Hydrogen Siloxane Equilibration Using Macroporous Acid Resin

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Solution Overview

Problem

Existing methods struggle to produce hydrogen siloxanes with a statistically uniform distribution of SiH functions, particularly methyl hydrogen siloxy and dimethyl hydrogen siloxy groups, while minimizing SiH losses, which is crucial for applications like polyether siloxanes in surfactants and polyurethane foams.

Innovation Solution

A process using a macro-crosslinked, aqueous cation exchange resin with specific surface area and pore diameter, and a water content of 6-16 wt%, to equilibrate siloxanes at controlled temperatures, followed by noble metal-catalyzed hydrosilylation to assess clarity, ensuring uniform SiH distribution.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If homogeneous acid catalysts are used for equilibration, then equilibration efficiency is improved, but post-treatment complexity increases due to neutralization and filtration requirements

Engineering Contradiction:
Improveequilibration efficiencyVSAvoidpost-treatment complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent employs solid-phase acid catalysts as intermediaries that enable equilibration without requiring neutralization. The solid catalyst can be easily separated from the liquid siloxane phase through filtration, eliminating the complex post-treatment steps associated with homogeneous acid catalysts while maintaining high equilibration efficiency

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent replaces the chemical neutralization step (chemical system) with a physical filtration step (mechanical system). By using solid-phase catalysts, the complex chemical post-treatment involving neutralization and salt removal is substituted with simple mechanical filtration, reducing overall process complexity

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

2Ease of manufacture

If conventional equilibration methods are used, then processing is simplified, but SiH function losses increase

Engineering Contradiction:
Improveprocessing simplicityVSAvoidSiH function losses
Core Design Contradiction:
Ease of manufactureVSLoss of substance

Solution Approach 1:

The patent optimizes equilibration parameters including temperature control (10-120°C range), catalyst acidity strength, and reaction time to achieve complete equilibration while minimizing SiH losses. By carefully controlling these parameters, the process maintains simplicity while preserving SiH functionality through optimized reaction conditions rather than complex additional steps

Inventive Principle:
Principle #35Parameter changes

3Quantity of substance

If non-macrocrosslinked catalysts are used, then catalyst cost is reduced, but product uniformity decreases

Engineering Contradiction:
Improvecatalyst costVSAvoidproduct uniformity
Core Design Contradiction:
Quantity of substanceVSManufacturing precision

Solution Approach 1:

The patent specifies the use of macrocrosslinked catalysts with controlled pore structures that provide uniform active sites for equilibration. The macrocrosslinked structure ensures consistent product uniformity and distribution of SiH functions while maintaining reasonable catalyst costs through efficient catalytic activity per unit mass

Inventive Principle:
Principle #31Porous materials

4Measurement precision

If complex analysis methods are used to confirm equilibration, then measurement precision is improved, but process complexity increases

Engineering Contradiction:
Improveequilibration confirmation accuracyVSAvoidanalysis complexity
Core Design Contradiction:
Measurement precisionVSDevice complexity

Solution Approach 1:

The patent employs simple, inexpensive visual inspection methods (clarity and uniformity assessment) rather than complex instrumental analysis. This disposable-like approach uses basic observational techniques that provide sufficient confirmation of equilibration without requiring sophisticated equipment, maintaining measurement adequacy while eliminating analytical complexity

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

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

Produces acid-free, stable, and clear hydrogen siloxane equilibrates with preserved SiH functionality, suitable for further processing into polyether siloxanes, by visually confirming uniformity without complex analysis.

Implementation Method 1

the siloxane mixture is treated with a macrocrosslinked, aqueous cation exchange resin containing sulfonic acid groups and is rearranged by the SiOSi bonds are allowed to react

Methodology Applied
Scientific EffectAcid catalysis: Catalysis

Implementation Method 2

yields a clear addition product at T = 25°C upon noble metal-catalyzed, hydrosilylation, addition to at least one unsaturated polyether

Methodology Applied
Scientific EffectHydrosilylation: Chemical Bonding

Data Source

PatentEP4650385A1Production of acid free hydrogen siloxane equilibrationates
Publication Date: 2025.11.19 EVONIK OPERATIONS GMBH
  • EP4650385A1 patent drawing
  • EP4650385A1 patent drawing
  • EP4650385A1 patent drawing

AI summary

The invention relates to a process for producing acid-free hydrogen siloxane equilibrates, wherein a mixture comprising at least two different siloxanes, which together possess dimethyl hydrogen siloxy groups, methyl hydrogen siloxy groups, dimethyl siloxy groups, and preferably trimethyl siloxy groups, is brought into contact with a macro-crosslinked, aqueous cation exchange resin containing sulfonic acid groups and is allowed to react with rearrangement of the SiOSi bonds until the acid-free hydrogen siloxane equilibrate produced in this way yields a clear addition product at T = 25°C upon noble metal-catalyzed, hydrosilylic addition to at least one unsaturated polyether having an arithmetically averaged HLB value >9.0 calculated according to the Guo increment method, wherein the rearrangement of the SiOSi bonds is carried out in the temperature range of 10 to 50°C, with the proviso thatthat the cation exchange resin is characterized by the fact that the product P from its specific surface area and its mean pore diameter P ≥ 2.2 × 10-3 m3/kg and the specific surface area A ≥ 35 m2/g and that it also has a water content of 6 to 16 percent by weight based on the weight of the cation exchange resin.