Polybutene Separation via Distillation with Viscosity Control

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Solution Overview

Problem

Existing methods for separating polybutene from reaction solutions struggle with achieving high purity and efficient separation, particularly in reducing the residual content of specific solvents in the polymer.

Innovation Solution

A method involving the introduction of a polybutene solution containing halogenated and non-polar hydrocarbon solvents into a distillation column, where the solvents are separated from the polybutene, allowing for high purity separation and reduced energy consumption.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If a distillation column is used to separate polybutene from reaction solution, then separation purity is improved, but handling difficulty increases due to high viscosity

Engineering Contradiction:
Improveseparation purityVSAvoidhandling difficulty
Core Design Contradiction:
Manufacturing precisionVSEase of operation

Solution Approach 1:

The patent changes the physical parameters of the system by introducing a viscosity-reducing agent that lowers the viscosity of the polybutene solution from potentially very high values to within the range of 10-150 cp. This parameter change enables the high-viscosity material to be effectively handled in the distillation column while maintaining high separation purity through the distillation process

Inventive Principle:
Principle #35Parameter changes

2Ease of manufacture

If flash drum or devolatilizer is used to remove low-boiling point material, then equipment cost and handling ease are improved, but separation purity deteriorates

Engineering Contradiction:
Improveequipment costVSAvoidseparation purity
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The patent merges two separation approaches: first using a flash drum or devolatilizer for preliminary removal of low-boiling point solvents (achieving cost-effectiveness), then following with a distillation column for high-purity separation of polybutene. This combination achieves both low equipment cost and high separation purity

Inventive Principle:
Principle #5Merging (Combining)

3Manufacturing precision

If distillation column is used to achieve high purity separation, then separation efficiency is improved, but energy consumption increases

Engineering Contradiction:
Improveseparation purityVSAvoidenergy consumption
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The patent applies preliminary action by first removing the bulk of low-boiling point solvents using a flash drum or devolatilizer before subjecting the material to distillation. This preliminary removal reduces the energy burden on the distillation column, achieving high purity separation with reduced overall energy consumption

Inventive Principle:
Principle #10Preliminary action

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

The method effectively separates polybutene to high purity with reduced residual solvent content and lower energy consumption, addressing the inefficiencies of previous separation techniques.

Implementation Method 1

a distillation column may separate a mixture to high purity using the difference in boiling point

Methodology Applied
Scientific EffectDistillation: Distillation

Implementation Method 2

having a viscosity of 1 cp to 50 cp measured at 25° C. using a rotational viscometer

Methodology Applied
Scientific EffectRotational viscometry: Rotational Viscometer

Data Source

PatentUS12202924B2Method for separating polybutene
Publication Date: 2025.01.21 LG CHEM LTD
  • US12202924B2 patent drawing

AI summary

A method for separating polybutene, the method including: (1) introducing a polybutene solution into a distillation column, the solution including polybutene, a halogenated hydrocarbon solvent, and a non-polar hydrocarbon solvent and having a viscosity of 1 cp to 50 cp measured at 25° C. using a rotational viscometer; (2) collecting an upper stream including the halogenated hydrocarbon solvent and a portion of the non-polar hydrocarbon solvent from an upper portion of the distillation column, and collecting a lower stream including the polybutene and a remaining portion of the non-polar hydrocarbon solvent from a lower portion of the distillation column, where the lower stream has a viscosity of 10 cp to 150 cp; and (3) separating the remaining portion of the non-polar hydrocarbon solvent and the polybutene from the lower stream.