Loop Reactor Slurry Cavitation Control

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Solution Overview

Problem

Current olefin polymerization processes in loop reactors face challenges in maintaining efficient operation, including cavitation issues and suboptimal polymerization conditions, which affect the properties and yield of polyolefins.

Innovation Solution

The process involves circulating a slurry of olefin monomers, a liquid diluent, catalyst, and polyolefin particles within a loop reactor under specific conditions, including controlled cavitation numbers, circulation velocities, and temperature and pressure ranges, to enhance polymerization efficiency and polyolefin particle suspension.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If circulation velocity is increased to improve polymerization efficiency, then productivity increases, but cavitation occurs causing harmful effects

Engineering Contradiction:
Improvepolymerization efficiencyVSAvoidcavitation
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent changes the operating parameters by controlling the cavitation number within a specific range (0.5 to 5.0) and maintaining Euler number above 4.0, along with specific temperature (38-121°C) and pressure (27-50 bar) conditions, to achieve optimal polymerization efficiency while preventing harmful cavitation effects

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent implements process control through continuous monitoring and adjustment of circulation velocity to maintain the cavitation number within the optimal range, using feedback mechanisms to balance productivity enhancement with cavitation prevention

Inventive Principle:
Principle #23Feedback

2Productivity

If solids content is increased to improve polymer yield, then productivity increases, but slurry viscosity increases making circulation difficult

Engineering Contradiction:
Improvepolymer yieldVSAvoidslurry circulation
Core Design Contradiction:
ProductivityVSEase of operation

Solution Approach 1:

The patent optimizes the balance between solids content and circulation velocity by maintaining specific dimensionless numbers (cavitation number 0.5-5.0, Euler number ≥4.0), allowing high solids content (improved yield) while managing slurry viscosity through controlled flow conditions

Inventive Principle:
Principle #35Parameter changes

3Temperature

If circulation velocity is increased to improve heat transfer, then temperature control improves, but energy consumption increases

Engineering Contradiction:
Improvetemperature controlVSAvoidenergy consumption
Core Design Contradiction:
TemperatureVSUse of energy by moving object

Solution Approach 1:

The patent achieves optimal temperature control by operating at specific cavitation numbers (0.5-5.0) and Euler numbers (≥4.0), which provide sufficient heat transfer through controlled circulation without excessive energy consumption, balancing thermal management with energy efficiency

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 approach allows for improved polymerization processes with reduced cavitation, increased solids content, and optimized reactor operation, leading to higher quality polyolefins with enhanced properties and reduced operational costs.

Implementation Method 1

the process has a cavitation number (Ca) of from 6 to 60

Methodology Applied
Scientific EffectCavitation: Cavitation

Data Source

PatentEP3574023B1Flow in a slurry loop reactor
Publication Date: 2020.11.18 CHEVRON PHILLIPS CHEMICAL COMPANY LP
  • EP3574023B1 patent drawingFigure 1
  • EP3574023B1 patent drawing
  • EP3574023B1 patent drawing

AI summary

Olefin polymerization processes are described herein. The processes generally include circulating a slurry including an olefin monomer selected from C2-C12 olefin monomers, a liquid diluent selected from C3-C7 alkanes, catalyst and polyolefin particles under polymerization conditions within a loop reactor. In one or more specific embodiments, in operation, the process has a cavitation number of from 6 to 60 and the polymerization conditions include a polymerization temperature of from 38°C to 121°C and a polymerization pressure of from 27 bar to 50 bar. In other embodiments, the process has a Euler Number (Eu) of at least (5).