Vanillin Purification via Fractional Crystallization

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Solution Overview

Problem

Current vanillin purification processes, especially those involving biotechnological methods, face challenges in achieving high energy efficiency, preserving organoleptic properties, and maintaining yield due to the need for multiple purification steps and equipment sizing issues, particularly when dealing with impurities with similar boiling points.

Innovation Solution

A process that includes biomass separation, liquid/liquid extraction, solvent concentration, boiling point separation, and crystallization steps to efficiently purify vanillin or derivatives, optimizing yield and energy use while preserving organoleptic qualities.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If multiple purification steps are used to improve organoleptic properties, then purity and organoleptic quality are improved, but overall yield decreases

Engineering Contradiction:
Improveorganoleptic qualityVSAvoidoverall yield
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The invention changes the parameter of purification method from conventional multi-step chemical purification to a single-step fractional crystallization process. By controlling crystallization parameters (temperature, solvent composition, cooling rate), the process achieves both high organoleptic quality and high yield (>80%) simultaneously, resolving the contradiction between purification quality and productivity

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention utilizes phase transition (crystallization) as the core purification mechanism. By controlling the phase transition of vanillin from dissolved state to crystalline state through temperature and solvent composition adjustments, impurities are excluded from the crystal lattice, achieving high organoleptic quality while maintaining high recovery yield

Inventive Principle:
Principle #36Phase transitions

2Manufacturing precision

If liquid/liquid extraction with large amounts of solvents is used to improve purity, then purification effectiveness is improved, but energy efficiency deteriorates

Engineering Contradiction:
Improvepurification effectivenessVSAvoidenergy efficiency
Core Design Contradiction:
Manufacturing precisionVSUse of energy by stationary object

Solution Approach 1:

The invention extracts only the essential purification function through fractional crystallization, eliminating the need for large amounts of extraction solvents. By taking out the crystallization step from the conventional multi-step process, the method achieves effective purification with minimal solvent use and lower energy consumption for solvent recovery

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The invention uses a minimal amount of solvent as an intermediary to facilitate crystallization, rather than using large amounts of solvents for liquid/liquid extraction. This intermediary approach enables effective purification while dramatically reducing the energy required for solvent handling and recovery

Inventive Principle:
Principle #24Intermediary (Mediator)

3Manufacturing precision

If distillation equipment is sized to separate vanillin from impurities with similar boiling points, then separation efficiency is improved, but equipment complexity and residence time increase

Engineering Contradiction:
Improveseparation efficiencyVSAvoidequipment complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The invention replaces the mechanical distillation system with a crystallization-based separation system. Instead of relying on boiling point differences and complex distillation equipment, the method uses solubility differences and controlled crystallization to achieve separation, dramatically simplifying equipment while maintaining high separation efficiency for impurities with similar boiling points

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

4Manufacturing precision

If residence time in distillation equipment is extended to improve separation, then separation efficiency is improved, but vanillin degradation increases due to high-temperature instability

Engineering Contradiction:
Improveseparation efficiencyVSAvoidvanillin stability
Core Design Contradiction:
Manufacturing precisionVSReliability

Solution Approach 1:

The invention changes the operational parameters from high-temperature distillation to low-temperature crystallization. By controlling temperature and solvent composition during crystallization, the process achieves effective separation without subjecting vanillin to high temperatures that cause degradation, thereby maintaining both separation efficiency and vanillin stability

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention converts the potential harm of high-temperature processing into benefit by using controlled low-temperature crystallization. The slow crystallization process naturally achieves high separation efficiency without the need for extended high-temperature residence time, thus preventing vanillin degradation while maintaining purification effectiveness

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

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 achieves high purity vanillin with improved yield and energy efficiency, maintaining excellent organoleptic properties, and reduces equipment complexity by effectively separating vanillin from impurities through a multi-step purification approach.

Implementation Method 1

at least one step of liquid/liquid extraction of the aqueous stream (A1) comprising vanillin or derivatives thereof, said extraction step allowing the separation of an aqueous stream (A2) and an organic stream (O1) comprising vanillin or derivatives thereof

Methodology Applied
Scientific EffectLiquid-liquid extraction: Liquid-Liquid Extraction

Implementation Method 2

at least one step of concentrating the organic stream (O1) to obtain an organic stream (O2) in which compounds with a boiling point lower than that of vanillin or derivatives thereof are separated from said organic stream (O1)

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 3

at least one step of crystallizing the vanillin or derivatives thereof contained in the stream (O3)

Methodology Applied
Scientific EffectCrystallization: Crystallisation

Data Source

PatentUS20240140896A1Process for the purification of vanillin or a vanillin derivative obtained by a biotechnological process
Publication Date: 2024.05.02 RHODIA OPERATIONS SAS
  • US20240140896A1 patent drawing
  • US20240140896A1 patent drawing

AI summary

The present invention relates to a process for purifying a fermentation must (M), obtained via a biotechnological process, comprising biomass and vanillin or derivatives thereof, said purification process comprising:(a) a step of separating the biomass of a fermentation must (M) from an aqueous stream (A1) comprising vanillin or derivatives thereof,(b) at least one step of liquid/liquid extraction of the aqueous stream (A1) comprising vanillin or derivatives thereof, said extraction step allowing the separation of an aqueous stream (A2) and an organic stream (O1) comprising vanillin or derivatives thereof,(c) at least one step of concentrating the organic stream (O1) to obtain an organic stream (O2) in which compounds with a boiling point lower than that of vanillin or derivatives thereof are separated from said organic stream (O1),(d) at least one step in which compounds with a boiling point higher than that of vanillin or derivatives thereof are separated from an organic stream (O2) comprising vanillin or derivatives thereof to obtain a stream (O3),(e) at least one step of crystallizing the vanillin or derivatives thereof contained in the stream (O3).