Phenol Distillation Column Reflux Ratio Control

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Solution Overview

Problem

Phenol production plants face inefficiencies and increased impurity levels due to overloading of distillation columns, leading to reduced quality and commercial value of phenol products, particularly with the formation and removal of hydroxyacetone, which is difficult and costly to remove using existing methods.

Innovation Solution

A method involving the separation of acetone in an evaporator unit, recycling and bypassing a portion of it to reduce the reflux ratio in the distillation column, and maintaining a determined temperature profile to enhance hydroxyacetone removal, thereby reducing impurity levels and increasing column capacity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If the distillation column is overloaded to increase output, then productivity increases, but manufacturing precision deteriorates due to increased impurity levels

Engineering Contradiction:
Improvecolumn outputVSAvoidphenol purity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent divides the acetone removal process into two stages: first removing most acetone in the distillation column, then removing remaining acetone and hydroxyacetone in a separate extraction column using water as solvent. This segmentation allows the distillation column to operate at high capacity while the extraction column ensures high purity, resolving the contradiction between productivity and manufacturing precision.

Inventive Principle:
Principle #1Segmentation

2Manufacturing precision

If conventional hydroxyacetone removal methods are used, then manufacturing precision improves, but device complexity increases

Engineering Contradiction:
Improvehydroxyacetone removal efficiencyVSAvoidpurification system complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent uses water as a homogeneous solvent for extracting hydroxyacetone from the phenol stream. This simple, homogeneous extraction system replaces complex chemical treatment methods, achieving effective hydroxyacetone removal while minimizing device complexity and avoiding the need for multiple chemical reagents and treatment units.

Inventive Principle:
Principle #33Homogeneity

3Manufacturing precision

If conventional hydroxyacetone removal methods are used, then manufacturing precision improves, but loss of substance increases

Engineering Contradiction:
Improvehydroxyacetone removal efficiencyVSAvoidcumene recycling cost
Core Design Contradiction:
Manufacturing precisionVSLoss of substance

Solution Approach 1:

The patent uses water to extract hydroxyacetone from the phenol stream, and then recycles the water back to the distillation column. This self-service approach eliminates the need for additional chemical reagents and minimizes material loss, as the water acts as both extraction medium and process utility, avoiding the need for expensive cumene recycling that would be required with alternative removal methods.

Inventive Principle:
Principle #25Self-service

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 significantly reduces hydroxyacetone and alpha-methylstyrene levels in the phenol product, improving the quality and efficiency of phenol production by decreasing the reflux ratio and volumetric flow rate, while increasing the production capacity of the distillation column.

Implementation Method 1

separating a first portion of acetone from a phenol product stream in an evaporator unit

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 2

separating the distillation feed stream into a bottom stream and an overhead stream

Methodology Applied
Scientific EffectDistillation: Distillation

Data Source

PatentUS20240010588A1Method for producing phenol
Publication Date: 2024.01.11 SABIC GLOBAL TECHNOLOGIES BV
  • US20240010588A1 patent drawing
  • US20240010588A1 patent drawing

AI summary

A method of separating phenol can include: separating a first portion of acetone from a product stream in an evaporator unit, wherein the first portion of the acetone includes recycle acetone and bypass acetone; recycling the recycle acetone; withdrawing a bottom fraction from the evaporator unit; neutralizing the bottom fraction to form a distillation feed stream that is directed to a distillation column; separating the distillation feed stream into a bottom stream and an overhead stream, the bottom stream including a crude phenol fraction; passing the overhead stream through a condenser to produce a distillate as a crude acetone fraction, and wherein reflux ratio of the distillation column is less than or equal to 0.40, with the reflux ratio a ratio of a weight of a reflux to distillate weight; and directing the bypass acetone around the distillation column.