Effervescent Nozzle for Catalyst Injection in Olefin Polymerization

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Solution Overview

Problem

Existing nozzles for catalyst injection in olefin polymerization face challenges such as uneven catalyst distribution, accelerated polymer growth, and particle accumulation, leading to fouling and unpredictable reactor performance, especially with highly active catalysts that polymerize quickly and form agglomerates.

Innovation Solution

A nozzle design featuring a first conduit with a tapered section and an injection tip, surrounded by a second conduit with radially and axially spaced orifices, and a support member, which allows for controlled catalyst slurry and inert gas flow to prevent agglomeration and ensure uniform dispersion within the reactor.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If liquid catalyst is injected directly into the reactor, then catalyst injection is simple, but catalyst dispersal is uneven and polymer particles grow too large

Engineering Contradiction:
Improvenozzle structure complexityVSAvoidcatalyst dispersal uniformity
Core Design Contradiction:
Device complexityVSManufacturing precision

Solution Approach 1:

The nozzle divides the liquid catalyst stream into multiple smaller streams through multiple injection holes, and further atomizes them into droplets using compressed gas. This segmentation prevents uneven dispersal and controls particle growth by distributing catalyst more uniformly throughout the reactor.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Compressed gas is introduced as an intermediary substance between the liquid catalyst and the polymer particles. The gas atomizes the liquid catalyst into fine droplets and carries them into the reactor, improving dispersal uniformity while preventing direct contact that would cause rapid polymerization and particle growth.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If high concentration of catalyst is used to increase productivity, then polymer production increases, but particle agglomeration and fouling worsen

Engineering Contradiction:
Improvepolymer production rateVSAvoidparticle agglomeration and fouling
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

Compressed gas is used to atomize the liquid catalyst into fine droplets and transport them into the reactor. This pneumatic delivery method ensures that even at high catalyst concentrations, the catalyst is distributed as discrete droplets rather than a continuous stream, preventing particle agglomeration and fouling while maintaining high productivity.

Inventive Principle:
Principle #29Pneumatics and hydraulics

Solution Approach 2:

The physical state of catalyst delivery is changed from liquid stream to atomized droplets through compression and shearing forces. This parameter change in the catalyst delivery form allows higher catalyst concentrations to be used without causing agglomeration, as the droplet morphology prevents coalescence and subsequent particle growth.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If catalyst injection rate is increased to maintain production, then productivity is maintained, but particle size increases and fluidization is lost

Engineering Contradiction:
Improvecatalyst injection rateVSAvoidpolymer particle size
Core Design Contradiction:
ProductivityVSShape

Solution Approach 1:

The injection system segments the catalyst flow into multiple holes, each creating a separate stream that is further broken into droplets. This segmentation allows high total injection rates while maintaining small individual droplet sizes, preventing particle agglomeration and maintaining fluidization even at high productivity levels.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Compressed gas provides the mechanical energy to atomize the liquid catalyst into fine droplets at high injection rates. The pneumatic atomization ensures that increased catalyst injection rate does not lead to increased droplet size or particle agglomeration, thereby maintaining particle fluidization and preventing reactor shutdown.

Inventive Principle:
Principle #29Pneumatics and hydraulics

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 nozzle design ensures uniform and repeatable catalyst injection, controlling polymer growth and particle size, reducing fouling and reactor shutdowns by creating small droplets that are well dispersed in the fluidized bed, thereby maintaining consistent polymer production.

Implementation Method 1

The effervescent nozzle atomizes the liquid catalyst into fine droplets using compressed gas

Methodology Applied
Scientific EffectAtomization:

Implementation Method 2

uniform dispersion within the fluidized bed

Methodology Applied
Scientific EffectFluidization: Fluidisation

Implementation Method 3

A three-dimensional computational fluid dynamics (CFD) study was conducted to model the effervescent flow patterns within the nozzle

Methodology Applied
Scientific EffectEffervescent flow:

Implementation Method 4

The CFD simulations revealed that the tapered section and multiple orifices created effervescent flow patterns

Methodology Applied
Scientific EffectTurbulence: Turbulence

Data Source

PatentEP2076548B1Effervescent nozzle for catalyst injection and method for using this nozzle
Publication Date: 2019.08.14 UNIVATION TECH LLC
  • EP2076548B1 patent drawingFigure 1~1A
  • EP2076548B1 patent drawingFigure 2~4
  • EP2076548B1 patent drawingFigure 5

AI summary

A nozzle for catalyst injection for olefin polymerization is provided. In one or more embodiments the nozzle includes a first conduit including a body, a tapered section, and an injection tip. The nozzle also includes a second conduit having an inner surface and an outer surface. The first conduit is disposed about the second conduit defining a first annulus therebetween. The nozzle further includes a support member at least partially disposed about the outer surface of the first conduit defining a second annulus therebetween. The support member has a converging outer surface at a first end thereof.