Dominika Kaczmarek-Piastka, Tomasz Halon, Bartosz Zajaczkowski
{"title":"3 ~ 5kpa下管束池沸腾的实验研究","authors":"Dominika Kaczmarek-Piastka, Tomasz Halon, Bartosz Zajaczkowski","doi":"10.1016/j.ijheatmasstransfer.2025.127878","DOIUrl":null,"url":null,"abstract":"<div><div>This paper presents an experimental investigation of pool boiling of water on isolated copper tubes and vertically aligned tandem tube bundles under subatmospheric conditions, with saturation pressures of 3 and 5 kPa. The experimental setup represents compact, staggered tube arrangements used in low-temperature evaporators. All tests were performed on 25.4 mm diameter tubes with a pitch-to-diameter ratio of 1.0 and at two liquid levels (0 cm and 20 cm), to explore the effects of the hydrostatic head and subcooling on boiling heat transfer. For these thermohydraulic and geometrical configurations, boiling curves were obtained under systematically controlled conditions.</div><div>High-speed imaging was used to correlate bubble dynamics and vapor structures with heat transfer performance. The results demonstrate the sensitivity of the boiling behavior to system pressure, subcooling, and vertical tube interaction. In particular, on the top tube under base level (<span><math><mrow><msub><mrow><mi>L</mi></mrow><mrow><mi>h</mi></mrow></msub><mo>=</mo><mn>0</mn></mrow></math></span> cm) conditions, phenomena such as vapor blanketing, rupture, and droplet and film evaporation on partially exposed surfaces were observed. The onset of nucleate boiling occurred at wall superheats of approximately 4.5–5 K. The corresponding heat fluxes ranged from 12.7 to 21.2 kW/m<span><math><msup><mrow></mrow><mrow><mn>2</mn></mrow></msup></math></span>, depending on tube position, liquid level, and system pressure. In tandem tube configurations, vapor interactions from the bottom tube enhance nucleation and reduce wall superheat on the top tube by approximately 1–2 K, confirming the presence of a bundle effect.</div><div>Detailed boiling curve measurements and high-speed visualization for compact staggered tube bundles at saturation pressures as low as 3 kPa are shown in this paper. These findings provide new insights into low-pressure boiling and the performance of compact heat exchangers.</div></div>","PeriodicalId":336,"journal":{"name":"International Journal of Heat and Mass Transfer","volume":"256 ","pages":"Article 127878"},"PeriodicalIF":5.8000,"publicationDate":"2025-10-16","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Experimental study of pool boiling on tube bundles at 3 to 5 kPa\",\"authors\":\"Dominika Kaczmarek-Piastka, Tomasz Halon, Bartosz Zajaczkowski\",\"doi\":\"10.1016/j.ijheatmasstransfer.2025.127878\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>This paper presents an experimental investigation of pool boiling of water on isolated copper tubes and vertically aligned tandem tube bundles under subatmospheric conditions, with saturation pressures of 3 and 5 kPa. The experimental setup represents compact, staggered tube arrangements used in low-temperature evaporators. All tests were performed on 25.4 mm diameter tubes with a pitch-to-diameter ratio of 1.0 and at two liquid levels (0 cm and 20 cm), to explore the effects of the hydrostatic head and subcooling on boiling heat transfer. For these thermohydraulic and geometrical configurations, boiling curves were obtained under systematically controlled conditions.</div><div>High-speed imaging was used to correlate bubble dynamics and vapor structures with heat transfer performance. The results demonstrate the sensitivity of the boiling behavior to system pressure, subcooling, and vertical tube interaction. In particular, on the top tube under base level (<span><math><mrow><msub><mrow><mi>L</mi></mrow><mrow><mi>h</mi></mrow></msub><mo>=</mo><mn>0</mn></mrow></math></span> cm) conditions, phenomena such as vapor blanketing, rupture, and droplet and film evaporation on partially exposed surfaces were observed. The onset of nucleate boiling occurred at wall superheats of approximately 4.5–5 K. The corresponding heat fluxes ranged from 12.7 to 21.2 kW/m<span><math><msup><mrow></mrow><mrow><mn>2</mn></mrow></msup></math></span>, depending on tube position, liquid level, and system pressure. In tandem tube configurations, vapor interactions from the bottom tube enhance nucleation and reduce wall superheat on the top tube by approximately 1–2 K, confirming the presence of a bundle effect.</div><div>Detailed boiling curve measurements and high-speed visualization for compact staggered tube bundles at saturation pressures as low as 3 kPa are shown in this paper. These findings provide new insights into low-pressure boiling and the performance of compact heat exchangers.</div></div>\",\"PeriodicalId\":336,\"journal\":{\"name\":\"International Journal of Heat and Mass Transfer\",\"volume\":\"256 \",\"pages\":\"Article 127878\"},\"PeriodicalIF\":5.8000,\"publicationDate\":\"2025-10-16\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"International Journal of Heat and Mass Transfer\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S001793102501213X\",\"RegionNum\":2,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"ENGINEERING, MECHANICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"International Journal of Heat and Mass Transfer","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S001793102501213X","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, MECHANICAL","Score":null,"Total":0}
Experimental study of pool boiling on tube bundles at 3 to 5 kPa
This paper presents an experimental investigation of pool boiling of water on isolated copper tubes and vertically aligned tandem tube bundles under subatmospheric conditions, with saturation pressures of 3 and 5 kPa. The experimental setup represents compact, staggered tube arrangements used in low-temperature evaporators. All tests were performed on 25.4 mm diameter tubes with a pitch-to-diameter ratio of 1.0 and at two liquid levels (0 cm and 20 cm), to explore the effects of the hydrostatic head and subcooling on boiling heat transfer. For these thermohydraulic and geometrical configurations, boiling curves were obtained under systematically controlled conditions.
High-speed imaging was used to correlate bubble dynamics and vapor structures with heat transfer performance. The results demonstrate the sensitivity of the boiling behavior to system pressure, subcooling, and vertical tube interaction. In particular, on the top tube under base level ( cm) conditions, phenomena such as vapor blanketing, rupture, and droplet and film evaporation on partially exposed surfaces were observed. The onset of nucleate boiling occurred at wall superheats of approximately 4.5–5 K. The corresponding heat fluxes ranged from 12.7 to 21.2 kW/m, depending on tube position, liquid level, and system pressure. In tandem tube configurations, vapor interactions from the bottom tube enhance nucleation and reduce wall superheat on the top tube by approximately 1–2 K, confirming the presence of a bundle effect.
Detailed boiling curve measurements and high-speed visualization for compact staggered tube bundles at saturation pressures as low as 3 kPa are shown in this paper. These findings provide new insights into low-pressure boiling and the performance of compact heat exchangers.
期刊介绍:
International Journal of Heat and Mass Transfer is the vehicle for the exchange of basic ideas in heat and mass transfer between research workers and engineers throughout the world. It focuses on both analytical and experimental research, with an emphasis on contributions which increase the basic understanding of transfer processes and their application to engineering problems.
Topics include:
-New methods of measuring and/or correlating transport-property data
-Energy engineering
-Environmental applications of heat and/or mass transfer