Dividing-Wall Distillation for Fatty Acid Fractionation

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Solution Overview

Problem

Existing methods for fractionating fatty acid mixtures, such as palm kernel and coconut fatty acids, require multiple distillation columns, leading to high energy consumption, large plot areas, and lower purity fractions.

Innovation Solution

The method involves using middle dividing-wall distillation columns to reduce the number of distillation columns required, allowing for continuous fractionation with improved purity and reduced energy consumption.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If multiple distillation columns are used to fractionate fatty acid mixtures, then the purity of fractions is improved, but the energy consumption increases

Engineering Contradiction:
Improvepurity of fatty acid fractionsVSAvoidenergy consumption
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The patent combines multiple distillation columns into a single dividing-wall distillation column that performs the function of multiple columns simultaneously. The dividing wall creates separate sections within one column, allowing multiple fractions (C6, C8, C10, C12, C14, C16, and C18+) to be obtained in a single continuous operation, thereby reducing energy consumption while maintaining high purity levels.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The dividing-wall column is segmented into multiple sections by the dividing wall, with each section dedicated to separating specific fatty acid fractions. This segmentation allows the single column to perform multiple separation tasks that would traditionally require separate columns, achieving both high purity and energy efficiency.

Inventive Principle:
Principle #1Segmentation

2Manufacturing precision

If multiple distillation columns are used to fractionate fatty acid mixtures, then the purity of fractions is improved, but the plot area required increases

Engineering Contradiction:
Improvepurity of fatty acid fractionsVSAvoidplot area
Core Design Contradiction:
Manufacturing precisionVSArea of stationary object

Solution Approach 1:

The patent merges multiple distillation columns into a single dividing-wall distillation column, significantly reducing the plot area required for the fractionation plant. The compact design of one column with internal dividing walls replaces what would traditionally require multiple separate columns spread across a large area.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The dividing wall structure creates nested separation sections within the single column body, allowing multiple fractionation functions to be nested within one physical structure. This nesting approach maximizes the use of vertical space and minimizes the horizontal footprint of the plant.

Inventive Principle:
Principle #7Nested doll (Nesting)

3Device complexity

If traditional distillation columns are used, then the process is simpler in design, but the operation is discontinuous due to campaign mode

Engineering Contradiction:
Improvedesign simplicityVSAvoidcontinuous operation capability
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The patent combines multiple distillation functions into a single continuous dividing-wall column operation, enabling continuous production of all fatty acid fractions simultaneously. This eliminates the need for campaign-mode operation where columns are sequentially taken offline for maintenance or product changeover, thereby improving productivity while maintaining operational simplicity.

Inventive Principle:
Principle #5Merging (Combining)

4Device complexity

If six distillation columns connected in series are used, then the number of columns is reduced, but the purities of fractions are lower than with seven columns

Engineering Contradiction:
Improvenumber of distillation columnsVSAvoidpurity of fatty acid fractions
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

The patent merges the separation functionality of six or seven columns into a single dividing-wall column with optimized internal structure. The dividing wall creates multiple theoretical stages within one column, providing sufficient separation efficiency to achieve high purities (C6: 99.5%, C8: 99.5%, C10: 99.5%, C12: 99.5%, C14: 99.5%, C16: 99.5%, C18+: 99.0%) while using fewer physical columns.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The patent changes the operational parameters and internal structure of the distillation column by introducing a dividing wall with specific configuration. This parameter change enables the single column to achieve separation efficiency equivalent to or better than multiple columns, maintaining high purity levels while reducing the number of columns required.

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 approach achieves high-purity fractions of fatty acids (up to 99.5% purity) while significantly reducing energy consumption and the required plot area, enabling a more efficient and compact fractionation process.

Implementation Method 1

This fractionation is usually performed by distillation, wherein 7 distillation columns are needed to obtain 7 fractions from palm kernel fatty acid

Methodology Applied
Scientific EffectDistillation: Distillation

Data Source

PatentUS20250171711A1Plant and process for fractionating fatty acid mixtures
Publication Date: 2025.05.29 SULZER MANAGEMENT AG
  • US20250171711A1 patent drawing
  • US20250171711A1 patent drawing
  • US20250171711A1 patent drawing

AI summary

A method for fractionating a crude composition comprising at least six fatty acids each having a different chain length into at least four fractions is provided. The method comprises feeding the crude composition into a first distillation column to obtain a first overhead fraction and a first bottom fraction, feeding the first bottom fraction to a second distillation column to obtain a second overhead fraction and a second bottom fraction, feeding the second bottom fraction to a third distillation column to obtain a third overhead fraction and a third bottom fraction, and feeding the third bottom fraction to a fourth distillation column to obtain a fourth overhead fraction, a fourth side fraction and a fourth bottom fraction. At least one of the first distillation column, the second distillation column and the third distillation column is a middle dividing-wall column, from which also at least two side fractions are obtained.