Fats and Oils Deodorization Using Adsorbent Pretreatment

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Solution Overview

Problem

Conventional deodorization processes for refining fats and oils often result in the production of unwanted by-products, particularly glycidol fatty acid esters, which can impair the taste, flavor, and hue of diacylglycerols-rich oils, especially when performed at high temperatures, while low-temperature processes fail to adequately improve sensory qualities.

Innovation Solution

A method involving preliminary treatment of fats and oils with an adsorbent, such as activated clay, followed by deodorization with steam distillation under specific temperature and time conditions to minimize by-product formation, thereby enhancing the taste, flavor, and hue of the refined oils.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If deodorization is performed at high temperature, then taste and flavor are improved, but by-products such as glycidol fatty acid esters increase

Engineering Contradiction:
Improvetaste and flavor qualityVSAvoidby-product formation
Core Design Contradiction:
Manufacturing precisionVSObject-generated harmful factors

Solution Approach 1:

The patent applies preliminary action by conducting decolorization treatment with a porous adsorbent before deodorization. This preliminary step removes impurities that would otherwise react during high-temperature deodorization to form harmful by-products, enabling effective deodorization at lower temperatures without compromising taste and flavor quality.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent introduces a porous adsorbent as an intermediary substance between the crude oil and the deodorization process. This adsorbent mediates by absorbing unwanted components and coloring matter, thereby preventing their conversion into harmful by-products during subsequent heating while still allowing effective removal of odor components.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If deodorization temperature is increased, then odor components are removed more effectively, but glycidol fatty acid esters are produced

Engineering Contradiction:
Improvedeodorization efficiencyVSAvoidglycidol fatty acid ester formation
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent applies preliminary action by conducting decolorization treatment with a porous adsorbent before deodorization. This preliminary step removes impurities that would otherwise react during high-temperature deodorization to form harmful by-products, enabling effective deodorization at lower temperatures without compromising taste and flavor quality.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent applies parameter changes by optimizing the deodorization temperature to be 200°C or lower, and by controlling the sequence of operations (decolorization first, then deodorization). These parameter changes maintain high deodorization efficiency while preventing the formation of glycidol fatty acid esters that occur at higher temperatures.

Inventive Principle:
Principle #35Parameter changes

3Reliability

If conventional deodorization is performed, then edible oil quality is improved, but by-products impair taste and flavor

Engineering Contradiction:
Improveedible oil qualityVSAvoidtaste and flavor quality
Core Design Contradiction:
ReliabilityVSManufacturing precision

Solution Approach 1:

The patent applies preliminary action by conducting decolorization treatment with a porous adsorbent before deodorization. This preliminary step removes impurities that would otherwise react during high-temperature deodorization to form harmful by-products, enabling effective deodorization at lower temperatures without compromising taste and flavor quality.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent introduces a porous adsorbent as an intermediary substance between the crude oil and the deodorization process. This adsorbent mediates by absorbing unwanted components and coloring matter, thereby preventing their conversion into harmful by-products during subsequent heating while still allowing effective removal of odor components.

Inventive Principle:
Principle #24Intermediary (Mediator)

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 approach effectively reduces the production of by-products like glycidol fatty acid esters, resulting in refined fats and oils with improved taste, flavor, and hue, while maintaining high diacylglycerol content, thus meeting consumer demands for higher-quality edible oils.

Implementation Method 1

treating fats and oils by bringing the fats and oils into contact with an adsorbent

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 2

treating the fats and oils by bringing the fats and oils into contact with water vapor under at least one condition selected from the following conditions

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 3

treatment of so-called deodorization, in which the fats and oils are brought into contact with water vapor under reduced pressure at high temperature

Methodology Applied
Scientific EffectSteam distillation: Distillation

Data Source

PatentUS8927039B2Method for manufacturing refined fat or oil
Publication Date: 2015.01.06 KAO CORP
  • US8927039B2 patent drawing
  • US8927039B2 patent drawing

AI summary

Provided is a method for manufacturing refined fats and oils. Here fats and oils are brought into contact with an adsorbent and subsequently treated with water vapor under at least one condition of the following conditions. In condition I, the time for which the fats and oils are brought into contact with the water vapor in a temperature range of 175° C. to 205° C. for from 5 to 110 minutes. In condition 2, the fats and oils are brought into contact with the water vapor in a temperature range of 205° C. to 215° C. for from 5 to 50 minutes. In condition 3, the fats and oils are brought into contact with the water vapor in a temperature range of 215° C. to 230° C. for from 5 to 30 minutes.