Movement and evaporation of water droplets under conditions typical for heat-exchange chambers of contact water heaters

Результат исследований: Материалы для журналаСтатья

1 цитирование (Scopus)

Выдержка

The macroscopic regularities and integrated characteristics of the motion and evaporation of sprayed water droplets in the field of high-temperature (1100 K) combustion products under the conditions typical for water heaters of contact type (economizers) were studied using a cross-correlation complex working on the basis of panoramic optical methods (particle image velocimetry, particle tracking velocimetry, shadow photography) and high-speed (105 fps) Phantom video cameras. High-speed video recording devices with specialized software were used for continuously monitoring the motion and evaporation of droplets. Titanium dioxide nanopowder tracer particles were introduced to determine the rate of high-temperature gases. The characteristic distances covered by water droplets before their full retardation in the counter-flow of high-temperature combustion products were determined. The integrated dependences were obtained, and the main characteristics of evaporation were determined, which allow one to predict the intensity of the phase transformations of droplets (with sizes of 0.05–0.5 mm) and the distances covered by them before they completely turn in the opposite direction under the conditions corresponding to the heat-exchange chambers of contact water heaters: the vapor-droplet rate 1–5 m/s, gas flow rate 0.5–2 m/s, and gas temperature ~1100 K. Approximating expressions were derived to predict the characteristics of the processes. The performance of the economizers under study can be significantly increased by using the obtained experimental dependences, the corresponding approximating expressions, and the resulting conclusions. Conditions were determined under which the influence of phase transformations on retardation exceeds the contribution of the counter-motion and active retardation and evaporation of water droplets occur in the heat-exchange chambers of contact water heaters of typical sizes.

Язык оригиналаАнглийский
Страницы (с-по)666-673
Число страниц8
ЖурналThermal Engineering (English translation of Teploenergetika)
Том63
Номер выпуска9
DOI
СостояниеОпубликовано - 1 сен 2016

Отпечаток

Water heaters
Evaporation
Economizers
Water
Velocity measurement
Contacts (fluid mechanics)
Phase transitions
Video recording
Temperature
Photography
Video cameras
Gases
Titanium dioxide
Flow of gases
Hot Temperature
Vapors
Flow rate
Monitoring

ASJC Scopus subject areas

  • Nuclear Energy and Engineering
  • Energy Engineering and Power Technology

Цитировать

Movement and evaporation of water droplets under conditions typical for heat-exchange chambers of contact water heaters. / Volkov, R. S.; Kuznetsov, G. V.; Strizhak, P. A.

В: Thermal Engineering (English translation of Teploenergetika), Том 63, № 9, 01.09.2016, стр. 666-673.

Результат исследований: Материалы для журналаСтатья

@article{dbe35aaf4d414169af2a5b460330f7a0,
title = "Movement and evaporation of water droplets under conditions typical for heat-exchange chambers of contact water heaters",
abstract = "The macroscopic regularities and integrated characteristics of the motion and evaporation of sprayed water droplets in the field of high-temperature (1100 K) combustion products under the conditions typical for water heaters of contact type (economizers) were studied using a cross-correlation complex working on the basis of panoramic optical methods (particle image velocimetry, particle tracking velocimetry, shadow photography) and high-speed (105 fps) Phantom video cameras. High-speed video recording devices with specialized software were used for continuously monitoring the motion and evaporation of droplets. Titanium dioxide nanopowder tracer particles were introduced to determine the rate of high-temperature gases. The characteristic distances covered by water droplets before their full retardation in the counter-flow of high-temperature combustion products were determined. The integrated dependences were obtained, and the main characteristics of evaporation were determined, which allow one to predict the intensity of the phase transformations of droplets (with sizes of 0.05–0.5 mm) and the distances covered by them before they completely turn in the opposite direction under the conditions corresponding to the heat-exchange chambers of contact water heaters: the vapor-droplet rate 1–5 m/s, gas flow rate 0.5–2 m/s, and gas temperature ~1100 K. Approximating expressions were derived to predict the characteristics of the processes. The performance of the economizers under study can be significantly increased by using the obtained experimental dependences, the corresponding approximating expressions, and the resulting conclusions. Conditions were determined under which the influence of phase transformations on retardation exceeds the contribution of the counter-motion and active retardation and evaporation of water droplets occur in the heat-exchange chambers of contact water heaters of typical sizes.",
keywords = "contact water heaters, evaporation, heat exchange chamber, high-temperature gases, water droplets",
author = "Volkov, {R. S.} and Kuznetsov, {G. V.} and Strizhak, {P. A.}",
year = "2016",
month = "9",
day = "1",
doi = "10.1134/S004060151609007X",
language = "English",
volume = "63",
pages = "666--673",
journal = "Thermal Engineering (English translation of Teploenergetika)",
issn = "0040-6015",
publisher = "Maik Nauka-Interperiodica Publishing",
number = "9",

