{"title":"带内扭曲管的三螺旋管的热液压特性测定和能耗分析","authors":"","doi":"10.1016/j.cep.2024.109922","DOIUrl":null,"url":null,"abstract":"<div><p>An innovative technique to enhance heat transfer as a passive method was investigated. The combination of the twisted tube and helical coil to increase the swirl intensity is presented. The current investigation showed experimentally and numerically the exergy and thermal performance analysis of a new design of a triple tube design called a triple helical tube with inner twisted tube, <em>THTITT.</em> The new design is a modified design of a double helical tube with inner twisted tube, <em>DHTITT</em> which is created by twisting the inner tube. Besides the benefits of adding the third fluid to <em>DHTITT</em> that achieve extra contact surface area per unit length between the intermediate tube and the new passage in the outer tube. In which expected to enhance the temperature gradient between the three fluids and consequently, the thermal characteristics augment occurred. The twisted tube increased the intensity of the swirl flow and more intense disturbance of the fluid in the tube occurred. A 3d <em>CFD</em> model was established to get more insight at a level of detail not always available in the experiment. The effects of twisted pitch ratio, <em>ξ</em> hydraulic diameter, <em>ω</em>, helical coil torsion, <em>α</em>, helical coil inclination angle, <em>φ</em>, as well as Dean number, <em>N<sub>Dn, h</sub></em> were explored. Four groups of test specimens include various <em>ξ</em> of 5.32, 7.97, and ∞, various <em>ω</em> of 3.8, 6.8, and 9.9 mm, various α of 0.068, 0.095, and 0.121, and various <em>φ</em> of 0°, 45°, and 90° were established, manufactured and examined in this investigation. The investigation covered Reynolds number, <em>N<sub>Re,h</sub></em>, for a range of 2450:29300 corresponding to Dean number, <em>N<sub>Dn, h</sub></em>, for a range of 570:4800. The results showed a higher Nusselt number, <em>N<sub>Nu, h</sub></em>, of <em>THTITT</em> compared to <em>DHTITT</em> by 61.8 %%, while the increase in <em>f<sub>h</sub></em> is approximately negligible. Also, by decreasing <em>ξ</em> from ∞ to 5.32 increases <em>N<sub>Nu, h</sub></em> by 33.4 %, with an increase in friction factor, <em>f<sub>h</sub></em> by 57.6 %. Furthermore, with a decreasing <em>ω</em> from 9.9 mm to 3.8 mm, a significant increase in <em>N<sub>Nu, h</sub></em> occurs by 20.6 %, at the expense of increasing <em>f<sub>h</sub></em> by 36.4 %. In addition, with decreasing <em>α</em> from 0.121 to 0.068, a significant increase in <em>N<sub>Nu, h</sub></em> occurs by 27.6 %, at the expense of increasing <em>f<sub>h</sub></em> by 17.1 %. Finally, the <em>THTITT</em> decreases the heat loss (exergy destruction) between the hot and cold fluids. New correlations to predict <em>N<sub>Nu,h</sub>,</em> and <em>f<sub>h</sub></em> are presented.</p></div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":null,"pages":null},"PeriodicalIF":3.8000,"publicationDate":"2024-08-03","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Determining of the thermo-hydraulic characteristics and exergy analysis of a triple helical tube with inner twisted tube\",\"authors\":\"\",\"doi\":\"10.1016/j.cep.2024.109922\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>An innovative technique to enhance heat transfer as a passive method was investigated. The combination of the twisted tube and helical coil to increase the swirl intensity is presented. The current investigation showed experimentally and numerically the exergy and thermal performance analysis of a new design of a triple tube design called a triple helical tube with inner twisted tube, <em>THTITT.</em> The new design is a modified design of a double helical tube with inner twisted tube, <em>DHTITT</em> which is created by twisting the inner tube. Besides the benefits of adding the third fluid to <em>DHTITT</em> that achieve extra contact surface area per unit length between the intermediate tube and the new passage in the outer tube. In which expected to enhance the temperature gradient between the three fluids and consequently, the thermal characteristics augment occurred. The twisted tube increased the intensity of the swirl flow and more intense disturbance of the fluid in the tube occurred. A 3d <em>CFD</em> model was established to get more insight at a level of detail not always available in the experiment. The effects of twisted pitch ratio, <em>ξ</em> hydraulic diameter, <em>ω</em>, helical coil torsion, <em>α</em>, helical coil inclination angle, <em>φ</em>, as well as Dean number, <em>N<sub>Dn, h</sub></em> were explored. Four