Diphenylmethane Di- and Polyamine Cascade Synthesis to Reduce Discoloration

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Solution Overview

Problem

Existing methods for producing di- and polyamines of the diphenylmethane series result in chromophores that cause discoloration and the formation of N-methylated secondary products, leading to darkly colored polyurethane products and undesirable chlorine compounds.

Innovation Solution

A process involving a cascade of reaction zones with a split formaldehyde addition, where a first portion of formaldehyde is added initially and a second portion is added to the second reactor, followed by a controlled temperature increase, to minimize chromophore and N-methylated product formation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If aniline and formaldehyde are reacted in the presence of acid catalysts using conventional methods, then the production efficiency is maintained, but chromophores are formed that cause discoloration of the final polyurethane products

Engineering Contradiction:
Improveproduction efficiencyVSAvoiddiscoloration
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The formaldehyde addition is divided into two distinct portions: a first portion added at the beginning of the reaction and a second portion added to the second reactor in the cascade. This segmentation allows different reaction conditions to be applied at different stages, suppressing chromophore formation while maintaining production efficiency

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The process implements a controlled temperature increase across the reaction cascade (from 20-40°C in early reactors to 80-150°C in later reactors) and adjusts formaldehyde concentration dynamically. These parameter changes optimize the reaction at each stage to minimize chromophore formation while maintaining productivity

Inventive Principle:
Principle #35Parameter changes

2Productivity

If conventional acid-catalyzed reaction methods are used, then the reaction proceeds efficiently, but N-methylated secondary products are formed leading to undesirable chlorine compounds

Engineering Contradiction:
Improvereaction efficiencyVSAvoidN-methylated secondary products
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The reaction is divided into multiple zones in a cascade configuration, with each zone having optimized conditions. The split formaldehyde addition specifically targets the suppression of N-methylation side reactions while maintaining the main condensation reaction efficiency

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The first portion of formaldehyde is added preliminarily to establish optimal reaction conditions before the main reaction cascade begins. This preliminary action sets up the reaction environment to favor the desired condensation pathway over N-methylation side reactions

Inventive Principle:
Principle #10Preliminary action

3Productivity

If the reaction is carried out at elevated temperatures to increase reaction rate, then productivity improves, but chromophore formation and discoloration worsen

Engineering Contradiction:
Improvereaction rateVSAvoidchromophore formation
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The reaction cascade is segmented into zones with progressively increasing temperatures. Early zones operate at lower temperatures (20-40°C) to suppress chromophore formation, while later zones operate at higher temperatures (80-150°C) to complete the reaction and drive productivity

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The temperature parameter is dynamically changed across the reaction cascade and over time. The controlled temperature increase profile allows the system to achieve high reaction rates in later stages while maintaining low chromophore formation conditions in earlier stages

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 process significantly reduces discoloration and N-methylated product formation, resulting in high-quality di- and polyamines suitable for producing light-colored polyisocyanates and polyurethanes with reduced chlorine content.

Implementation Method 1

converting the first reaction product to a second reaction product comprising di- and polyamines of the diphenyl methane series in a cascade of 4 to 25 reaction zones arranged in series

Methodology Applied
Scientific EffectRearrangement reaction: Chemical Bonding

Implementation Method 2

the temperature consecutively increases from the third to the last of the reaction zones, the temperature in the third of the reaction zones being from 15°C to 50°C higher than in the second of the reaction zones

Methodology Applied
Scientific EffectThermal heating: Heating

Data Source

PatentEP4345088B1A process for preparing di- and polyamines of the diphenyl methane series
Publication Date: 2025.10.22 COVESTRO DEUTSCHLAND AG
  • EP4345088B1 patent drawing

AI summary

The present invention relates to a process for preparing di- and polyamines of the diphenyl methane series. More specifically, the process comprises reacting aniline and formaldehyde by (1a) mixing aniline with hydrochloric acid to form aniline hydrochloride, and (1b) mixing the aniline hydrochloride with a first portion of aqueous formaldehyde; or (1c) mixing aniline with a first portion of aqueous formaldehyde to form an aminal, and (1d) mixing the aminal with hydrochloric acid; to obtain a first reaction product; (2) converting the first reaction product to a second reaction product comprising di- and polyamines of the diphenyl methane series in a cascade of 4 to 25 reaction zones arranged in series, wherein a second portion of aqueous formaldehyde is added to the second of the reaction zones, in which second reaction zone the temperature is equal to or up to 20°C higher than the temperature in the first reaction zone, and wherein the temperature consecutively increases from the third to the last of the reaction zones, the temperature in the third of the reaction zones being from 15°C to 50°C higher than in the second of the reaction zones, and (3) working-up the second reaction product to obtain the di- and polyamines of the diphenyl methane series.