| 000 | 03959nlm1a2200433 4500 | ||
|---|---|---|---|
| 001 | 658926 | ||
| 005 | 20231030041612.0 | ||
| 035 | _a(RuTPU)RU\TPU\network\27185 | ||
| 090 | _a658926 | ||
| 100 | _a20181217a2018 k y0engy50 ba | ||
| 101 | 0 | _aeng | |
| 102 | _aNL | ||
| 135 | _adrcn ---uucaa | ||
| 181 | 0 | _ai | |
| 182 | 0 | _ab | |
| 200 | 1 |
_aThe role of convection in gas and liquid phases at droplet evaporation _fP. A. Strizhak, R. S. Volkov, S. Ya. Misyura [et al.] |
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| 203 |
_aText _celectronic |
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| 300 | _aTitle screen | ||
| 320 | _a[References: 62 tit.] | ||
| 330 | _aThe article presents the measuring results of droplet velocity and temperature fields using non-contact optical methods: Particle Image Velocity (PIV), Planar Laser Induced Fluorescence (PLIF) and Thermal imager. The novelty of the work is that the influence of free convection in gas and liquid is investigated experimentally and theoretically and that the key criteria affecting heat and mass transfer are determined. The analysis of experimental data has shown that in the initial period of water drop evaporation, the predominant role in the heat exchange is played by the thermal Marangoni convection. However, for an aqueous salt solution, in spite of the strong influence of the surfactant, the dominant role passes to the solutal Marangoni convection (MaC). In the first seconds after the drop falling, convection and heat transfer in liquid are maximal. Under such conditions it is important to realize an accurate numerical simulation to assess the degree of wall cooling and calculate the non-stationary evaporation. When simulating heat transfer, it is incorrect to neglect free convection in gas or liquid due to their strong nonlinear influence on each other. The heat exchange in the drop is extremely conservative to convection in the liquid (the Peclet number Pe?=?100 and the Nusselt number Nu?=?4). | ||
| 333 | _aРежим доступа: по договору с организацией-держателем ресурса | ||
| 461 | _tInternational Journal of Thermal Sciences | ||
| 463 |
_tVol. 134 _v[P. 421-429] _d2018 |
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| 610 | 1 | _aэлектронный ресурс | |
| 610 | 1 | _aтруды учёных ТПУ | |
| 610 | 1 | _aкапля | |
| 610 | 1 | _aиспарение | |
| 610 | 1 | _aтеплопередача | |
| 610 | 1 | _aфлуоресценция | |
| 701 | 1 |
_aStrizhak _bP. A. _cSpecialist in the field of heat power energy _cDoctor of Physical and Mathematical Sciences (DSc), Professor of Tomsk Polytechnic University (TPU) _f1985- _gPavel Alexandrovich _2stltpush _3(RuTPU)RU\TPU\pers\30871 |
|
| 701 | 1 |
_aVolkov _bR. S. _cspecialist in the field of power engineering _csenior lecturer, engineer of the Tomsk Polytechnic University, candidate of technical Sciences _f1987- _gRoman Sergeevich _2stltpush _3(RuTPU)RU\TPU\pers\33926 |
|
| 701 | 1 |
_aMisyura _bS. Ya. _cspecialist in the field of power engineering _cleading researcher of Tomsk Polytechnic University, candidate of technical sciences _f1964- _gSergey Yakovlevich _2stltpush _3(RuTPU)RU\TPU\pers\39641 |
|
| 701 | 1 |
_aLezhnin _bS. I. _gSergey Ivanovich |
|
| 701 | 1 |
_aMorozov _bV. S. _gVladimir Sergeevich |
|
| 712 | 0 | 2 |
_aНациональный исследовательский Томский политехнический университет _bИнженерная школа энергетики _bНаучно-образовательный центр И. Н. Бутакова (НОЦ И. Н. Бутакова) _h8025 _2stltpush _3(RuTPU)RU\TPU\col\23504 |
| 712 | 0 | 2 |
_aНациональный исследовательский Томский политехнический университет _bИсследовательская школа физики высокоэнергетических процессов _c(2017- ) _h8118 _2stltpush _3(RuTPU)RU\TPU\col\23551 |
| 801 | 2 |
_aRU _b63413507 _c20210201 _gRCR |
|
| 856 | 4 | _uhttps://doi.org/10.1016/j.ijthermalsci.2018.08.031 | |
| 942 | _cCF | ||