`
`MDMENTUJM rmmsnsn
`
`warren M. Rohsenew
`
`PROFESSOR OF MECHANICAL ENGINEERING
`MASSACHUSETTS INSTITUTE OF TECHROLOGY
`
` Harry L Bhoi
`
`ASSOCMTE PROFESSOR OF MECHANICAL ENGINEERING
`TUFTS UNIVERSITY
`
`R.J. Reynolds Vapor
`IPR2016-01268
`
`R.J. Reynolds Vapor v. Fontem
`Exhibit 1016-00001
`
`
`
`© 1961
`
`by PRENTICE-HALL, INC.
`
`Englewood Cliffs, N. J.
`
`this
`reserved. No part of
`rights
`All
`book may be reproduced in any form, by
`mimeograph or any other means, without
`permission in writing from the publisher.
`
`Library of Congress Catalog Card No. 61-15516
`
`Printed in the United States of America
`
`48418-C
`
`Current printing (last digit):
`
`1312111098765
`
`Exhibit 1016-00002
`
`
`
`102
`
`HEAT TRANSFER IN s'r.-vrronnnr SYSTEMS
`
`TABLE 6.1 onnrm on MAGNITUDE or 12, are/Has-r’ F
`
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`Gases (natural convection) .
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`Flowing gases .
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`Flowing liquids (nonmetallic) .
`Fiowing liquid metals .
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`Boiling liquids .
`. . .
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`Condensing vapors .
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`0.9-5
`.
`2-50
`.
`30—~1,000
`.
`. 1,000-50,000
`.
`200-50,000
`.
`500—5,000
`
`For a wall, the equivalent in is k/as. For example, for a. steel wall 0.12‘in.
`thick and is = 26 Btu/hr ft F, the equivalent h is 26 X 12/0.12 or 2600,
`but for an asbestos wall 1 ft thick with It = 0.13 Btu/hr ft F, the equivalent
`his 0.13/l or 0.13.
`For certain combinations of these various resistances in series, some
`may be negligible compared with others.
`
`Example 6.1: What resistances are negligible when heat is transferred
`through 1 ft” of a 0.12-in. thick steel plate (kw = 26) with a. flowing liquid
`(h: = 1000) on one side and a flowing gas on the other (kg, = 10)?
`Assume a scale coefficient of h, = 1000 on the liquid side. From Eq. (6.22)
`
`In this case the wall and scale resistances are negligible.
`
`1
`
`1
`
`1
`
`as...
`
`1
`
`1
`
`1
`
`0.12
`
`1
`
`U_h;+h,+lc..,+h,,—1000+1000+(26)(12)+10
`
`....1__1
`"*10"h,,
`
`In this case, the only significant resistance is at theigas side surface.
`
`Example 6.2: Same as Example (6.1) with the flowing gas replaced by
`condensing steam (h = 1000).
`
`l__1_+_L+ 1+;
`U*1ooe
`1000
`2600
`1000
`
`In this case, none of the resistances is negligible.
`
`Example 6.3: Same as Example (6.1) withethe flowing liquid replaced by
`another flowing gas (h,,. = 5).
`'
`
`Exhibit 1016-00003
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