Engineering Commons^™

Transient Phenomena Of Polymer Solutions, Nikolaus Zwetkow

Theses

With the aid of a rotational viscometer, several transient phenomena were studied with different polymer solutions. In order to be acquainted with the operations of the rotational viscometer, viscosity measurements were made on polystyrene solution of a 7.14 wt. % NBS-2-35967 in a 35 - 65 mixture of aroclor and TCP, polyisobutylene (16.5% in mineral spirits), Indopol H-1900 (polyisobutylene) and 4.5% polyisobutylene in Primol 355. All these were done at a temperature of 77°F, except for Indopol H-1900 which was done at different temperatures. The results are listed in the section of tables and graphs.

Viscosity was measured with a …

Antoine Type Equation For Liquid Viscosity Correlations, Edward Goletz Jr.

Theses

A modified Andrade⁴ equation, similar to the Antoine equation for vapor pressure-temperature correlations, was developed for liquid viscosity-temperature correlations. Included in the investigation were the following compounds: n-alkanes (C₂-C₂₀), n-alkenes (C₂-C₂₀), n-alkyl benzenes (C₆-C₁₀), n-alkyl cyclohexanes (C₆-C₂₂), and fifteen polar compounds. Except for propene, errors of less than 5% were obtained. Normal heptadecane was used to compare correlations developed by Andrade⁴, Walther²⁰, and Doolittle⁹, with the modified Andrade equation. The latter was found to give the best …

A Study Of Emulsion Viscosities, Frederick R. Cummings

Theses

The apparent viscosity of stable emulsions has been measured and evaluated. The systems studied consisted of various oil in water emulsions, utilizing a series of six n-paraffins from heptane to octadecane. The system was stabilized with a conventional emulsifying agent. The apparent viscosity of these emulsions was studied in relation to (a) the concentration of the disperse phase and, (b) the viscosity of the hydrocarbon used as the continuous phase.

It was established that the volume concentration of the disperse phase had considerable effect on the apparent viscosity of the emulsion. An increase in the concentration of the disperse phase …

Effect Of Liquid Viscosity On Performance Of Wire Mesh Entrainment Separators, Raymond Paul Vogel

Theses

The knitted wire mesh entrainment separator, commonly referred to as a demister*, is in common use to separate entrained liquid from vapor streams. However, little quantitative information is available concerning the effect of physical properties of the entrained liquid on allowable gas velocities.

Studies were made on two demister styles to determine the effect of liquid viscosity on demister performance, Liquid viscosities from 0.9 to 12 centipoise were investigated using water, glycerine-water mixtures and heavy no. 2 fuel oil as the test liquids. Air was used as the gas medium in all cases.

Regression analysis of the test data indicates …

Absolute Viscosity Of The N-Paraffin Liquids, Gerald Permutt

Theses

The absolute viscosity of the normal paraffins C₅H₁₂ to C₂₀H₄₂ was studied to determine a relationship more useful in predicting liquid viscosities than existing correlations such as the methods of Andrade, Souders, Thomas, and Doolittle.

It was found that a function of corresponding liquid states could be designed which related viscosity to the number of carbon atoms. This function, here called liquidity, is defined as the extent to which a substance exists as a liquid with respect to temperature. This function can be expressed mathematically as:

L_c = (t - t_m)/(t …

Viscosity Of A Three Component System, Acetone-Ethanol-Water, At 25°C And 30°C, Peter Fred Widmer

Theses

The viscosity in the three component system Acetone-Ethanol-Water has been determined over a range of compositions at two different temperatures, 25°C and 30°C. Compositions have been varied in increments of ten percent by weight to cover all possible combinations of the three components. The data obtained are presented on triangular coordinate graph paper with lines of constant viscosity indicated and also in tabular form.

Correlation Of Curtis And Gullett Equation For Viscosity Of Non-Newtonian Suspensions And Franks And Rinaldi Equation For Heat Transfer Coefficients, Irene S. Wisla, John L. Kukowski

Theses

Curtis and Gullett (7) developed an equation correlating the effect of velocity, concentration and particle size on apparent viscosity of non-Newtonian water slurries.

μ/μ_w=1.02(AK/GC)^.105

The object of this paper was to determine the validity of using the viscosity, as determined by the Curtis-GulLett (7) equation, in predicting the heat transfer coefficient of non-Newtonian fluids, where the suspending medium is something other than pure water . The authors used various concentrations of sugar solutions as the dispersion medium, for the slurries.

A dimensionless equation resembling the flittusBoelter equation with modified exponents and additional dimensionless groups has been developed …

Viscosity Of Non-Newtonian Suspensions, David Edward Gullett, Edward Curtis

Theses

The object of this project ras to obtain a reasonable correlation of the effect of velocity, concentration and particle size on apparent viscosity of non-Newtonian slurries.

Through the use of dimensional and graphical analysis an equation, μ/μ_w=1.02(Ak/GC)^.105, was developed which filled these conditions. The average deviation of the apparent viscosity calculated from this equation compared to the experimental value was 14.4%.

The authors believe that this correlation should be tested under a greater variety of conditions of particle size and particle thermal conductivity and for suspending mediums other than water.

Viscosity Determination During Polymerization, Elmer David Jones

Theses

This project was undertaken for the purpose of designing, constructing, and operating a viscometer which could be employed for measuring viscosities in the range of 200 to 700 poises at temperatures up to 300°C. Such an instrument was built and used to study the viscosity of Type EV polymer during polymerization.

The new viscometer is based cm the principle of concentric rotating cylinders. It is unique in that it can be suspended directly in a polymer batch and will operate under temperature and viscosity conditions as outlined above. Polymerization curves for batches studied show that the instrument gives viscosity values …