Gas-Phase Polymerization Reactor Transport Section Design

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Solution Overview

Problem

The existing gas-phase polymerization reactors with interconnected zones face challenges in maintaining homogeneous polymer flow and preventing obstructions in the transport section connecting the downcomer and riser, leading to partial melting and clogging due to high friction and temperature conditions.

Innovation Solution

The reactor design includes a transport section that is shaped as a descending bend with a gas distribution grid extending along the bending section for an angle of at least 50°, ensuring optimal carrier gas distribution and reducing friction, and a control valve to adjust the polymer flow rate, preventing polymer agglomerates and ensuring regular transfer.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If a carrier gas is fed to the inlet of the transport section for pneumatic transfer, then the polymer flow rate from downcomer to riser is improved, but the friction between polymer and wall increases causing superficial melting and polymer chunk formation

Engineering Contradiction:
Improvepolymer flow rateVSAvoidfriction between polymer and wall
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The transport section is designed with a curved descending bend geometry rather than a straight pipe, allowing the polymer flow to follow a smoother path that reduces abrupt changes in direction and minimizes wall friction. The curved shape enables gentler contact between polymer particles and section walls throughout the descent.

Inventive Principle:
Principle #14Spheroidality (Curvature)

Solution Approach 2:

A gas distribution grid is introduced within the transport section to provide localized carrier gas distribution along the curved path. This ensures that carrier gas is available at multiple points along the transport section, maintaining polymer flowability without requiring excessive gas flow rates that would increase friction and melting.

Inventive Principle:
Principle #3Local quality

2Device complexity

If the transport section is designed as a straight pipe, then the structure is simpler, but the polymer flow becomes blocked due to high friction and temperature conditions

Engineering Contradiction:
Improvetransport section structureVSAvoidpolymer flow continuity
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

The transport section employs a curved descending bend design that replaces the straight pipe configuration. This curvature allows the polymer flow to transition smoothly from the downcomer to the riser, reducing abrupt directional changes and minimizing wall friction that would otherwise cause blocking and agglomerate formation.

Inventive Principle:
Principle #14Spheroidality (Curvature)

3Device complexity

If a gas distribution grid covers only the inlet of the transport section, then the device complexity is reduced, but the polymer flowability is not ensured due to partial blocking

Engineering Contradiction:
Improvegas distribution grid coverageVSAvoidpolymer flowability
Core Design Contradiction:
Device complexityVSEase of operation

Solution Approach 1:

The gas distribution grid is segmented into multiple zones along the curved transport section, with gas distribution outlets positioned at intervals along the bend. This segmentation ensures that carrier gas is distributed throughout the entire transport path, maintaining polymer flowability from the downcomer inlet through the curved section to the riser, and preventing blocking and agglomerate formation.

Inventive Principle:
Principle #1Segmentation

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 design enhances the operability and efficiency of the polymer transfer from the downcomer to the riser, maintaining polymer flowability and preventing clogging, thus ensuring continuous and homogeneous polymer circulation without partial melting or agglomerate formation.

Implementation Method 1

The transfer of polymer between dowcomer and riser is generally achieved by means of pneumatic transport, i.e. by feeding a carrier gas to the inlet of the transport section

Methodology Applied
Scientific EffectPneumatic transport:

Implementation Method 2

a second polymerization zone (denominated as 'the downcomer'), through which they flow in a densified form under the action of gravity

Methodology Applied
Scientific EffectGravity: Gravitation

Implementation Method 3

The polymer particles flow upwards through a first polymerization zone (denominated as 'the riser') under fast fluidization or transport conditions

Methodology Applied
Scientific EffectFast fluidization: Fluidisation

Data Source

PatentEP2613873B1Process and apparatus for the gas-phase polymerization of olefins
Publication Date: 2018.03.14 BASELL POLIOLEFINE ITALIA SRL
  • EP2613873B1 patent drawingFigure 1
  • EP2613873B1 patent drawingFigure 2
  • EP2613873B1 patent drawing

AI summary

A gas-phase polymerization reactor having interconnected polymerization zones comprising: - a riser through which the polymer particles flow upwards under fast fluidization conditions or transport conditions; -a dowcomer through which the polymer particles flow downward in a densified form under the action of gravity, the bottom of said downcomer being connected to the lower region of said riser by means of a transport section, said transport section being designed as a bend descending from the downcomer to the riser.