Slurry Bubble Column Reactor Catalyst Bed Re-suspension

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Solution Overview

Problem

Large slurry bubble column reactors experience high uplift forces during catalyst bed re-suspension, which can damage reactor internals, especially when using conventional methods that rely solely on gas flow to re-suspend settled catalyst beds.

Innovation Solution

Introducing a re-suspension liquid into the settled or slumped catalyst bed before or simultaneously with gas introduction, with the gas flow initially kept below 10 cm/s superficial velocity, and then increasing to above 10 cm/s once the bed is loosened, to reduce uplift forces and prevent damage to reactor internals.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of operation

If conventional gas flow methods are used to re-suspend settled catalyst beds, then the catalyst bed can be re-suspended, but high uplift forces are generated that can damage reactor internals

Engineering Contradiction:
Improvecatalyst bed re-suspensionVSAvoiduplift forces
Core Design Contradiction:
Ease of operationVSForce

Solution Approach 1:

The method introduces gas flow at a controlled initial rate below 10 cm/s before increasing to above 10 cm/s, allowing the catalyst bed to gradually transition from settled to fluidized state. This preliminary controlled action prevents sudden high uplift forces that would damage reactor internals while still achieving complete re-suspension of the catalyst bed

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The method changes the gas flow velocity parameter in a controlled sequence: first maintaining gas flow rate below 10 cm/s to minimize uplift forces, then increasing to above 10 cm/s to ensure complete re-suspension. This parameter transformation allows the system to achieve the desired catalyst bed fluidization while staying within safe force limits for reactor internals

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 method significantly reduces uplift forces during catalyst bed re-suspension, minimizing the risk of damaging reactor internals and allowing for safer and more efficient restarts of slurry bubble column reactors.

Implementation Method 1

introducing a flow of a re-suspension liquid into the settled or slumped bed to loosen the settled or slumped bed

Methodology Applied
Scientific EffectFluid penetration and particle disruption:

Implementation Method 2

fine solids (typically catalyst particles usually smaller than 200 microns) are kept in suspension in a liquid phase or medium mainly or completely by turbulence created as gas bubbles rise through a slurry bed inside the reactor

Methodology Applied
Scientific EffectGas-induced turbulence and fluidization: Fluidisation

Implementation Method 3

turbulence created as gas bubbles rise through a slurry bed inside the reactor

Methodology Applied
Scientific EffectBubble rise and turbulence creation: Turbulence

Implementation Method 4

passing gas at a superficial gas velocity above 10 cm/s through the liquid phase

Methodology Applied
Scientific EffectGas flow uplift force: Drag

Data Source

PatentUS11505749B2Method of operating a slurry bubble column reactor
Publication Date: 2022.11.22 SASOL TECHNOLOGY (PTY) LTD
  • US11505749B2 patent drawing
  • US11505749B2 patent drawing
  • US11505749B2 patent drawing

AI summary

A method for starting a slurry bubble column reactor that includes a reactor vessel holding a settled or slumped bed of particles and a liquid phase from which the particles have settled includes introducing a flow of a re-suspension liquid into the settled or slumped bed to loosen the settled or slumped bed. The introduction of the re-suspension liquid takes place before the introduction of any gas into the settled or slumped bed, or together with feeding of gas into the settled or slumped bed, provided that, if gas is fed together with the re-suspension liquid into the settled or slumped bed before the settled or slumped bed has been loosened, the gas has a superficial gas velocity in the reactor below 10 cm/s. Once the settled or slumped bed has been loosened by at least the re-suspension liquid, gas is passed at a superficial gas velocity above 10 cm/s through the liquid phase.