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Microfluidic Preparation of Liquid Crystalline Elastomer Actuators
Published on: May 20, 2018
Continuous flow hydroformylation using supported ionic liquid phase catalysts with carbon dioxide as a carrier.
Ulrich Hintermair1, Zenxing Gong, Ana Serbanovic
1EaStCHEM, School of Chemistry, University of St. Andrews, St. Andrews, Fife KY16 9ST, Scotland.
This study demonstrates a supported ionic liquid phase (SILP) catalyst for continuous flow hydroformylation. Optimized CO(2) pressure enhances reaction rates and reduces catalyst leaching, achieving high stability and selectivity.
Area of Science:
- Catalysis
- Chemical Engineering
- Materials Science
Background:
- Supported ionic liquid phase (SILP) catalysts offer potential for continuous flow processes.
- Hydroformylation is a key industrial reaction for producing aldehydes.
- Understanding the influence of reaction parameters on SILP catalyst performance is crucial for process optimization.
Purpose of the Study:
- To investigate the continuous flow hydroformylation of 1-octene using a novel SILP catalyst.
- To determine the effect of process parameters, particularly CO(2) pressure, on reaction rate, yield, and catalyst stability.
- To optimize conditions for enhanced catalytic activity and minimized metal leaching.
Main Methods:
- Preparation of a SILP catalyst using [PrMIM][Ph(2)P(3-C(6)H(4)SO(3))], [Rh(CO)(2)(acac)], [OctMIM]NTf(2), and microporous silica.
- Continuous flow hydroformylation of 1-octene in the presence of compressed CO(2).
- Statistical experimental design to analyze the impact of film thickness, syngas:substrate ratio, and CO(2) pressure on reaction performance.
Main Results:
- Reaction rate is influenced by an interaction between syngas:substrate ratio and film thickness.
- Increasing CO(2) pressure improved reaction rates and significantly reduced ionic liquid (IL) and rhodium (Rh) leaching by forming an expanded liquid phase.
- Optimal conditions yielded a stable catalyst with a turnover frequency (TOF) of 500 h(-1) and low Rh leaching (0.2 ppm) over 40 hours, with consistent linear:branched selectivity (l:b ratio ≈ 3).
Conclusions:
- The phase behavior of the mobile phase, controlled by CO(2) pressure, is critical for SILP catalyst performance in hydroformylation.
- Optimized CO(2) pressure enhances mass transfer and reduces catalyst/IL solubility, leading to improved activity and stability.
- The developed SILP catalyst demonstrates robust performance and selectivity for continuous flow hydroformylation.
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