Pervaporation Membrane for Cyclohexanone Separation

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Conventional methods for synthesizing cyclohexanone result in low conversion rates and high by-product formation, leading to decreased selectivity and increased production of unwanted compounds, making it challenging to obtain high-purity cyclohexanone.

Innovation Solution

The use of a pervaporation technique with a poly(styrene-maleic anhydride-dihydropyrane) membrane, synthesized by cationic polymerization of styrene, maleic, and dihydropyrane monomers, to selectively separate cyclohexanone from a mixture of cyclohexane, cyclohexanol, and cyclohexanone, allowing for high-purity cyclohexanone extraction.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If conventional oxidation methods are used to synthesize cyclohexanone, then the process is simple and straightforward, but the conversion rate remains low (3-8%) and by-product formation increases significantly

Engineering Contradiction:
Improvesimplicity of synthesis processVSAvoidconversion rate of cyclohexane
Core Design Contradiction:
Ease of manufactureVSProductivity

Solution Approach 1:

The patent introduces a pervaporation membrane as an intermediary component that selectively separates cyclohexanone from the reaction mixture. This membrane acts as a mediator between the oxidation reaction and product collection, enabling continuous removal of cyclohexanone while maintaining simple oxidation conditions. The membrane's selective permeability allows cyclohexanone to pass through while retaining cyclohexane and other by-products, thus resolving the contradiction between process simplicity and conversion efficiency.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent changes the physical state and separation parameters by implementing pervaporation technology. By controlling temperature, pressure, and membrane permeability parameters, the system achieves high conversion rates without increasing reaction complexity. The selective permeation parameters of the membrane allow differentiation between cyclohexanone and other components, enabling efficient separation and continuous production.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If conversion of cyclohexane is increased above 3-8% using conventional methods, then more cyclohexanone is produced, but selectivity decreases and further oxidation into by-products occurs

Engineering Contradiction:
Improvequantity of cyclohexanone producedVSAvoidselectivity of cyclohexanone
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent applies extraction principle by continuously removing cyclohexanone from the reaction mixture through the pervaporation membrane. This selective extraction prevents further oxidation of cyclohexanone into by-products while allowing the oxidation reaction to proceed at high conversion levels. The membrane effectively extracts cyclohexanone as it forms, maintaining high selectivity even at elevated conversion rates where conventional methods would produce excessive by-products.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The pervaporation membrane performs preliminary separation action immediately as cyclohexanone is formed in the oxidation reaction. By preemptively separating the desired product before further oxidation can occur, the system maintains high selectivity. This preliminary action prevents the formation of over-oxidized by-products while enabling continuous high-yield production.

Inventive Principle:
Principle #10Preliminary action

3Ease of manufacture

If conventional separation methods are used after oxidation, then the process follows traditional procedures, but high-purity cyclohexanone is difficult to obtain due to mixture complexity

Engineering Contradiction:
Improveadherence to traditional proceduresVSAvoidpurity of cyclohexanone
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The patent replaces complex mechanical separation systems (such as distillation columns, multiple extraction stages) with a single pervaporation membrane system. This substitution maintains procedural simplicity while achieving superior separation performance. The membrane's molecular-level selectivity provides high-purity cyclohexanone separation without requiring complex equipment or multiple processing stages, thus resolving the contradiction between traditional simplicity and modern purity requirements.

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

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 achieves high-purity cyclohexanone production with enhanced yield in an environmentally friendly process, suitable for further synthesis reactions like caprolactam polymerization, while minimizing by-product formation.

Implementation Method 1

separating the cyclohexanone from the mixture by pervaporation using a poly(styrene-maleic anhydride-dihydropyrane) pervaporation membrane

Methodology Applied
Scientific EffectPervaporation: Pervaporation

Implementation Method 2

The cyclohexanone can be extracted selectively and immediately through the pervaporation membrane

Methodology Applied
Scientific EffectPermeation: Permeation

Data Source

PatentUS10865175B1Method of synthesizing cyclohexanone
Publication Date: 2020.12.15 KING SAUD UNIVERSITY
  • US10865175B1 patent drawing
  • US10865175B1 patent drawing

AI summary

A method of synthesizing cyclohexanone can include oxidation of cyclohexane to produce a mixture including cyclohexanone, cyclohexanol, and cyclohexane, and separating cyclohexanone from the mixture using a pervaporation method. The pervaporation method includes contacting the mixture with a first side of a poly(styrene-maleic anhydride-dihydropyrane) membrane and receiving the cyclohexanone from a second side of the poly(styrene-maleic anhydride-dihydropyrane) membrane as a low-pressure vapor. The method can be performed in a pervaporation unit including a reactant portion for receiving the cyclohexane, a permeate portion for receiving the cyclohexanone, and a poly(styrene-maleic anhydride-dihydropyrane) membrane separating the reactant portion from the permeate portion.