Fatty Alcohol Purification via Soap Extraction

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Solution Overview

Problem

Current methods for purifying fatty alcohols from hydrogenation of fatty acid methyl esters are energy-intensive and result in unwanted by-products that are often wasted, rather than being reused as valuable materials.

Innovation Solution

A process involving the use of alkaline bases to convert alkyl and wax esters into alkaline soaps, followed by separation and treatment with mineral acids to release free fatty acids, effectively purifying fatty alcohols while producing a valuable by-product, reducing energy consumption and eliminating the need for overhead distillation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If standard fractionation and distillation operations are used to purify fatty alcohols, then purification is achieved, but energy consumption is high and technical equipment is extensive

Engineering Contradiction:
Improvepurification qualityVSAvoidenergy consumption
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The invention changes the chemical state of ester impurities by converting them into alkaline soaps through chemical reaction with alkaline bases, transforming the purification approach from physical separation to chemical conversion followed by phase separation

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention extracts ester impurities from the fatty alcohol mixture by converting them into alkaline soaps that form a separate aqueous phase, allowing removal through phase separation rather than energy-intensive distillation

Inventive Principle:
Principle #2Taking out (Extraction)

2Manufacturing precision

If overhead distillation is used to remove high boilers such as wax esters, then purification is achieved, but energy consumption increases and equipment complexity increases

Engineering Contradiction:
Improvepurification qualityVSAvoidequipment complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The invention changes the chemical nature of wax esters by converting them into alkaline soaps through saponification, transforming them from high-boiling point substances requiring complex distillation into water-soluble soaps that separate easily in aqueous phase

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention replaces the mechanical distillation system with a chemical conversion system followed by simple phase separation, eliminating the need for complex overhead distillation equipment

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

3Manufacturing precision

If standard distillation processes are used, then by-products are removed, but the waste material has no application and must be used as expensive fuel

Engineering Contradiction:
Improvepurification qualityVSAvoidwaste material value
Core Design Contradiction:
Manufacturing precisionVSLoss of substance

Solution Approach 1:

The invention converts the harmful ester impurities and wax esters into beneficial free fatty acids through acidification of the alkaline soap phase, transforming waste material into a saleable product

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

Solution Approach 2:

The invention recovers value from the by-products by converting esters into alkaline soaps and then into free fatty acids that can be sold, rather than discarding them as waste or using them only as fuel

Inventive Principle:
Principle #34Discarding and recovering

4Manufacturing precision

If multiple fractionation columns are used to separate low boilers and high boilers, then purification is achieved, but the process becomes more complex and expensive

Engineering Contradiction:
Improvepurification qualityVSAvoidprocess simplicity
Core Design Contradiction:
Manufacturing precisionVSEase of manufacture

Solution Approach 1:

The invention merges multiple separation functions into a single chemical treatment step that simultaneously handles both low boilers and high boilers through conversion to alkaline soaps and phase separation

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The invention changes the solubility parameters of impurities by converting them into alkaline soaps that preferentially partition into the aqueous phase, simplifying separation from the organic fatty alcohol phase

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 energy usage, minimizes product loss, and converts by-products into saleable free fatty acids, improving yield and reducing waste, while maintaining the color quality of the fatty alcohols.

Implementation Method 1

crude fatty alcohols comprising up to 70 % b.w. alkyl esters and/or wax esters are treated with alkaline bases in an amount sufficient to essentially convert said esters into alkaline soaps

Methodology Applied
Scientific EffectTransesterification: Chemical Bonding

Implementation Method 2

said alkaline soaps are separated from said fatty alcohols by extraction to produce a purified fraction of fatty alcohols and an aqueous soap phase

Methodology Applied
Scientific EffectExtraction: Liquid-Liquid Extraction

Implementation Method 3

said soap phase is treated with strong mineral acids in order to release the fatty acids from the soaps

Methodology Applied
Scientific EffectAcidification: Chemical Bonding

Data Source

PatentEP2522650B1Process for purifying crude fatty alcohols
Publication Date: 2016.03.09 COGNIS IP MANAGEMENT GMBH
  • EP2522650B1 patent drawingFigure 1~2

AI summary

Suggested is a process for simultaneously purifying fatty alcohols and obtaining a fraction of free fatty acids, which is characterised in that (a) crude fatty alcohols comprising up to 70 % b.w. alkyl esters and/or wax esters are treated with alkaline bases in an amount sufficient to essentially convert said esters into alkaline soaps, (b) said alkaline soaps are separated from said fatty alcohols by extraction to produce a purified fraction of fatty alcohols and an aqueous soap phase, and (c) said soap phase is treated with strong mineral acids in order to release the fatty acids from the soaps.