Research output: Chapter in Book/Report/Conference proceeding › Conference contribution › Research › peer-review
Special features of nucleate boiling under the abruptly escalating heat input in subcooled flow. / Levin, Anatoliy; Khan, Polina.
International Heat Transfer Conference. Begell House Inc., 2023.Research output: Chapter in Book/Report/Conference proceeding › Conference contribution › Research › peer-review
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TY - GEN
T1 - Special features of nucleate boiling under the abruptly escalating heat input in subcooled flow
AU - Levin, Anatoliy
AU - Khan, Polina
N1 - Conference code: 17
PY - 2023
Y1 - 2023
N2 - This paper considers the results of an experimental study of non-stationary nucleate boiling that develops on the heater surface as a result of abruptly escalating heat inputs. The isolated bubble model that is commonly used to describe nucleate boiling on a surface has a number of limitations. First, we have to describe the characteristics of an ensemble of bubbles instead of an idealized object, which is a single vapor bubble. Second, three different ways of interaction between bubbles (hydrodynamic, thermal, and mass transfer) are possible on the heat-releasing surface, the contribution of which should be taken into account. In the present study, we highlight the influence of these important factors on the determination of heat transfer during the development of unsteady boiling. Two regimes of nucleate boiling that are significant for numerical simulation were identified. The first one is described by existing models and represents the existence of isolated bubbles. The second regime begins with an active mass transfer between closely spaced bubbles that give rise to specific structures-bubble clusters. Such key characteristics of nucleate boiling as separation diameter, nucleation frequency, and density of vaporization centers require a special approach due to clusters that occur on the surface. The analysis of the results of high-speed video shooting (200,000 frame/sec) revealed that we have to refine the initial data of the existing heat flux partition wall boiling models. The existing approaches to determining heat transfer under nucleate boiling conditions can be extended from isolated bubbles to the formation of stable vapor structures above a heat-releasing surface.
AB - This paper considers the results of an experimental study of non-stationary nucleate boiling that develops on the heater surface as a result of abruptly escalating heat inputs. The isolated bubble model that is commonly used to describe nucleate boiling on a surface has a number of limitations. First, we have to describe the characteristics of an ensemble of bubbles instead of an idealized object, which is a single vapor bubble. Second, three different ways of interaction between bubbles (hydrodynamic, thermal, and mass transfer) are possible on the heat-releasing surface, the contribution of which should be taken into account. In the present study, we highlight the influence of these important factors on the determination of heat transfer during the development of unsteady boiling. Two regimes of nucleate boiling that are significant for numerical simulation were identified. The first one is described by existing models and represents the existence of isolated bubbles. The second regime begins with an active mass transfer between closely spaced bubbles that give rise to specific structures-bubble clusters. Such key characteristics of nucleate boiling as separation diameter, nucleation frequency, and density of vaporization centers require a special approach due to clusters that occur on the surface. The analysis of the results of high-speed video shooting (200,000 frame/sec) revealed that we have to refine the initial data of the existing heat flux partition wall boiling models. The existing approaches to determining heat transfer under nucleate boiling conditions can be extended from isolated bubbles to the formation of stable vapor structures above a heat-releasing surface.
KW - Nucleate boiling
KW - Subcooled flow boiling
KW - Unsteady heat transfer
UR - https://www.scopus.com/record/display.uri?eid=2-s2.0-85189158000&origin=inward&txGid=58f47159a891c883e34a0ec58b645854
UR - https://www.mendeley.com/catalogue/1e932e21-4a8b-311b-ac7d-596a63c68c40/
U2 - 10.1615/IHTC17.150-210
DO - 10.1615/IHTC17.150-210
M3 - Conference contribution
BT - International Heat Transfer Conference
PB - Begell House Inc.
T2 - 17th International Heat Transfer Conference
Y2 - 14 August 2023 through 18 August 2023
ER -
ID: 59893535