Extractive Distillation of Phenol and Cyclohexanone Using Diol Solvents

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Solution Overview

Problem

The production of phenol via the cyclohexylbenzene route faces challenges due to the formation of an azeotropic mixture with cyclohexanone, requiring alternative separation methods like extractive distillation, where solvents such as diols and glycols can react with cyclohexanone to form hemiketals and enol-ethers, affecting separation efficiency.

Innovation Solution

The use of diols and glycols with non-adjacent hydroxyl groups as solvents in extractive distillation processes to separate phenol and cyclohexanone, where hemiketals and enol-ethers are formed, allowing for effective separation by altering the relative volatilities of the components.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If extractive distillation is used to separate phenol and cyclohexanone, then separation efficiency is improved, but solvents react with cyclohexanone to form hemiketals and enol-ethers causing side reactions

Engineering Contradiction:
Improveseparation efficiencyVSAvoidside reactions
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent introduces a specific solvent (ethylene glycol) as an intermediary that mediates the separation process. The solvent forms hemiketals and enol-ethers with cyclohexanone, which are then separated through distillation. This intermediary approach enables effective separation while managing the side reactions through controlled conditions and subsequent hydrolysis steps.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent utilizes parameter changes by controlling temperature, pressure, and solvent-to-feed ratio during extractive distillation. By adjusting these parameters, the relative volatility between phenol and cyclohexanone is modified, enabling separation. The parameters are optimized to minimize unwanted side reactions while maintaining separation efficiency.

Inventive Principle:
Principle #35Parameter changes

2Device complexity

If simple distillation is used to separate phenol and cyclohexanone, then process complexity is reduced, but separation purity is insufficient due to azeotropic mixture

Engineering Contradiction:
Improveprocess complexityVSAvoidseparation purity
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

The patent employs an extractive distillation process where a solvent acts as an intermediary to break the azeotropic mixture. The solvent selectively interacts with one component (cyclohexanone), altering the relative volatilities and enabling separation that simple distillation cannot achieve. This approach maintains reasonable process complexity while significantly improving separation purity.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Productivity

If diols and glycols are used as solvents in extractive distillation, then separation effectiveness is improved, but hemiketal and enol-ether formation affects separation efficiency

Engineering Contradiction:
Improveseparation effectivenessVSAvoidcyclohexanone loss
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The patent performs preliminary action by pre-mixing the solvent with the phenol-cyclohexanone mixture before distillation. This allows the solvent to interact with cyclohexanone and form hemiketals/enol-ethers under controlled conditions, facilitating subsequent separation. The preliminary mixing optimizes the separation effectiveness while minimizing cyclohexanone loss through controlled reaction conditions.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent converts the harmful side reaction (hemiketal and enol-ether formation) into a beneficial separation mechanism. By allowing controlled reaction between the solvent and cyclohexanone, the process creates distinct chemical species with different volatilities, enabling effective separation. The reaction products are then hydrolyzed to recover cyclohexanone, converting what was initially a loss into a separable and recoverable form.

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

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 enables the efficient separation of phenol and cyclohexanone, avoiding undesirable side reactions and improving the purity of both products, with the solvent being recycled to maintain process efficiency.

Implementation Method 1

solvents such as diols and glycols can react with cyclohexanone to form hemiketals and enol-ethers

Methodology Applied
Scientific EffectHemiketal formation: Chemical Bonding

Implementation Method 2

solvents such as diols and glycols can react with cyclohexanone to form hemiketals and enol-ethers

Methodology Applied
Scientific EffectEnol-ether formation: Chemical Bonding

Implementation Method 3

extractive distillation process for separating a mixture of phenol and cyclohexanone

Methodology Applied
Scientific EffectExtractive distillation: Distillation

Data Source

PatentUS9464020B2Process for producing phenol and cyclohexanone
Publication Date: 2016.10.11 EXXONMOBIL CHEMICAL PATENTS INC
  • US9464020B2 patent drawing
  • US9464020B2 patent drawing
  • US9464020B2 patent drawing

AI summary

In a process for separating a mixture comprising cyclohexanone and phenol, at least a portion of the mixture is distilled in the presence of a solvent including at least two alcoholic hydroxyl groups attached to non-adjacent saturated carbon atoms and at least one hemiketal defined by the formula (I) or the formula (II):wherein R1, the same or different at each occurrence, is independently an alkylene group having from 2 to 10 carbon atoms, R2 is an alkylene group having from 4 to 10 carbon atoms, and R3 is hydrogen or the following group:and/or an enol-ether derived from the hemiketal defined by the formula (I) or the formula (II), wherein the total concentration of the hemiketal and the enol-ether, expressed in terms of weight percentage on the basis of the total weight of the feed to the distilling step (a), is at least 0.01%.