Internal Olefin Sulfonate Production via Low-Temperature Shear Neutralization

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Solution Overview

Problem

Conventional methods for producing internal olefin sulfonates are insufficient in preventing the by-production of internal olefins and inorganic salts, which affects the quality and performance of the surfactant.

Innovation Solution

A method involving a sulfonating step with sulfur trioxide, followed by a neutralizing step where the sulfonated internal olefin is mixed with an aqueous alkaline solution at 40°C or lower and subjected to shearing force to reduce oil droplet size to 10 µm or less, and a hydrolyzing step to produce a high-quality internal olefin sulfonate with reduced impurities.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional sulfonation method is used, then internal olefin sulfonate is produced, but internal olefins and inorganic salts are by-produced affecting quality

Engineering Contradiction:
Improvepurity of internal olefin sulfonateVSAvoidby-production of internal olefins and inorganic salts
Core Design Contradiction:
Manufacturing precisionVSObject-generated harmful factors

Solution Approach 1:

The patent applies parameter changes by controlling the neutralization temperature at 40°C or lower and using high-shearing force agitation to achieve fine emulsification with oil droplet diameters of 10 μm or less. These parameter optimizations prevent reverse reactions of β-sultone, thereby reducing by-production of internal olefins and inorganic salts while improving product purity

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs preliminary anti-action by pre-controlling the neutralization conditions (temperature ≤40°C and high shearing force) to prevent the reverse reaction of β-sultone before it can generate harmful by-products. This proactive approach eliminates the formation of internal olefins and inorganic salts rather than treating them after formation

Inventive Principle:
Principle #9Preliminary anti-action

2Productivity

If internal olefin sulfonate is produced by conventional method, then surfactant is obtained, but basic washing performances are insufficient

Engineering Contradiction:
Improveproduction of internal olefin sulfonateVSAvoidwashing performance and foaming property
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent improves washing performance and foaming properties by optimizing process parameters: maintaining neutralization temperature at 40°C or lower and applying high-shearing force agitation. These parameter changes produce an internal olefin sulfonate with superior performance characteristics compared to conventional methods

Inventive Principle:
Principle #35Parameter changes

3Ease of manufacture

If neutralization is performed without sufficient mixing, then process is simple, but reverse reactions of β-sultone occur generating impurities

Engineering Contradiction:
Improvesimplicity of neutralization processVSAvoidcontent of internal olefin and inorganic substance
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The patent applies dynamics by using high-shearing force agitation during neutralization to create intense mixing conditions. This dynamic approach ensures thorough contact between reactants, preventing reverse reactions of β-sultone and minimizing impurity formation while maintaining operational simplicity

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The patent employs preliminary action by pre-establishing optimal neutralization conditions (temperature control and high-shearing force agitation) before the reaction proceeds. This ensures that the neutralization process immediately achieves effective mixing, preventing reverse reactions and impurity generation from the outset

Inventive Principle:
Principle #10Preliminary action

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 effectively reduces the content of internal olefin and inorganic substances, resulting in a high-quality internal olefin sulfonate with improved washing performance and foaming properties.

Implementation Method 1

a sulfonating step of causing an internal olefin to react with sulfur trioxide to yield a sulfonated internal olefin

Methodology Applied
Scientific EffectSulfonation: Chemical Bonding

Implementation Method 2

a neutralizing step of mixing the resultant sulfonated internal olefin with an aqueous alkaline solution at 40°C or lower to yield a mixture

Methodology Applied
Scientific EffectNeutralization: Chemical Bonding

Implementation Method 3

applying shearing force to the mixture at an agitating speed of 5 m/s or more until the particle diameter of oil droplets of an oily product of the mixture turns to 10 μm or less

Methodology Applied
Scientific EffectShear stress: Shear Stress

Implementation Method 4

mixing the resultant sulfonated internal olefin with an aqueous alkaline solution at 40°C or lower

Methodology Applied
Scientific EffectCooling: Cooling

Implementation Method 5

a hydrolyzing step of hydrolyzing the resultant neutralized product

Methodology Applied
Scientific EffectHydrolysis: Hydrolysis

Data Source

PatentEP3088386B1Method for producing internal olefin sulfonate
Publication Date: 2021.07.28 KAO CORP

AI summary

The present invention provides a method for producing a high-quality internal olefin sulfonate in which the content of any internal olefin and inorganic substance is small. This method for producing an internal olefin sulfonate, comprising: a sulfonating step of causing an internal olefin to react with sulfur trioxide to yield a sulfonated internal olefin; a neutralizing step of mixing the resultant sulfonated internal olefin with an aqueous alkaline solution at 40°C or lower to yield a mixture, and applying shearing force to the mixture until the particle diameter of oil droplets of an oily product of the mixture turns to 10 µm or less to yield a neutralized product; and a hydrolyzing step of hydrolyzing the resultant neutralized product.