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  • About
  • The Global ETD Search service is a free service for researchers to find electronic theses and dissertations. This service is provided by the Networked Digital Library of Theses and Dissertations.
    Our metadata is collected from universities around the world. If you manage a university/consortium/country archive and want to be added, details can be found on the NDLTD website.
41

Mixing pulp suspensions

Bennington, Chad Patrick Joseph January 1988 (has links)
Initiation and maintenance of motion within a pulp suspension is necessary for effective mixing. This requires imposition of forces greater than the network strength and depends on suspension rheology once motion begins. As pulp suspensions display non-Newtonian and solid-like behaviour, studies were conducted using profiled rotors which imposed stress within the body of suspensions contained in cylindrical devices. A concentric cylinder device capable of high torques (85 N-m) and high rotational speeds (524 rad/s) was built to study pulp suspension dynamic behaviour. Most work used a profiled rotor 0.1 m in diameter with baffled housings 0.13 and 0.22 m in diamter. The yield stress of low consistency pulp suspensions were measured with a Haake RV12 Ro-tovisco concentric cylinder viscometer. Semi-bleached kraft pulp was used throughout the study. Some tests were made with stone groundwood and thermomechanical pulps. Yield stress measurements were made for nylon and Spectra-900 fibre suspensions. The yield stress of pulp suspensions, ty, have been measured and correlated with mass concentration (Cm) and volumetric concentration (Cv) over the range 0.4 ≤ Cm(%) ≤ 33. It was found that because of increasing gas content that correlations developed using the mass concentration were inaccurate above approximately 20% Cm. Correlations developed using the volumetric concentration were accurate over the full range tested. For a West-Coast semi-bleached kraft pulp, ty(Pa) = 1.40CV(%)²ֹ⁷². Once rotor motion was initiated, pulp suspensions exhibited two distinct regimes of behaviour. The first was a tangential-cavity regime in which predominantly tangential motion grew to fill the chamber as shear rate increased. When motion reached the outer housing wall a flow transition occurred, likely triggered by flow interaction with the housing baffles. The subsequent post-transition regime was characterized by radial and axial flow that effectively mixed the suspension on both the macroscale and fibre-scale. The flow transition appeared to be what earlier workers reported as the onset of "fluidization". During tangential-cavity flow, phase segregation occurred. Gas present in the suspension collected around the rotor and reduced momentum transfer from the rotor to the suspension. This caused the torque for the pulp suspension to fall below that for water at the same rotational speed, and the cessation of flow development in the chamber. If sufficient momentum transfer was attained to initiate post-transition flow, the chamber contents became effectively mixed. The torque could still fall below that of water depending on the effective density of the suspension in the rotor vicinity. / Applied Science, Faculty of / Chemical and Biological Engineering, Department of / Graduate
42

The leaching of lignin macromolecules from pulp fibres during washing /

Favis, Basil D. January 1981 (has links)
No description available.
43

An investigation of the time-dependent structural and mechanical behavior of individual pulp fibers when subjected to an applied stress

Hill, Richard L., January 1967 (has links) (PDF)
Thesis (Ph. D.)--Institute of Paper Chemistry, 1967. / Bibliography: leaves 101-104.
44

An investigation of the adsorption of gases by wood and its components and of gas adsorption techniques as a means of studying the area and structure of pulp and paper

Haselton, William R., January 1953 (has links) (PDF)
Thesis (Ph. D.)--Institute of Paper Chemistry, 1953. / Bibliography: leaves 144-148.
45

Activated sludge biotreatability of pulp and paper bleach wastes : investigation of bleaching options

Baker, Scott Alan 12 1900 (has links)
No description available.
46

Molecular weight distributions of total organic halide in an aerated stabilization basin treating paper and pulp wastewater

Alleman, Bruce Charles, January 1986 (has links) (PDF)
Thesis (M.S. - Civil Engineering and Engineering Mechanics)--University of Arizona, 1986. / Includes bibliographical references (leaves 81-82).
47

The demand for British Columbia kraft pulp

Suderman, Henry Leonard January 1969 (has links)
The major objective of this study was to determine the outlook of the British Columbia kraft pulp industry for the period 1969 - 1974. To attain this objective and develop the necessary perspective, the global economy and particularly world trade developments were studied. An historical analysis of world economic variables was made and then, where possible, projections into the future made. From these studies, specific applications to the British Columbia industry were given. Consequently, the approach of this study was to begin with general global considerations and then proceed to more specific items pertaining to the British Columbia industry. The global demand trends for kraft pulp were obtained by studying the major kraft pulp consuming areas individually. Other kraft pulp producing areas of the world were analyzed to see what portion of potential demand they would be able to supply on competitive terms with British Columbia. As the perspective of the study narrowed, it focused on Canada. This country's historic economic and future potential were analyzed in detail. Recent rapid growth trends were noted and their expansionary effect on British Columbia's economy noted. This study revealed that previous forecasters generally understated future economic growth, particularly in the area of world trade. Consequently, a more liberal attitude was adopted in this analysis. On the basis of future reductions in tariffs, particularly the Kennedy Round cuts in the projection period, the mood of this forecast is one of optimism. Buoyant economic conditions are projected based on premises that state no abrupt changes in world affairs should be expected in the next five years. Global kraft pulp demand is expected to grow at least at the same rate as the world GNP growth. The growth rate in economic output has not been too much alike for all countries and consequently the average global GNP growth has given only a rough indication of kraft pulp consumption. Disproportionate GNP growth in the countries is forecast for the next five years. The industrialized countries will continue to grow faster than the less-developed countries. Most of the growth in kraft pulp demand will occur in the industrialized countries, of which the most promising areas are in Europe and Japan. Because the traditional sources for European markets are approaching their raw material limits, substitution from abroad should occur, consequently the demand for British Columbia kraft pulp should increase at a faster rate than overall global demand. The overall growth rate for British Columbia kraft pulp is expected to continue close to its historic average annual rate of 16%. The growth in British Columbia however has characteristically run in cycles and the secondary trend has been accentuated by industry moods of optimism and pessimism. In the last two years pessimism resulting from over-supply has tempered the overall general growth and a trough in the cyclical pattern is forecast for 1970 or 1971. The market is currently firming; consequently construction and expansion of mills is expected to accelerate and a peak in capacity growth should occur in the latter portion of the five-year projection period. / Business, Sauder School of / Graduate
48

Pulping qualities of refractory vs. permeable douglas-fir heartwood /

Blackman, Gary Lee. January 1970 (has links)
Thesis (M.S.)--Oregon State University, 1970. / Typescript. Mounted photographs. Includes bibliographical references (leaves 64-69). Also available on the World Wide Web.
49

Carbohydrates in a thermomechanical pulp, a sulfite pulp, and a solvent sulfite pulp from western hemlock /

Ni, Hae-Rong. January 1983 (has links)
Thesis (Ph. D.)--Oregon State University, 1984. / Typescript (photocopy). Includes bibliographical references (leaves 108-115). Also available on the World Wide Web.
50

Two-stage high-yield sulfite pulping of red alder (Alnus rubra Bong.) /

Hansen, Edward Dee. January 1967 (has links)
Thesis (M.S.)--Oregon State University, 1967. / Typescript (photocopy). Includes bibliographical references (p. 52-60). Also available on the World Wide Web.

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