Dihydrolipoic Acid Multi-Stage Process Selectivity

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Solution Overview

Problem

Current synthetic routes for dihydrolipoic acid suffer from low selectivity, product mixtures, and the need for purification through distillation, which are inefficient and labor-intensive, especially in industrial-scale production.

Innovation Solution

A multi-stage process involving the reaction of 6,8-dichlorooctanoic acid ester with a mixture of sodium sulfide and sulfur in an alcoholic solvent at controlled temperatures and pressures, followed by reduction and pH adjustment, effectively suppressing the formation of by-products and polymers, allowing for a high space-time yield without intermediate isolation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional synthetic routes are used for dihydrolipoic acid, then the product can be obtained, but the selectivity is low and product mixtures are formed requiring complex purification

Engineering Contradiction:
ImproveselectivityVSAvoidpurification complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent applies parameter changes by optimizing reaction conditions including temperature ranges (80-130°C), pressure ranges (0.12-0.60 MPa), and solvent composition (alcoholic solvent mixtures) to achieve high selectivity for dihydrolipoic acid while suppressing by-product formation and polymerization, thereby simplifying purification requirements

Inventive Principle:
Principle #35Parameter changes

2Manufacturing precision

If distillation is used for purification of dihydrolipoic acid, then impurities can be removed, but the process becomes labor-intensive and inefficient

Engineering Contradiction:
ImprovepurityVSAvoidproduction efficiency
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The patent employs extraction methods using alcoholic solvent mixtures to selectively dissolve and separate dihydrolipoic acid from reaction by-products and polymers, replacing time-consuming distillation processes with more efficient liquid-liquid extraction that maintains high purity while improving production efficiency

Inventive Principle:
Principle #2Taking out (Extraction)

3Manufacturing precision

If multi-stage processes with intermediate isolation are used, then product quality can be controlled, but the production time and complexity increase

Engineering Contradiction:
Improveproduct quality controlVSAvoidproduction time
Core Design Contradiction:
Manufacturing precisionVSLoss of time

Solution Approach 1:

The patent combines multiple reaction stages and purification steps into a streamlined integrated process where intermediates are carried forward without isolation, and purification is achieved through selective extraction in the final stage, thereby reducing production time while maintaining product quality control

Inventive Principle:
Principle #5Merging (Combining)

4Quantity of substance

If radical addition of cyclohexanone to vinyl derivative is used, then dihydrolipoic acid can be synthesized, but the selectivity is low and by-products are formed

Engineering Contradiction:
ImproveyieldVSAvoidselectivity
Core Design Contradiction:
Quantity of substanceVSManufacturing precision

Solution Approach 1:

The patent changes reaction parameters including using specific temperature ranges (80-130°C), pressure conditions (0.12-0.60 MPa), and alcoholic solvent mixtures to optimize the radical addition reaction, achieving high selectivity for the desired product while minimizing by-product formation and maintaining good yield

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

This process significantly reduces by-product formation, enhances yield, and allows for the efficient production of dihydrolipoic acid on an industrial scale, enabling its conversion to alpha-lipoic acid or physiologically tolerable derivatives with improved efficiency.

Implementation Method 1

an ester of 6,8-dichlorooctanoic acid according to general formula (II) is reacted with a mixture comprising sodium sulfide and sulfur

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Implementation Method 2

in a second process stage the reaction mixture obtained from the first process stage is subjected to a reduction

Methodology Applied
Scientific EffectReduction: Reduction

Implementation Method 3

the reaction is carried out in an alcoholic solvent mixture at a temperature in the range of 80 °C to 130 °C and a pressure in the range of 0.12 MPa to 0.60 MPa

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 4

in a third process stage the reaction mixture resulting from the second process stage is adjusted to a pH value in the range of pH 1.5 to

Methodology Applied
Scientific EffectpH adjustment:

Data Source

PatentEP3573951B1Process for the preparaiton of dihydrolipoic acid
Publication Date: 2020.10.28 ALZCHEM TROSTBERG
  • EP3573951B1 patent drawing
  • EP3573951B1 patent drawing
  • EP3573951B1 patent drawing

AI summary

The present invention relates to a multi-step process for the production of dihydrolipoic acid, which can particularly be carried out as a one-pot reaction and without isolation of intermediates.