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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.
11

An experimental study of immersed coil heat exchangers

Feiereisen, Thomas James. January 1982 (has links)
Thesis (M.S.)--University of Wisconsin--Madison, 1982. / Typescript. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaf 109).
12

Frequency response of shell and tube heat exchangers

Iscol, Lewis, January 1959 (has links)
Thesis (Ph. D.)--University of Wisconsin--Madison, 1959. / Typescript. Vita. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 31-33).
13

Dynamic characteristics of crossflow heat exchangers

Gartner, Joseph R. January 1964 (has links)
Thesis (Ph. D.)--University of Wisconsin--Madison, 1964. / Typescript. Vita. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 313-314).
14

The design of resilient heat exchanger networks and their control structures

Marselle, Daniel F. January 1980 (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 189-192).
15

Transfer functions for a tube in crossflow

McNamara, Robert Tucker. January 1964 (has links)
Thesis (M.S.)--University of Wisconsin--Madison, 1964. / eContent provider-neutral record in process. Description based on print version record.
16

Synthesis and analysis of resilient heat exchanger networks

Saboo, Alok Kumar. January 1984 (has links)
Thesis (Ph. D.)--University of Wisconsin--Madison, 1984. / Typescript. Vita. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 286-291).
17

A procedure for dealing with temperature variations in the synthesis of resilient heat exchanger networks

Snyder, John D. January 1982 (has links)
Thesis (M.S.)--University of Wisconsin--Madison, 1982. / Typescript. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 78-80).
18

Factors affecting boiling heat transfer coefficient

Hsu, Charles Teh-Ching. January 1962 (has links)
Thesis (M.S.)--University of Wisconsin--Madison, 1962. / Typescript. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaf 173).
19

A study of cross-flow heat exchanger transients

Nagaoka, Ryuzo. January 1964 (has links)
Thesis (M.S.)--University of Wisconsin--Madison, 1964. / eContent provider-neutral record in process. Description based on print version record. Bibliography: l. 91-92.
20

Characterisation of a plate heat exchanger under superheat conditions

Schröder, Lukas Herman 05 September 2012 (has links)
M.Ing. / The objective of this study is to analytically evaluate the heat transfer and area requirements of a plate heat exchanger, in which the refrigerant exits the heat exchanger as a saturated vapour; a superheated vapour, under variable inlet conditions, through application of the experimental results obtained by Yan and Lin (1999) on the evaporation heat transfer and pressure drop of refrigerant R134a in a plate heat exchanger. Through the analytical evaluation it will firstly be shown that for the instance in which the refrigerant enters the heat exchanger at different inlet qualities and exits the heat exchanger as a saturated vapour that the amount of heat transferred and area requirement reduces as the inlet quality of the refrigerant increases. Secondly, when the refrigerant enters the heat exchanger as a saturated vapour and exits at different values of superheated vapour that the amount of heat transferred from the water to the refrigerant increases as the amount by which the refrigerant is superheated increases, combined with an increased area requirement in order to realise a certain amount of heat transfer. All evaluations are conducted at fixed mass flow rates. Through comparison of the two evaluations it will be shown that the area requirement in the superheated region is significantly larger than in the evaporation region of the heat exchanger whilst obtaining significantly less heat transfer.

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