Reactor Solvent Circulation for Faster Polymer Fouling Removal

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Solution Overview

Problem

The existing methods for cleaning oligomerization reactors of ethylene are inefficient, leading to prolonged reactor downtime, increased cleaning costs, and reduced production due to the accumulation of polymer fouling.

Innovation Solution

A reactor cleaning method involving the pressurization of a washing solvent container to 5 kg/cm2·g to 40 kg/cm2·g, supplying the washing solvent stream to the lower or side portions of the reactor, and circulating the solvent while maintaining the reactor temperature between 115° C. and 200° C.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional washing methods are used to clean polymer accumulation in the reactor, then the reactor can be cleaned, but the washing rate is low and downtime is prolonged

Engineering Contradiction:
Improvewashing rateVSAvoidreactor downtime
Core Design Contradiction:
ProductivityVSLoss of time

Solution Approach 1:

The patent applies parameter changes by optimizing the washing solvent circulation temperature (maintaining reactor temperature between 115-200°C) and pressure (5-40 kg/cm²·g) to enhance the washing rate. By controlling these parameters, the polymer accumulation is removed more efficiently, improving productivity while reducing the time the reactor remains non-operational.

Inventive Principle:
Principle #35Parameter changes

2Ease of manufacture

If conventional washing methods are used, then cleaning can be performed, but cleaning costs increase due to prolonged downtime

Engineering Contradiction:
Improvecleaning efficiencyVSAvoidcleaning time
Core Design Contradiction:
Ease of manufactureVSLoss of time

Solution Approach 1:

The patent implements continuous circulation of the washing solvent between the washing solvent container and the reactor. This continuous action ensures that the washing process operates efficiently without interruption, improving cleaning efficiency while minimizing the total time required for the cleaning operation, thereby reducing associated costs.

Inventive Principle:
Principle #20Continuity of useful action

3Productivity

If polymer accumulation is not removed, then the reactor can continue operating, but reaction stability deteriorates

Engineering Contradiction:
Improvecontinuous operationVSAvoidreaction stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent performs preliminary cleaning action by circulating the washing solvent to remove polymer accumulation before it significantly impacts reaction stability. This preventive maintenance approach allows the reactor to return to stable operation more quickly, maintaining both productivity and reliability by addressing fouling before it causes major performance degradation.

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

This method significantly improves the washing rate of the reactor, reduces downtime, lowers cleaning costs, and enhances reaction stability by effectively removing polymer accumulations.

Implementation Method 1

circulating a washing solvent stream between the washing solvent container and the reactor

Methodology Applied
Scientific EffectSolvation: Solvation

Implementation Method 2

pressurizing a washing solvent container to 5 kg/cm2·g to 40 kg/cm2·g using pressurized gas

Methodology Applied
Scientific EffectPressure increase: Pressure Increase

Implementation Method 3

maintaining a temperature of the reactor at 115° C. to 200° C.

Methodology Applied
Scientific EffectThermal heating: Heating

Data Source

PatentUS12343774B2Reactor cleaning method
Publication Date: 2025.07.01 LG CHEM LTD
  • US12343774B2 patent drawing
  • US12343774B2 patent drawing
  • US12343774B2 patent drawing

AI summary

A reactor cleaning method includes pressurizing a washing solvent container to 5 kg/cm2·g to 40 kg/cm2·g using pressurized gas; supplying a washing solvent stream from the washing solvent container to one or more of a lower portion or a side portion of the reactor to fill an inside of the reactor; and circulating the washing solvent stream between the washing solvent container and the reactor while maintaining a temperature of the reactor at 115° C. to 200° C.