Kayansayan, 1994 - Google Patents
Heat transfer characterization of plate fin-tube heat exchangersKayansayan, 1994
View PDF- Document ID
- 13962128015745682826
- Author
- Kayansayan N
- Publication year
- Publication venue
- International journal of refrigeration
External Links
Snippet
The effects upon the performance of plate fin-tube cross flow heat exchangers due to outer surface geometry are considered. The finning parameter varying from 11 to 23, a total of 10 geometrically distinct configurations was tested over a Reynolds number range from 100 to …
- 238000010192 crystallographic characterization 0 title description 3
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING ENGINES OR PUMPS
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
- F28F13/12—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F1/00—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through the meter in a continuous flow
- G01F1/05—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through the meter in a continuous flow by using mechanical effects
- G01F1/34—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through the meter in a continuous flow by using mechanical effects by measuring pressure or differential pressure
- G01F1/36—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through the meter in a continuous flow by using mechanical effects by measuring pressure or differential pressure the pressure or differential pressure being created by the use of flow constriction
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING ENGINES OR PUMPS
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular lements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING ENGINES OR PUMPS
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/047—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F1/00—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through the meter in a continuous flow
- G01F1/68—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through the meter in a continuous flow by using thermal effects
- G01F1/684—Structural arrangements; Mounting of elements, e.g. in relation to fluid flow
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01K—MEASURING TEMPERATURE; MEASURING QUANTITY OF HEAT; THERMALLY-SENSITIVE ELEMENTS NOT OTHERWISE PROVIDED FOR
- G01K17/00—Measuring quantity of heat
- G01K17/06—Measuring quantity of heat conveyed by flowing mediums, e.g. in heating systems e.g. the quantity of heat in a transporting medium, delivered to or consumed in an expenditure device
- G01K17/08—Measuring quantity of heat conveyed by flowing mediums, e.g. in heating systems e.g. the quantity of heat in a transporting medium, delivered to or consumed in an expenditure device based upon measurement of temperature difference or of a temperature
- G01K17/20—Measuring quantity of heat conveyed by flowing mediums, e.g. in heating systems e.g. the quantity of heat in a transporting medium, delivered to or consumed in an expenditure device based upon measurement of temperature difference or of a temperature across a radiating surface, combined with ascertainment of the heat transmission coefficient
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING ENGINES OR PUMPS
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/08—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F1/00—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through the meter in a continuous flow
- G01F1/76—Devices for measuring mass flow of a fluid or a fluent solid material
- G01F1/86—Indirect mass flowmeters, e.g. measuring volume flow and density, temperature or pressure
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Kayansayan | Heat transfer characterization of flat plain fins and round tube heat exchangers | |
Wongwises et al. | Effect of fin pitch and number of tube rows on the air side performance of herringbone wavy fin and tube heat exchangers | |
Wang et al. | Sensible heat and friction characteristics of plate fin-and-tube heat exchangers having plane fins | |
Wang et al. | Heat transfer and friction characteristics of plain fin-and-tube heat exchangers, part I: new experimental data | |
Pongsoi et al. | Effect of fin pitches on the optimum heat transfer performance of crimped spiral fin-and-tube heat exchangers | |
Momin et al. | Heat transfer and friction in solar air heater duct with V-shaped rib roughness on absorber plate | |
Moawed | Experimental study of forced convection from helical coiled tubes with different parameters | |
Wang | Investigation of wavy fin-and-tube heat exchangers: a contribution to databank | |
Mirth et al. | Prediction of cooling-coil performance under condensing conditions | |
Ahmadi Nadooshan et al. | Perforated fins effect on the heat transfer rate from a circular tube by using wind tunnel: an experimental view | |
Marner et al. | Augmentation of tubeside laminar flow heat transfer by means of twisted-tape inserts, static-mixer inserts, and internally finned tubes | |
Kayansayan | Heat transfer characterization of plate fin-tube heat exchangers | |
Pongsoi et al. | Experimental study on the air-side performance of a multipass parallel and counter cross-flow L-footed spiral fin-and-tube heat exchanger | |
CN110309591A (en) | It exchanges heat under a kind of flat finned heat exchanger air side laminar condition and drag computation method | |
Barbosa Jr et al. | Air-side heat transfer and pressure drop in spiral wire-on-tube condensers | |
Lee et al. | Determination of airside heat transfer coefficient on wire-on-tube type heat exchanger | |
ElSherbini et al. | Experimental investigation of thermal contact resistance in plain-fin-and-tube evaporators with collarless fins | |
Jabardo et al. | Experimental study of the air side performance of louver and wave fin-and-tube coils | |
Chokeman et al. | Effect of fin pattern on the air-side performance of herringbone wavy fin-and-tube heat exchangers | |
Hofmann et al. | Heat transfer and pressure drop performance comparison of finned-tube bundles in forced convection | |
Wongwises et al. | Effect of fin thickness on air-side performance of herringbone wavy fin-and-tube heat exchangers | |
Karatas et al. | An experimental study of air-side heat transfer and friction factor correlations on domestic refrigerator finned-tube evaporator coils | |
Davies | Heat transfer and visualization in large flattened-tube condensers with variable inclination | |
Habeeb et al. | Heat Transfer Analysis of Integral-Fin Tubes | |
Kayansayan | Heat transfer characterization of plate fin-tube heat exchangers |