Through the vantage point of institutions of higher learning, Utah's distinction as a politically conservative state dominated by the Church of Jesus Christ of Latter-day Saints is examined during the Vietnam War era. The three universities in the study-Brigham Young University, University of Utah, and Utah State University- are the three oldest and most populous universities in the state. This thesis concentrates on these three institutions and less on the politics of the state at the time. Studies showed that the universities, to varying degrees, exhibited antiwar sentiment Still, the campuses were less active in opposing the war, drawing only a very small percentage of students to demonstrations. Brigham Young University's President, Ernest L. Wilkinson (1951-1971), vigorously guarded against signs of antiwar activity. He was involved in the 1966 spy ring, which organized students for surveillance of supposedly liberal faculty. Students who appeared to be antiwar were also scrutinized. Despite the negative sanctions on such students, a minority of pupils did oppose the war and Wilkinson's tactics. The University of Utah produced the highest number of protesters, largely because of its more diverse and urban population. Many of the demonstrators at the U of U continued as activists in the Salt Lake Valley into the 1990s. Utah State University echoed the U of U, but to a lesser extent. Still, underground newspapers and an organized antiwar political party showed that USU also had a movement against the war. The administrations of the two schools figure into the text less powerfully than BYU's Wilkinson because they failed to become as involved in the debate. Oral interviews dominate this thesis. Subjects were chosen according to their involvement in particular events or movements. Student newspapers and underground newspapers were also utilized. This thesis attempted to recreate a tumultuous and turbulent time in American history. Utah's unique cultural slant showed that the Beehive State could not isolate itself from international events but also responded in its own way.

Recent developments have indicated high oxygen consumption rates of about 35 g-mole/m³-min during oxidative pressure leaching. At such high oxygen consumption rates the mass transfer of dissolved oxygen at the gas-liquid interface may become rate-limiting. The objective of this study was to obtain an understanding of the gas-liquid mass transfer processes that take place in mechanically agitated pressure leaching systems. The classical reaction between sodium sulphite and dissolved oxygen to form sulphate at atmospheric pressure was used to determine the oxygen mass transfer rates in a 200-liter asymmetrical plastic tank, modelled after the shape of the first compartment of the zinc pressure leach. The effect of this asymmetry was compared with the work of Swiniarski who used a cylindrical symmetrical tank of similar volume. A number of process variables such as the impeller type and size, the impeller speed, the impeller immersion depth and the effect of full baffles that affect mixing were investigated. Also, the volumetric power consumption associated with the mass transfer rates were measured. The results indicate that the asymmetrical tank is at least 3.6 times more efficient in mass transfer than the symmetrical tank. There is a critical speed below which the mass transfer parameter, K[formula omitted], is almost zero and above which K[formula omitted] increases almost linearly with impeller tip speed. A simple energy balance model for bubble creation can predict the critical tip speed. It is shown that K[formula omitted] is enhanced at shallow depths, with a corresponding high mass transfer to energy ratio. The relative effectiveness of impeller types and sizes with regard to the use of power for gas-liquid mass transfer was established. Full baffles degrade the mass transfer rate at increased depth of impeller immersion. The results also add substantial support to the findings provided by DeGraaf [5] that: (i) The dimensionless correlations used in liquid mixing systems do not accurately predict dispersion rates by agitators. (ii) The optimum conditions for gas dispersion and the consequent generation of gas-liquid interfacial area are different from fluid mixing. (iii) The classical mixing power equations for impellers markedly overestimate power requirements during impeller gas dispersion. / Applied Science, Faculty of / Materials Engineering, Department of / Graduate

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