Zobrazeno 1 - 10
of 38
pro vyhledávání: '"B. M. Burnside"'
Publikováno v:
Applied Thermal Engineering. 115:1438-1450
Experimental data are reported for boiling water and a glycerol-water mixture at a free surface pressure of 50 mbar absolute on the shell-side of a thin slice model of an industrial boiler. The boiler test section was 1 m high, 0.75 m wide, 98 mm lon
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::fc9cee0d2dd324cbffd9dc7c98c011fe
https://doi.org/10.1016/j.applthermaleng.2016.11.169
https://doi.org/10.1016/j.applthermaleng.2016.11.169
Publikováno v:
International Journal of Heat and Mass Transfer. 85:488-504
Experimental data are reported for water boiling at pressures of 850 and 50 mbar absolute on the shell-side of a model industrial boiler slice. The boiler test section was 1 m high, 0.75 m wide and contained 36 electrically heated tubes. The tubes we
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::7337e8718d9aaec708d0d1e50f53b399
https://doi.org/10.1016/j.ijheatmasstransfer.2015.02.004
https://doi.org/10.1016/j.ijheatmasstransfer.2015.02.004
Publikováno v:
International Journal of Heat and Mass Transfer. 54:1907-1923
The two-fluid model is applied to a thin sliced kettle reboiler. The tube bundle is treated as a porous medium in which the drag coefficient and tube-wall force are deduced from the empirically-based, one-dimensional model. Methods available in the o
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::ce4341ae1a0f2294c970a379768578cf
https://doi.org/10.1016/j.ijheatmasstransfer.2011.01.012
https://doi.org/10.1016/j.ijheatmasstransfer.2011.01.012
Publikováno v:
Journal of Mechanical Engineering. 40:79-89
The paper presents the results of numerical calculations for filmwise condensation of downward flowing pure saturated steam on a horizontal tube. A tube of 19.05 mm diameter was used. Steam approach conditions used were 5000 N/m 2 (T sat = 32.9 o C)
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::39f98aae995c512087aaee1c9d913794
https://doi.org/10.3329/jme.v40i2.5347
https://doi.org/10.3329/jme.v40i2.5347
Publikováno v:
Journal of Mechanical Engineering. 41:31-41
In condensation over horizontal tubes where the wall temperature is not measured directly, the Wilson plot is used to determine the cooling side heat transfer coefficient. Conventionally, the variation in Nusselt number, Nu, with condensate side temp
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::7ec2a9a3d0c8d531d92837feb57286cb
https://doi.org/10.3329/jme.v41i1.5360
https://doi.org/10.3329/jme.v41i1.5360
Publikováno v:
International Journal of Heat and Mass Transfer. 53:825-835
A one-fluid, or algebraic slip, model has been developed to simulate two-dimensional, two-phase flow in a kettle reboiler. The model uses boundary conditions that allow for a change in flow pattern from bubbly to intermittent flow at a critical super
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::b615794fa00ace7b7326678b869f8138
https://doi.org/10.1016/j.ijheatmasstransfer.2009.11.042
https://doi.org/10.1016/j.ijheatmasstransfer.2009.11.042
Autor:
N.F. Shire, B. M. Burnside
Publikováno v:
Chemical Engineering Research and Design. 83:527-538
The paper describes tests boiling R 113 at atmospheric pressure in upward flow over a 17 row column of square pitched electrically heated tubes. Uniform heat fluxes of 10–65 kW m–2 and maximum Reynolds numbers, Remax, between 7800 and 27 000 were
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::62576ebe94b4811d2c6797130f070e2a
https://doi.org/10.1205/cherd.04313
https://doi.org/10.1205/cherd.04313
Publikováno v:
International Journal of Heat and Mass Transfer. 48:1000-1016
A particle image velocimetry (PIV) autocorrelation technique was applied to produce whole field vector maps of flow beneath and to the side of a 17 row × l7 column kettle reboiler thin slice rig, boiling pentane at atmospheric pressure. The flow pro
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::9ba87c46230630ebd2112b2e05531f39
https://doi.org/10.1016/j.ijheatmasstransfer.2004.09.023
https://doi.org/10.1016/j.ijheatmasstransfer.2004.09.023
Publikováno v:
Applied Thermal Engineering. 24:1365-1379
Pressure drop measurements were carried out in a test condenser of staggered configuration with p/D = 1.33. The test conditions were: steam inlet pressure, 50 mbar, inlet velocity 10-30 m s -1 and steam-to-cooling water temperature difference 5-15 K.
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::2a822aedbcb15ea59e209d003edfedce
https://doi.org/10.1016/j.applthermaleng.2003.11.024
https://doi.org/10.1016/j.applthermaleng.2003.11.024
Publikováno v:
Applied Thermal Engineering. 22:803-814
An experimental study has been undertaken into the enhancement obtained in the heat-transfer coefficients when HIGHFLUX tubes are used in preference to plain tubes while boiling pentane. The study involved two experimental facilities, a single-tube p
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::e9584f123fa18189d91e35cf0b24e490
https://doi.org/10.1016/s1359-4311(01)00122-3
https://doi.org/10.1016/s1359-4311(01)00122-3