Engineering Commons^™

Agitation Requirements For Complete Liquid Dispersion In Liquid-Liquid-Gas Systems, Emad Ahmad Abu-Hakmeh

Theses

A number of studies have been published in the literature on the determination of the agitation intensity at which two immiscible liquids become completely dispersed in mechanically agitated vessels. However, no information is currently available on the agitation intensity required for the complete dispersion of two liquids in the presence of an additional gas phase. Therefore, the main objective of this study was to experimentally determine the minimum agitation speed for complete liquid-liquid dispersion, N_cd, in liquid-liquid-gas systems as a function of gas flow rate, impeller type, impeller size, and impeller off-bottom clearance. The minimum agitation speed was …

Evaluating The Homogeneity Of Solidification/Stabilization Treated Waste Soils By Chemical Analysis Method, Mei Liu

Theses

Solidification/Stabilization technology has been widely used for waste treatment, especially for heavy metals, non-volatile wastes, radioactive wastes and soils. Homogeneity is a very important criterion for this kind of technology.

This study focuses on the development of a method to evaluate the homogeneity of S/S treated soil. A chemical analysis method, atomic absorbance, is employed to evaluate the distribution of S/S reagent in a soil-cement mixture and thus the uniformity of the soil-cement mixture. Also, a fluorescent tracer method is discussed in this study, which can be used to estimate the homogeneity of the soil-cement surface. The fluorescent tracer method …

Liquid-Liquid Dispersion In Agitated Vessels Provided With Multiple Impellers, Yu-Tsang Huang

Theses

Baffled vessels with multiple impellers are widely used in industry to generate liquid-liquid dispersions. In this work, a new method to determine the minimum agitation speed for complete dispersion in two immiscible liquids was developed. This method was conceived to replace the traditional visual observation method that has been extensively used in the past for this purpose. The minimum agitation speeds for liquid-liquid dispersion with single and multiple impellers in baffled vessel were also measured. The effect of a number of variables such as size and type of impellers, size of tank, impeller location, spacing between impellers, and dispersed phase …

Solid-Liquid Suspension In Agitated Vessels Provided With Multiple Impellers, Tong Li

Theses

A large number of references can be found in the literature on the effect of mixing parameters on the achievement of the minimum agitation speed to just suspend solid particles. In the vast majority of these studies the agitation system consisted of just one centrally mounted impeller. However, the determination of the minimum agitation speed to achieve the just suspended state when the additional impellers are used have received very little attention. It is the intent of this work to investigate the role of multiple impeller agitation system on the achievement of the complete particle suspension state. The effect of …

Multiphase Solid-Liquid-Liquid Mixing In Stirred Tanks, George R. Deritter

Theses

A large number of investigations can be found in the literature which examine the effect of mixing parameters in both solid-liquid and liquid-liquid systems. However, very little is currently available for solid-liquid-liquid systems. It is the intent of this study to look at the various parameters affecting the point of complete dispersion for a liquid and the point of complete suspension for a solid phase, in a three phase liquid-liquid-solid system.

Agitation Of Dilatant Fluids, Vijay Jang Datta

Theses

No abstract provided.

The Influence Of Agitation On A Continuous Counter-Current Liquid-Liquid Extraction Column, William John Hartmann

Theses

This work presents operating data and correlations of agitated extraction equipment studied under continuous counter-current flow.

The experimental work was carried out in at agitated column 36 inches in length with an internal diameter of 2 inches using the system toluene, benzoic acid and water. The working section of the column was 24 inches. The design of the column used for the experimental work is similar to that proposed in a patent by van Dijck (3). The column is similar only to the extent that the patent covers numerous conditions of vertical agitation.

The distribution data and the equilibrium solubility …