TURBULENT FLOW, HEAT TRANSFER, AND MASS TRANSFER IN TUBE WITH SURFACE SUCTION

RB KINNEY RB; Ephraim M Sparrow

TURBULENT FLOW, HEAT TRANSFER, AND MASS TRANSFER IN TUBE WITH SURFACE SUCTION

RB KINNEY RB, Ephraim M Sparrow

Mechanical Engineering

Research output: Contribution to conference › Paper › peer-review

Abstract

Numerical results are presented for the friction factor, axial pressure gradient, heat and mass transfer coefficients, and velocity and temperature profiles. The results, relevant to forced- convection condensation in a tube (with or without noncondensable gases), are substantially affected by small amounts of wall suction. The present findings do not support the current practice of using impermeable-boundary transfer coefficients in condensation calculations. tTurbulent transport is expressed by the mixing- length model, modified around the wall by a specially derived damping factor.

Original language	English (US)
State	Published - Jan 1 1969
Event	Unknown conference - Duration: Aug 3 1969 → Aug 6 1969

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Other	Unknown conference
Period	8/3/69 → 8/6/69

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@conference{5444f83f9f524438a89a9a65d1665389,

title = "TURBULENT FLOW, HEAT TRANSFER, AND MASS TRANSFER IN TUBE WITH SURFACE SUCTION",

abstract = "Numerical results are presented for the friction factor, axial pressure gradient, heat and mass transfer coefficients, and velocity and temperature profiles. The results, relevant to forced- convection condensation in a tube (with or without noncondensable gases), are substantially affected by small amounts of wall suction. The present findings do not support the current practice of using impermeable-boundary transfer coefficients in condensation calculations. tTurbulent transport is expressed by the mixing- length model, modified around the wall by a specially derived damping factor.",

author = "{KINNEY RB}, RB and Sparrow, {Ephraim M}",

year = "1969",

month = jan,

day = "1",

language = "English (US)",

note = "Unknown conference ; Conference date: 03-08-1969 Through 06-08-1969",

}

TY - CONF

T1 - TURBULENT FLOW, HEAT TRANSFER, AND MASS TRANSFER IN TUBE WITH SURFACE SUCTION

AU - KINNEY RB, RB

AU - Sparrow, Ephraim M

PY - 1969/1/1

Y1 - 1969/1/1

N2 - Numerical results are presented for the friction factor, axial pressure gradient, heat and mass transfer coefficients, and velocity and temperature profiles. The results, relevant to forced- convection condensation in a tube (with or without noncondensable gases), are substantially affected by small amounts of wall suction. The present findings do not support the current practice of using impermeable-boundary transfer coefficients in condensation calculations. tTurbulent transport is expressed by the mixing- length model, modified around the wall by a specially derived damping factor.

AB - Numerical results are presented for the friction factor, axial pressure gradient, heat and mass transfer coefficients, and velocity and temperature profiles. The results, relevant to forced- convection condensation in a tube (with or without noncondensable gases), are substantially affected by small amounts of wall suction. The present findings do not support the current practice of using impermeable-boundary transfer coefficients in condensation calculations. tTurbulent transport is expressed by the mixing- length model, modified around the wall by a specially derived damping factor.

UR - http://www.scopus.com/inward/record.url?scp=0014626631&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=0014626631&partnerID=8YFLogxK

M3 - Paper

T2 - Unknown conference

Y2 - 3 August 1969 through 6 August 1969

ER -

TURBULENT FLOW, HEAT TRANSFER, AND MASS TRANSFER IN TUBE WITH SURFACE SUCTION

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