Regulated Membrane Separation for Homogeneous Catalyst Recovery

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Solution Overview

Problem

The separation of homogeneous catalysts from reaction mixtures is challenging due to their dissolution in the reaction mixture, leading to catalyst loss and deactivation, particularly in rhodium-catalyzed hydroformylation processes, where the catalyst is valuable and sensitive, and existing separation methods like adsorptive and thermal processes are inefficient and energy-intensive.

Innovation Solution

A controlled membrane separation unit is used to separate the homogeneous catalyst, where the retentate volume flow and retention are regulated to maintain constant conditions, ensuring high retention and low catalyst losses, and the retentate is recycled back to the reaction zone, stabilizing the hydrodynamics and simplifying catalyst addition.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of substance

If adsorptive separation processes are used to remove homogeneous catalyst from reaction mixture, then catalyst loss is reduced, but the process becomes energy-intensive and less efficient

Engineering Contradiction:
Improvecatalyst lossVSAvoidenergy consumption
Core Design Contradiction:
Loss of substanceVSUse of energy by moving object

Solution Approach 1:

The invention uses liquid-liquid extraction based on phase transition principles, where the homogeneous catalyst is transferred from the aqueous reaction phase to an organic extraction phase using specific solvents. This phase transition-based separation avoids the energy-intensive thermal processes and adsorption regeneration required by conventional methods, achieving catalyst recovery with significantly lower energy consumption while maintaining high recovery efficiency.

Inventive Principle:
Principle #36Phase transitions

2Productivity

If thermal separation processes are used to separate homogeneous catalyst, then separation efficiency is improved, but catalyst deactivation increases and energy consumption rises

Engineering Contradiction:
Improveseparation efficiencyVSAvoidcatalyst activity
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The invention employs liquid-liquid extraction utilizing phase transitions between aqueous and organic phases to separate the homogeneous catalyst. This method achieves high separation efficiency through selective solubility and phase distribution without exposing the catalyst to high temperatures that cause deactivation. The process maintains catalyst integrity and activity while efficiently separating the catalyst from the reaction mixture.

Inventive Principle:
Principle #36Phase transitions

3Device complexity

If membrane separation is used without regulation to separate catalyst, then equipment simplicity is maintained, but retention and separation performance become unstable under fluctuating flow conditions

Engineering Contradiction:
Improveequipment complexityVSAvoidretention stability
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

The invention implements a feedback control system for the membrane separation unit that monitors retention performance and automatically adjusts operating parameters such as cross-flow rate or transmembrane pressure. When retention drops below a set threshold, the system responds by adjusting flow rates to restore optimal separation performance. This feedback mechanism ensures stable catalyst retention and separation efficiency under varying feed conditions without requiring complex equipment modifications.

Inventive Principle:
Principle #23Feedback

4Device complexity

If retentate flow rate is not regulated in membrane separation, then process simplicity is maintained, but hydrodynamics in reaction zone are disrupted and catalyst balance becomes difficult to control

Engineering Contradiction:
Improveprocess complexityVSAvoidhydrodynamic stability
Core Design Contradiction:
Device complexityVSStability of the object's composition

Solution Approach 1:

The invention incorporates a feedback control system that monitors the retentate flow rate returning to the reaction zone and adjusts membrane separation operating parameters to maintain a constant or optimized flow rate. This ensures stable hydrodynamics in the reaction zone, preventing disruptions to mixing and mass transfer while maintaining proper catalyst balance. The feedback loop automatically compensates for variations in feed flow rate or composition, preserving reaction zone stability without requiring complex process changes.

Inventive Principle:
Principle #23Feedback

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 reduces catalyst losses and stabilizes the reaction zone, improving process control and energy efficiency, allowing for the effective separation and reuse of valuable catalysts even under fluctuating conditions.

Implementation Method 1

the reaction mixture originating from a reaction zone and containing the homogeneous catalyst is fed to the membrane separation unit as a feed, in which the homogeneous catalyst is depleted in the permeate of the membrane separation unit and enriched in the retentate

Methodology Applied
Scientific EffectPermeation: Permeation

Data Source

PatentEP2996805A1Separation of homogeneous catalysts by means of a regulated membrane separation unit
Publication Date: 2016.03.23 EVONIK OXENO GMBH & CO KG

AI summary

The invention relates to a method for separating a homogeneous catalyst out of a reaction mixture by means of at least one membrane separation unit, in which method: the reaction mixture coming from a reaction zone and containing the homogeneous catalyst is applied as a feed to the membrane separation unit; the homogeneous catalyst is depleted in the permeate of the membrane separation unit and enriched in the retentate of the membrane separation unit; and the retentate of the membrane separation unit is recirculated into the reaction zone. The invention addresses the problem of specifying a method for separating homogeneous catalyst out of reaction mixtures that simplifies the feeding of fresh catalyst into the reaction zone and avoids disruptions to the hydrodynamics within the reaction zone when the volumetric flow of the reaction mixture output from the reaction zone varies. This problem is solved in that both the retentate volumetric flow of the membrane separation unit and the retention of the membrane separation unit are kept constant by regulation.