Hexene Separation via Optimized Distillation Reflux

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Conventional methods for isolating hexene from hydrocarbon mixtures result in significant impurities, requiring costly and inefficient purification procedures.

Innovation Solution

A method involving a distillation column with a reflux ratio of 1.35 to 1.40, where a light fraction comprising 1-hexene and 1-butene is distributed to the top and a heavy fraction comprising 1-octene and toluene is distributed to the bottom, allowing for the withdrawal of a top product with less than 1 ppm toluene impurity, operated at 80 to 200°C and 0.3 to 1 MPa.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional distillation methods are used to isolate hexene from hydrocarbon mixtures, then hexene can be separated from the mixture, but significant impurities remain in the product requiring additional costly purification procedures

Engineering Contradiction:
Improvehexene purityVSAvoidpurification procedure complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent applies parameter changes by optimizing the reflux ratio to a specific range (1.35-1.40) and controlling distillation temperature (80-200°C) and pressure (0.3-1 MPa) to achieve high-purity hexene separation in a single distillation step, eliminating the need for additional purification equipment and procedures

Inventive Principle:
Principle #35Parameter changes

2Manufacturing precision

If conventional distillation methods are used to isolate hexene, then hexene can be separated from the mixture, but additional costly and inefficient purification procedures are required

Engineering Contradiction:
Improvehexene purityVSAvoidpurification efficiency
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

By optimizing distillation parameters including reflux ratio (1.35-1.40), temperature (80-200°C), and pressure (0.3-1 MPa), the process achieves high-purity hexene separation in a single step, significantly improving purification efficiency and eliminating the need for multiple processing stages

Inventive Principle:
Principle #35Parameter changes

3Manufacturing precision

If conventional distillation methods are used to isolate hexene, then hexene can be separated from the mixture, but costly additional processing is required

Engineering Contradiction:
Improvehexene purityVSAvoidprocessing cost
Core Design Contradiction:
Manufacturing precisionVSLoss of energy

Solution Approach 1:

The optimized distillation process with reflux ratio of 1.35-1.40 and controlled temperature-pressure conditions achieves high-purity hexene separation in a single step, reducing energy consumption and processing costs by eliminating the need for additional purification equipment and operations

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 method produces hexene with minimal impurities, reducing the need for additional purification steps and saving resources, while maintaining high purity and commercial value in the petrochemical industry.

Implementation Method 1

passing a feed stream comprising 1-hexene, 1-octene, 1-butene, water, and toluene through a distillation column

Methodology Applied
Scientific EffectDistillation: Distillation

Data Source

PatentEP3397607B1Method of separating hexene
Publication Date: 2022.12.28 SABIC GLOBAL TECHNOLOGIES BV
  • EP3397607B1 patent drawingFigure 1
  • EP3397607B1 patent drawingFigure 2

AI summary

A method of producing hexene includes: passing a feed stream comprising C1 to C24 hydrocarbons through a distillation column, wherein a reflux ratio of the distillation column is greater than or equal to 1.33; distributing a light fraction comprising C4-C6 hydrocarbons to a top portion of the distillation column; distributing a heavy fraction comprising C8-C12 hydrocarbons to a bottom portion of the distillation column; and withdrawing a top product comprising hexene from the distillation column.