scholarly journals The physics of non-Newtonian liquid slurry atomization. Part 2: Twin-fluid atomization of non-Newtonian liquids -- First quarterly technical report, 1 January--31 March 1994

1994 ◽  
Author(s):  
A. Mansour ◽  
N. Chigier
1981 ◽  
Vol 46 (9) ◽  
pp. 2021-2031 ◽  
Author(s):  
Pavel Seichter

Velocity profiles and pumping capacity have been determined using a thermistor anemometer in a vessel equipped with a screw impeller. In region of the creeping flow of a Newtonian liquid, i.e. for Re <15, the dimensionless pumping capacity is dependent on the geometrical arrangement of the mixing system. The efficiency was assessed of individual configuration from the value energy criterion expressing the dimensionless power requirements for recirculation of a highly viscous liquid in a vessel equipped with a screw impeller.


2014 ◽  
Vol 611 ◽  
pp. 137-144 ◽  
Author(s):  
Alexandr Shimanovsky ◽  
Maryna Kuzniatsova ◽  
Alžbeta Sapietová

Finite element modeling of the Newtonian and non Newtonian liquids oscillations in the cylindrical transport reservoir at its braking was performed. The peculiarities of the Newtonian, Ostwald de Waele and Bingham models of liquid sloshing in tank with internal perforated baffles and without them were analyzed. There were obtained the dependences of hydrodynamic pressures and liquid energy dissipation for Newtonian and non Newtonian liquids considering the different filling level of the reservoir.


1990 ◽  
Vol 220 ◽  
pp. 413-425 ◽  
Author(s):  
S. D. R. Wilson

The Taylor–Saffman problem concerns the fingering instability which develops when one liquid displaces another, more viscous, liquid in a porous medium, or equivalently for Newtonian liquids, in a Hele-Shaw cell. Recent experiments with Hele-Shaw cells using non-Newtonian liquids have shown striking qualitative differences in the fingering pattern, which for these systems branches repeatedly in a manner resembling the growth of a fractal. This paper is an attempt to provide the beginnings of a hydrodynamical theory of this instability by repeating the analysis of Taylor & Saffman using a more general constitutive model. In fact two models are considered; the Oldroyd ‘Fluid B’ model which exhibits elasticity but not shear thinning, and the Ostwald–de Waele power-law model with the opposite combination. Of the two, only the Oldroyd model shows qualitatively new effects, in the form of a kind of resonance which can produce sharply increasing (in fact unbounded) growth rates as the relaxation time of the fluid increases. This may be a partial explanation of the observations on polymer solutions; the similar behaviour reported for clay pastes and slurries is not explained by shear-thinning and may involve a finite yield stress, which is not incorporated into either of the models considered here.


Author(s):  
M. Kimiaghalam ◽  
M. Passandideh-Fard

We studied numerically impingement of vertical liquid jets of moderate Reynolds number for both Newtonian and non-Newtonian liquids to clarify the structure formation of circular hydraulic jump and the phenomenon of jet buckling. First, we have studied the hydraulic jump characteristics and governing parameters for a laminar water jet. Moreover, different types of hydraulic jump have been investigated by varying the height of a circular wall around the bed in flow downstream. The results show that a circular hydraulic jump has two kinds of steady states which can be reached by changing wall height. Next, we studied the impingement of a non-Newtonian liquid jet on a solid surface. In this case, we observe that instead of having a significant hydraulic jump, jet buckling phenomenon happens. The results were used in order to achieve a better understanding of the jet buckling phenomenon and the conditions in which this phenomenon happens.


1982 ◽  
Vol 104 (4) ◽  
pp. 469-474 ◽  
Author(s):  
S. S. Hwang

A blade coating process for non-Newtonian liquids is presented using different air pressure applied at the inlet and the exit of the coating gap. The system consists of a coating blade to form a gap and a vacuum box to create different air pressures to permit coating a thin liquid film on an advancing plastic web. The solution consists of matching the boundary conditions of each subregion of the coating process. The calculated liquid film thickness as a function of the coating gap and applied air pressure difference agrees closely with experimental data obtained on a laboratory coating device.


A technique of flow visualization by means of an expanded laser beam and trace amounts of particulate additives is used to study the behaviour of newtonian and nonnewtonian elastic liquids in complex geometries. Differences in response are highlighted between the newtonian and non-newtonian fluids when these flow separately in certain contraction flows and also in a two-dimensional T geometry. This information is then used to interpret the behaviour when both types of fluid flow together in the same geometry with a well-defined interface between them. Of major interest is the observation that a newtonian liquid in the two-liquid situation (the other liquid being non-newtonian) can behave as if it were highly elastic. We are led to associate this behaviour with the boundary conditions existing at the interface between the newtonian and the non-newtonian liquids. Powerful finite-element numerical techniques are used in an attempt to simulate the observed flow characteristics. The techniques are able to meet the challenges posed by the two-liquid situation when both liquids are newtonian. They are also able to simulate the distinctive vortex structure observed when only one highly elastic liquid is used in the experiments. They are, as yet, unable to meet the difficult challenge where one of the two liquids is highly elastic. The experimental and theoretical work has an obvious potential application to the important practical problem of ‘coextrusion’.


2021 ◽  
Author(s):  
Hadil Abukhalifeh

Little information is available in literature in terms of the hydrodynamic characteristics in a turbulent bed contractor [sic] (TBC) with viscous liquids. In this study, the hydrodynamic characteristics in three-phase turbulent bed contactor with counter current flow of air and non-Newtonian liquid was studied and compared with that of Newtonian liquid under consistent conditions. Aqueous solutions of carboxy methyl cellulose (CMC) with apparent viscosities ranged between 5 to 25 cP were used as non-Newtonian liquid. The hydrodynamic parameters iinvestigatedwere: bed pressure drop, minimum fluidization velocity, liquid holdup, bed expansion, and gas holdup. The effect of rheological properties of the CMC aqueous solutions and operating parameters on hydrodynamic characteristics of the TBC were examined. Results showed that increasing CMC concentration increased the net pressure drop across the bed and the liquid holdup, while the gas holdup and bed expansion decreased. At that quoted apparent viscosity range, aqueous solutions of CMC behaved as Newtonian viscous liquids in the TBC.


2021 ◽  
Vol 21 (3) ◽  
pp. 863-878
Author(s):  
SERPİL SAHİN ◽  
HÜSEYİN DEMİR

In this paper, we formulate the steady hydromagnetic lid-driven cavity problem in a stream function-vorticity form for weakly electrically conducting Newtonian and non-Newtonian liquids. Then we solve them by using the concept of pseudo time derivative. The classical benchmark results of the Newtonian liquid are recovered as a limiting case and the inhibiting influence of the magnetic field on the Newtonian and non-Newtonian liquids’ flow field is clearly depicted through graphs. We also show certain aspects of the flow for the first time in tables.


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