groups of test specimens include various <em>ξ</em> of 5.32, 7.97, and ∞, various <em>ω</em> of 3.8, 6.8, and 9.9 mm, various α of 0.068, 0.095, and 0.121, and various <em>φ</em> of 0°, 45°, and 90° were established, manufactured and examined in this investigation. The investigation covered Reynolds number, <em>N<sub>Re,h</sub></em>, for a range of 2450:29300 corresponding to Dean number, <em>N<sub>Dn, h</sub></em>, for a range of 570:4800. The results showed a higher Nusselt number, <em>N<sub>Nu, h</sub></em>, of <em>THTITT</em> compared to <em>DHTITT</em> by 61.8 %%, while the increase in <em>f<sub>h</sub></em> is approximately negligible. Also, by decreasing <em>ξ</em> from ∞ to 5.32 increases <em>N<sub>Nu, h</sub></em> by 33.4 %, with an increase in friction factor, <em>f<sub>h</sub></em> by 57.6 %. Furthermore, with a decreasing <em>ω</em> from 9.9 mm to 3.8 mm, a significant increase in <em>N<sub>Nu, h</sub></em> occurs by 20.6 %, at the expense of increasing <em>f<sub>h</sub></em> by 36.4 %. In addition, with decreasing <em>α</em> from 0.121 to 0.068, a significant increase in <em>N<sub>Nu, h</sub></em> occurs by 27.6 %, at the expense of increasing <em>f<sub>h</sub></em> by 17.1 %. Finally, the <em>THTITT</em> decreases the heat loss (exergy destruction) between the hot and cold fluids. New correlations to predict <em>N<sub>Nu,h</sub>,</em> and <em>f<sub>h</sub></em> are presented.</p></div>\",\"PeriodicalId\":9929,\"journal\":{\"name\":\"Chemical Engineering and Processing - Process Intensification\",\"volume\":null,\"pages\":null},\"PeriodicalIF\":3.8000,\"publicationDate\":\"2024-08-03\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chemical Engineering and Processing - Process Intensification\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0255270124002605\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q3\",\"JCRName\":\"ENERGY & FUELS\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering and Processing - Process Intensification","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0255270124002605","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
Determining of the thermo-hydraulic characteristics and exergy analysis of a triple helical tube with inner twisted tube
An innovative technique to enhance heat transfer as a passive method was investigated. The combination of the twisted tube and helical coil to increase the swirl intensity is presented. The current investigation showed experimentally and numerically the exergy and thermal performance analysis of a new design of a triple tube design called a triple helical tube with inner twisted tube, THTITT. The new design is a modified design of a double helical tube with inner twisted tube, DHTITT which is created by twisting the inner tube. Besides the benefits of adding the third fluid to DHTITT that achieve extra contact surface area per unit length between the intermediate tube and the new passage in the outer tube. In which expected to enhance the temperature gradient between the three fluids and consequently, the thermal characteristics augment occurred. The twisted tube increased the intensity of the swirl flow and more intense disturbance of the fluid in the tube occurred. A 3d CFD model was established to get more insight at a level of detail not always available in the experiment. The effects of twisted pitch ratio, ξ hydraulic diameter, ω, helical coil torsion, α, helical coil inclination angle, φ, as well as Dean number, NDn, h were explored. Four groups of test specimens include various ξ of 5.32, 7.97, and ∞, various ω of 3.8, 6.8, and 9.9 mm, various α of 0.068, 0.095, and 0.121, and various φ of 0°, 45°, and 90° were established, manufactured and examined in this investigation. The investigation covered Reynolds number, NRe,h, for a range of 2450:29300 corresponding to Dean number, NDn, h, for a range of 570:4800. The results showed a higher Nusselt number, NNu, h, of THTITT compared to DHTITT by 61.8 %%, while the increase in fh is approximately negligible. Also, by decreasing ξ from ∞ to 5.32 increases NNu, h by 33.4 %, with an increase in friction factor, fh by 57.6 %. Furthermore, with a decreasing ω from 9.9 mm to 3.8 mm, a significant increase in NNu, h occurs by 20.6 %, at the expense of increasing fh by 36.4 %. In addition, with decreasing α from 0.121 to 0.068, a significant increase in NNu, h occurs by 27.6 %, at the expense of increasing fh by 17.1 %. Finally, the THTITT decreases the heat loss (exergy destruction) between the hot and cold fluids. New correlations to predict NNu,h, and fh are presented.
期刊介绍:
Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.