Abstract
Bubble size distribution (BSD) is important for gas-liquid jet loop reactor (JLR)’s mass transfer performance of inter-phases. A self-designed reversed JLR was investigated with air-water system on the BSD. The CCD camera of particle imaging velocimetry (PIV) system and image processing technique were used to obtain the reliable photo. The influences of four parameters, gas phase flow rate, liquid phase flow rate, draft tube diameter and ejector mounting position, on the BSD were studied in detail. The results showed that the local BSD is accordance with log-normal distribution under the experimental conditions and the average diameter and BSD range increase with the increase of the gas phase flow rate, and decrease with the increase of the liquid phase flow rate, the downward movement of the nozzle installation position and the increase of the diameter of the draft tube.
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Articles in the same Issue
- Review
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- Role of Reaction Time on the Electrical Conductivity, Thermal Stability and Photoluminescence Property of Polyanilne Nanofibers
- Experimental Study on Bubble Size Distribution in Gas-Liquid Reversed Jet Loop Reactor
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- Kinetics Investigation of Carbon Dioxide Hydrate Formation Process in a New Impinging Stream Reactor
- Delumping Strategy to Infer Lubrication Reaction Pathways in Internal Combustion Engines
Articles in the same Issue
- Review
- Production of Sodium Bicarbonate from CO2 Reuse Processes: A Brief Review
- Article
- Role of Reaction Time on the Electrical Conductivity, Thermal Stability and Photoluminescence Property of Polyanilne Nanofibers
- Experimental Study on Bubble Size Distribution in Gas-Liquid Reversed Jet Loop Reactor
- Methylene Blue Adsorption onto Neem Leave/Chitosan Aggregates: Isotherm, Kinetics and Thermodynamics Studies
- Antibacterial Activity of Phenyllactic acid Against Staphylococcus Epidermidis and Its Microbial Production: Modelling and Optimization-Based Analysis
- A New Robust Approach for Reactor Network Synthesis by Combination of Mathematical Method and NSGAII
- Experimental Evaluation of Biomass Medium-Temperature Gasification with Rice Straw as the Fuel in a Bubbling Fluidized Bed Gasifier
- Effect of Catalyst (de)activation on Reagent Diffusion in ZSM-5/alumina Extruded Pellet for the Methanol-to-hydrocarbons Conversion
- Kinetics Investigation of Carbon Dioxide Hydrate Formation Process in a New Impinging Stream Reactor
- Delumping Strategy to Infer Lubrication Reaction Pathways in Internal Combustion Engines