}

TY - JOUR

T1 - Movement and evaporation of water droplets under conditions typical for heat-exchange chambers of contact water heaters

AU - Volkov, R. S.

AU - Kuznetsov, G. V.

AU - Strizhak, P. A.

PY - 2016/9/1

Y1 - 2016/9/1

N2 - The macroscopic regularities and integrated characteristics of the motion and evaporation of sprayed water droplets in the field of high-temperature (1100 K) combustion products under the conditions typical for water heaters of contact type (economizers) were studied using a cross-correlation complex working on the basis of panoramic optical methods (particle image velocimetry, particle tracking velocimetry, shadow photography) and high-speed (105 fps) Phantom video cameras. High-speed video recording devices with specialized software were used for continuously monitoring the motion and evaporation of droplets. Titanium dioxide nanopowder tracer particles were introduced to determine the rate of high-temperature gases. The characteristic distances covered by water droplets before their full retardation in the counter-flow of high-temperature combustion products were determined. The integrated dependences were obtained, and the main characteristics of evaporation were determined, which allow one to predict the intensity of the phase transformations of droplets (with sizes of 0.05–0.5 mm) and the distances covered by them before they completely turn in the opposite direction under the conditions corresponding to the heat-exchange chambers of contact water heaters: the vapor-droplet rate 1–5 m/s, gas flow rate 0.5–2 m/s, and gas temperature ~1100 K. Approximating expressions were derived to predict the characteristics of the processes. The performance of the economizers under study can be significantly increased by using the obtained experimental dependences, the corresponding approximating expressions, and the resulting conclusions. Conditions were determined under which the influence of phase transformations on retardation exceeds the contribution of the counter-motion and active retardation and evaporation of water droplets occur in the heat-exchange chambers of contact water heaters of typical sizes.

AB - The macroscopic regularities and integrated characteristics of the motion and evaporation of sprayed water droplets in the field of high-temperature (1100 K) combustion products under the conditions typical for water heaters of contact type (economizers) were studied using a cross-correlation complex working on the basis of panoramic optical methods (particle image velocimetry, particle tracking velocimetry, shadow photography) and high-speed (105 fps) Phantom video cameras. High-speed video recording devices with specialized software were used for continuously monitoring the motion and evaporation of droplets. Titanium dioxide nanopowder tracer particles were introduced to determine the rate of high-temperature gases. The characteristic distances covered by water droplets before their full retardation in the counter-flow of high-temperature combustion products were determined. The integrated dependences were obtained, and the main characteristics of evaporation were determined, which allow one to predict the intensity of the phase transformations of droplets (with sizes of 0.05–0.5 mm) and the distances covered by them before they completely turn in the opposite direction under the conditions corresponding to the heat-exchange chambers of contact water heaters: the vapor-droplet rate 1–5 m/s, gas flow rate 0.5–2 m/s, and gas temperature ~1100 K. Approximating expressions were derived to predict the characteristics of the processes. The performance of the economizers under study can be significantly increased by using the obtained experimental dependences, the corresponding approximating expressions, and the resulting conclusions. Conditions were determined under which the influence of phase transformations on retardation exceeds the contribution of the counter-motion and active retardation and evaporation of water droplets occur in the heat-exchange chambers of contact water heaters of typical sizes.

KW - contact water heaters

KW - evaporation

KW - heat exchange chamber

KW - high-temperature gases

KW - water droplets

UR - http://www.scopus.com/inward/record.url?scp=84983350447&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=84983350447&partnerID=8YFLogxK

U2 - 10.1134/S004060151609007X

DO - 10.1134/S004060151609007X

M3 - Article

AN - SCOPUS:84983350447

VL - 63

SP - 666

EP - 673

JO - Thermal Engineering (English translation of Teploenergetika)

JF - Thermal Engineering (English translation of Teploenergetika)

SN - 0040-6015

IS - 9

ER -