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Book ChapterDOI

Design Parameters for Mechanically Agitated Reactors

Y.T. Shah
- 01 Jan 1991 - 
- Vol. 17, pp 1-206
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This article is published in Advances in Chemical Engineering.The article was published on 1991-01-01. It has received 34 citations till now.

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Journal ArticleDOI

Gas–liquid flow generated by a Rushton turbine in stirred vessel: CARPT/CT measurements and CFD simulations

TL;DR: In this paper, computer-automated radioactive particle tracking (CARPT), computed tomography (CT) and computational fluid dynamic (CFD) based models were used to investigate gas-liquid flow generated by a Rushton turbine.
Journal ArticleDOI

Effect of inert solid particles at low concentrations on gas-liquid mass transfer in mechanically agitated reactors

TL;DR: In this paper, the volume referred mass transfer coefficients k L a were determined for the slurries of 6 solids in water and n -butanol in a mechanically agitatted reactor of standard configuration.
Patent

Process for preparing alkylene oxides

TL;DR: A process of preparing alkylene oxides comprises steps of: (1) optionally contacting metal hydroxide or oxide with chlorine to form a metal hypochlorite solution; (2) contacting chlorine with a solution of a metal hyper-chlorite at a temperature below 60 °C, and a pH of less than 5.5, with sufficient micromixing to achieve a product hypochchlorous acid in a yield of at least 80 mole percent based on hypochemically defined alkylorite; (3) separating at least a portion of the hyp
Journal ArticleDOI

Dynamics of Flow Structures and Transport Phenomena, 2. Relationship with Design Objectives and Design Optimization

TL;DR: There have been several approaches in the literature to identify and characterize flow structures qualitatively as well as quantitatively as discussed by the authors, and a stepwise procedure is suggested for the design of equipment using flow structure knowledge, where an attempt has been made to relate the structure properties (such as age, penetration depth, size, shape, and energy content distribution) to the design parameters, such as mixing time, heat and mass-transfer coefficient, drag coefficient, dissipation rate, etc.).
Journal ArticleDOI

A theoretical and experimental study of hyperbolic and degenerate mixing regions in a chaotic Stokes flow

TL;DR: In this article, the authors examined the rotor-oscillator flow, a slow viscous flow between long parallel plates driven by the rotation of a slender cylinder (the rotor) and the longitudinal oscillation of one of the plates (the oscillator).
References
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Journal ArticleDOI

Fundamentals of the hydrodynamic mechanism of splitting in dispersion processes

TL;DR: In this paper, Taylor's experiments on the breakup of a drop in simple types of viscous flow, (b) breakup of an air stream, and (c) emulsification in a turbulent flow are studied.
Journal ArticleDOI

Design parameters estimations for bubble column reactors

TL;DR: In this article, the present state-of-the-art for the estimation of nonadjustable parameters in bubble column reactors is evaluated and a discussion is followed by relevant recommendations for their predictions.
Journal ArticleDOI

Agitation of non‐Newtonian fluids

TL;DR: In this article, a general relationship between impeller speed and the shear rate of a non-Newtonian fluid has been developed, and the resulting relationship was then used to interpret and correlate power-consumption data on three non-newtonian fluids by use of a generalized form of the conventional power-number-Reynoldsnumber plot for Newtonians.
Journal ArticleDOI

Suspending of solid particles in liquid by agitators

TL;DR: In this paper, an investigation of the required stirrer speed and stirrer dimensions for the suspending of solid particles in a low viscosity liquid has been carried out and the results are given in dimensionless form.
Journal ArticleDOI

The continuous phase heat and mass transfer properties of dispersions

TL;DR: In this paper, the authors measured the interfacial area in gas-liquid dispersions and correlated the data with other published data for heat and mass transfer in liquid-liquid and solid-gas dispersions in which the dispersed phases are free to move under the action of gravity.
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