equipment requirements, while maintaining product quality and allowing for seamless integration with existing manufacturing units.

Implementation Method 1

Absorbing hydrogen chloride gas into aniline containing a controlled amount of water (0.1-7 wt%) to achieve the desired aniline/HCl ratio

Methodology Applied
Scientific EffectAbsorption: Absorption (physical)

Data Source

PatentEP1960346B2Process for preparing diaminodiphenylmethanes
Publication Date: 2019.03.27 HUNTSMAN INTERNATIONAL LLC
  • EP1960346B2 patent drawing
  • EP1960346B2 patent drawing
  • EP1960346B2 patent drawing

AI summary

Process for preparing diamino diphenyl methane and poly-(diamino diphenyl methane) comprising reacting aniline with formaldehyde in the presence of hydrogen chloride added in the gaseous form wherein the aniline contains 0.1 to 7 wt %, preferably 2 to 5 wt % of a protic chemical, preferably water.