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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.
1

The internal circulation of the adjacent fluidized bed reactor

Shih, Chuan-Cheng. January 1989 (has links)
Thesis (M.S.)--Ohio University, March, 1989. / Title from PDF t.p.
2

A systems approach to fluidized-beds

Ta'eed, O. January 1987 (has links)
No description available.
3

Fluidized bed hydrodynamics by means of electrical capacitance tomography

2015 January 1900 (has links)
Fluidized bed reactors are utilized in a variety of applications from hydrocarbon cracking to drying of mineral ore to coating of pharmaceutical pills. A proper understanding of bed hydrodynamics is essential to properly design, operate and control the process. Intrusive and non-intrusive measurement techniques have been utilized to study various aspects of fluidized bed behaviour. Electrical Capacitance Tomography (ECT) has been utilized to determine the distribution of gas-solid mixture in the bed. The Digital Image Analysis Technique (DIAT) is used to determine the bubble behavior in two-dimensional beds. The bubble behavior has not been studied by ECT. The premise of this research is to test a new technique by combining ECT solid fraction maps with image processing techniques to determine the bubble characteristics in the bed. Electrical Capacitance Tomography (ECT) was used to map the relative fractions of sand-air mixture in a 14 cm ID acrylic vessel at two different static bed heights. The voids were defined as the areas of gas-solid mixture with value of less than 0.25. Afterwards simple image analysis techniques were applied to isolate bubbles from the rest of the bed. The resulting data were converted into binary images to extract hydrodynamic information. The two main parameters of interest were the bubble diameter and its rise velocity. The experimental average velocities and average diameters matched the results obtained from respective correlations in the literature. However, large spreads existed for both these parameters due to the simultaneous presence of bubbles and slugs. The experimental fluidized bed did not transition fully into the turbulent regime but has the character of a hybrid bubbling-slugging regime. This is illustrated by experimental diameters which indicate presence of bubbles and slugs simultaneously. The same information was illustrated by experimental velocity-diameter envelopes (minimum and maximum values) which overlapped for higher flow conditions. The radial solid fraction distribution illustrated the same point with an inverted “M” profile which has been associated previously with regime transition. The path of bubble rise was identified, mainly rising through the midway point between the bed’s center and its inner edge. Five different types of bubbles were identified using the two dimensional binary images of voids. However, this technique can only be used for regimes where voids/bubbles are the main source of gas transfer to the surface of the bed.
4

Devolatilisation and volatile matter combustion during fluidised-bed gasification of low-rank coal / by Davide Ross.

Ross, David January 2000 (has links)
Bibliography: leaves 234-252. / xxiv, 254 leaves : ill. (some col.) ; 30 cm. / Title page, contents and abstract only. The complete thesis in print form is available from the University Library. / The devolution times of seven coals were determined by measuring the centre temperature response for single particles held stationary in a bench scale atmospheric fluidised-bed reactor. / Thesis (Ph.D.)--University of Adelaide, Dept. of Chemical Engineering, 2000
5

Temperature of burning carbonaceous particles in a fluidized-bed combustor /

Linjewile, Temi Makecha. January 1993 (has links) (PDF)
Thesis (Ph. D.)--University of Adelaide, Dept. of Chemical Engineering, 1993? / Includes bibliographical references (leaves 290-303).
6

Devolatilisation and volatile matter combustion during fluidised-bed gasification of low-rank coal /

Ross, David. January 2000 (has links) (PDF)
Thesis (Ph.D.)--University of Adelaide, Dept. of Chemical Engineering, 2000. / Bibliography: leaves 234-252.
7

Characterization of polycrystalline silicon grown in a fluidized bed reactor

Dahl, Megan Mureen. January 2009 (has links) (PDF)
Thesis (M.S. in materials science and engineering)--Washington State University, May 2009. / Title from PDF title page (viewed on Apr. 2, 2009). "School of Mechanical and Materials Engineering." Includes bibliographical references.
8

The transient behavior of fluidized bed reactors an experimental approach to predict erosion and attrition phenomena /

Aljodai, Abdulaziz. January 1900 (has links)
Thesis (Ph. D.)--West Virginia University, 2004. / Title from document title page. Document formatted into pages; contains xi, 120 p. : ill. (some col.). Includes abstract. Includes bibliographical references (p. 103-108).
9

Residence time distributions in moving fluidized beds

Tajuddin, Azizuddin, January 1976 (has links)
Thesis (M.S.)--University of Wisconsin--Madison. / Typescript. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 185-187).
10

Fluidized bed combustion of polyvinyl chloride with coal

Paul, Duane Bernard. January 1979 (has links)
Thesis (M.S.)--University of Wisconsin--Madison. / Typescript. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 44-47).

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