Stoffübergang und druckverlust an parallel angeströmten stabbündeln in einem grossen bereich von reynolds-zahlen und teilungsverhältnissen

Presser, K.H.

doi:10.1016/0017-9310(71)90175-x

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Single-phase Flow Of Exhaust Gas and Refrigerant1

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1972

2015

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Cited by 9 publications

(1 citation statement)

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“…The mentioned heat transfer equations of single-phase flow in tubes are commonly employed in a corrected form for the less well investigated heat transfer in tube bundles with lengthwise flow such as B2 Ex,l [41,42]. Markoczy [42] introduced the following correction:…”

Section: Single-phase Flow Of Exhaust Gas and Refrigerantmentioning

confidence: 99%

Simple models for the heat exchange from exhaust gas to super- and sub-critical refrigerant R134a at high temperature differences

Zegenhagen

Ziegler

2015

Applied Thermal Engineering

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Section: Single-phase Flow Of Exhaust Gas and Refrigerantmentioning

confidence: 99%

Simple models for the heat exchange from exhaust gas to super- and sub-critical refrigerant R134a at high temperature differences

Zegenhagen

Ziegler

2015

Applied Thermal Engineering

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Mass transfer in regular arrays of hollow fibers in countercurrent dialysis

Noda

Gryte

1979

AIChE Journal

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trol valve pi qc = output of controller q h qi q s qv S Ti To V2 V, LJTERATURE CITED Fussell, J. B., and W. E. Vesely, "A New Methodology for Obtaining Cut Sets for Fault Trees," Trans. Am. Nucl. SOC., 15, 262 ( 1972). Fussell, J. B., "Synthetic Tree Model-A Formal Methodology for Fault Tree Construction," ANCR-1098, Available from = actuating pressure of cooling water control valve = material gow rate to heat exchanger = inflow rate of material to be cooled = output of temperature sensor = flow rate of cooling water = internal mode of temperature sensor = temperature of material into heat exchanger = temperature of material out of heat exchanger = internal mode of cutoff valve = internal mode of cooling water control valveThe concentration profiles in a countercurrent hollow fiber bundle mass exchanger dialyzer is derived, assuming a uniform distribution of fibers in the dialyzer shell. Mass transfer coefficients are obtained as a function of fiber packing density, membrane thickness, membrane material, and solute tYPe* (1949), and Vyazovov (1940) have measured rates of abcal Engineers, 1979.

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Die Stoffübertragung fest-gasförmig bei laminarer freier Konvektion

Presser

1972

Wärme- und Stoffübertragung

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Stoffübergang und druckverlust an parallel angeströmten stabbündeln in einem grossen bereich von reynolds-zahlen und teilungsverhältnissen

Cited by 9 publications

References 11 publications

Simple models for the heat exchange from exhaust gas to super- and sub-critical refrigerant R134a at high temperature differences

Simple models for the heat exchange from exhaust gas to super- and sub-critical refrigerant R134a at high temperature differences

Mass transfer in regular arrays of hollow fibers in countercurrent dialysis

Die Stoffübertragung fest-gasförmig bei laminarer freier Konvektion

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