Limonene Oxidation Catalyst for Isomer Control

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Solution Overview

Problem

Current methods for producing p-2,8-menthadien-1-ol, p-1(7),8-menthadien-2-ol, and carveol from limonene are inefficient, requiring specialized photoreactors and expensive catalysts, leading to complex operations and odor/taste deviations, with difficulty in controlling reaction product ratios and recovering unreacted limonene.

Innovation Solution

A two-stage process using limonene and hydrogen peroxide in the presence of catalysts like sodium molybdate or lanthanum nitrate, followed by reduction with sodium sulfite, allowing for control over reaction conditions and product ratios, and enabling recovery of unreacted limonene in a standard chemical reactor.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If photochemical oxidation of limonene is used to produce p-2,8-menthadien-1-ol, p-1(7),8-menthadien-2-ol, and carveol, then the desired compounds are obtained with specific isomer ratios, but specialized photoreactor equipment is required which increases investment costs and operational complexity

Engineering Contradiction:
Improveisomer ratio controlVSAvoidphotoreactor equipment
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent changes the fundamental reaction parameters from photochemical to chemical oxidation conditions. By using hydrogen peroxide with metal catalysts (manganese, cobalt, iron, or tungsten salts) instead of light activation, the process eliminates photoreactor requirements while maintaining controlled product formation through catalyst selection and reaction condition optimization

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent replaces expensive, specialized photoreactor equipment with conventional, inexpensive chemical reactors. The catalysts used (metal salts) are relatively cheap and can be easily handled in standard equipment, significantly reducing both capital investment and operational complexity

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

2Manufacturing precision

If manganese(II)-substituted polyoxometalates are used as catalysts for limonene oxidation, then a specific isomer of p-2,8-menthadien-1-ol is produced, but the reaction takes many hours and yields only one isomer which causes odor and taste changes

Engineering Contradiction:
Improveisomer specificityVSAvoidreaction time
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The patent changes the catalyst system from highly specific polyoxometalates to metal salts that produce a mixture of isomers. This parameter change in catalyst type and composition allows for faster reaction times (completing in much shorter duration) and produces the desired isomer mixture that maintains the characteristic odor and taste profile

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

Instead of achieving complete isomer specificity, the patent accepts partial isomer formation (producing a mixture including the desired isomers). This partial action approach delivers the beneficial sensory properties while achieving much higher productivity and faster reaction completion

Inventive Principle:
Principle #16Partial or excessive action

3Productivity

If heterogeneous catalysts are used for limonene oxidation at 25°C to 120°C, then the reaction proceeds with moderate conversion, but the reaction time is approximately 24 hours and product ratio control is difficult

Engineering Contradiction:
Improvereaction temperature rangeVSAvoidproduct ratio control
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent optimizes reaction parameters including using pH 2-7 conditions, specific catalyst concentrations (0.01-10 mmol relative to limonene), and temperature ranges that favor faster reaction rates. These parameter adjustments enable both improved productivity and better control over the distribution of oxidation products

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs monitoring of reaction progress and product formation to adjust conditions for optimal product ratios. By tracking the oxidation process and modifying parameters such as hydrogen peroxide addition rate, temperature, and catalyst amount based on observed product distribution, the process achieves controllable product ratios while maintaining high productivity

Inventive Principle:
Principle #23Feedback

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 method produces high yields of the desired compounds with sensory properties matching photooxidation, is economically viable, and allows for flexible production based on demand, avoiding the need for expensive equipment and maintaining isomer ratios similar to photooxidation.

Implementation Method 1

the reaction of limonene with hydrogen peroxide in the presence of a catalyst selected from the group consisting of sodium molybdate, sodium molybdate dihydrate, sodium tungstate, sodium tungstate dihydrate, and lanthanum nitrate

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 2

followed by reduction with sodium sulfite

Methodology Applied
Scientific EffectReduction: Reduction

Data Source

PatentEP3095773B1Preparation of limonene derivatives
Publication Date: 2019.10.02 SYMRISE GMBH & CO KG

AI summary

The invention discloses a process for the oxidation of limonene comprising the reaction of limonene with hydrogen peroxide in the presence of a catalyst containing atoms and/or ions of at least one metal selected from the group consisting of molybdenum, tungsten, scandium, vanadium, titanium, lanthanum, zirconium, praseodymium, neodymium, samarium, europium, terbium, dysprosium, erbium or ytterbium, characterized in that the molecular weight of the catalyst is less than 2000 g/mol, preferably 1000 g/mol and particularly preferably less than 500 g/mol.