Solid Acid Catalyst for Isoprenol Aldehyde Condensation

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Solution Overview

Problem

Current methods for preparing 2-substituted 4-hydroxy-4-methyltetrahydropyrans face challenges in achieving high yield, diastereomer excess, and minimizing by-product formation while using inexpensive and readily available starting materials on an industrial scale.

Innovation Solution

A process involving the reaction of 3-methylbut-3-en-1-ol (isoprenol) with aldehydes in the presence of a strongly acidic cation exchanger, using water and optimizing reaction conditions to achieve high yield and purity of 2-substituted 4-hydroxy-4-methyltetrahydropyrans, such as 2-isobutyl-4-hydroxy-4-methyltetrahydropyran, with controlled diastereomer ratios and reduced by-product formation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If conventional acidic catalysts (mineral acids, sulfonic acids) are used for the reaction of isoprenol with aldehydes, then the reaction can proceed, but by-product formation increases and manufacturing precision deteriorates

Engineering Contradiction:
Improvereaction feasibilityVSAvoidproduct purity
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The patent introduces a solid acid catalyst as an intermediary substance that mediates the reaction between isoprenol and aldehydes. This solid acid catalyst provides the necessary acidic environment for reaction while being easily separable from the liquid products, thus preventing by-product formation and improving product purity without compromising reaction feasibility.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent replaces conventional liquid mineral acids and sulfonic acids with a solid acid catalyst system. This substitution eliminates the need for complex separation and purification steps required when using liquid acids, thereby improving manufacturing precision while maintaining ease of manufacture through simpler process operations.

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

2Productivity

If the reaction is carried out with conventional catalysts and conditions, then production can proceed, but yield and productivity are insufficient

Engineering Contradiction:
Improveproduction rateVSAvoidproduct yield
Core Design Contradiction:
ProductivityVSQuantity of substance

Solution Approach 1:

The patent optimizes reaction parameters including temperature (20-40°C), catalyst amount (0.1-5 wt%), and molar ratios of reactants to achieve maximum yield and productivity. By carefully controlling these parameters, the reaction proceeds efficiently with high conversion rates and minimal by-products, simultaneously improving both productivity and quantity of substance.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs a continuous reaction process where isoprenol and aldehyde react continuously in the presence of the solid acid catalyst. This continuous operation maintains optimal reaction conditions throughout the process, ensuring sustained high productivity and maximum product yield without interruption or loss of reaction efficiency.

Inventive Principle:
Principle #20Continuity of useful action

3Ease of manufacture

If aqueous acidic catalyst solutions are used as disclosed in JP 2007-154069, then the reaction can proceed, but water content increases leading to by-product formation and reduced manufacturing precision

Engineering Contradiction:
Improvereaction feasibilityVSAvoiddiastereomer excess
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The patent uses a solid acid catalyst that can be easily separated and disposed of after use, replacing the need for large amounts of aqueous acidic solutions. This approach eliminates water-related by-products and maintains high diastereomer excess while keeping the process economically viable through simple catalyst replacement rather than complex water removal procedures.

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

Solution Approach 2:

The patent creates a localized acidic environment at the catalyst surface where the reaction occurs, rather than using water throughout the entire reaction medium. This localized acidification provides the necessary catalytic activity while preventing water-induced by-product formation, thereby maintaining high manufacturing precision and diastereomer excess.

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

The process effectively produces 2-substituted 4-hydroxy-4-methyltetrahydropyrans in high yield and purity, with minimal by-products, utilizing inexpensive starting materials and achieving favorable diastereomer ratios suitable for aroma chemical applications.

Implementation Method 1

reacting 3-methylbut-3-en-1-ol (isoprenol) with the corresponding aldehydes in the presence of a strongly acidic cation exchanger

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS8618315B2Method for producing 2-substituted tetrahydropyranols
Publication Date: 2013.12.31 BASF SE
  • US8618315B2 patent drawing
  • US8618315B2 patent drawing
  • US8618315B2 patent drawing

AI summary

The present invention relates to a process for the preparation of 2-substituted 4-hydroxy-4-methyltetrahydropyranols by reacting 3-methylbut-3-en-1-ol (isoprenol) with the corresponding aldehydes in the presence of a strongly acidic cation exchanger. Specifically, the present invention relates to a corresponding process for the preparation of 2-isobutyl-4-hydroxy-4-methyltetrahydropyran by reacting isoprenol with isovaleraldehyde.