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氣相旋轉(zhuǎn)螺旋槽管式換熱器結(jié)構(gòu)優(yōu)化與性能試驗(yàn)
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黑龍江省自然科學(xué)基金項(xiàng)目(LH2022E098)和國(guó)家重點(diǎn)研發(fā)計(jì)劃項(xiàng)目(2021YFD2100901)


Structural Optimization and Performance Test of Gas-phase Rotating Spiral Grooved Tube Heat Exchanger
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    摘要:

    糧食干燥生產(chǎn)中換熱損失大,,存在煙氣熱量無(wú)法高效傳遞,導(dǎo)致?lián)Q熱效率低等問(wèn)題,。本文以集管殼與列管式換熱于一體的氣相旋轉(zhuǎn)螺旋槽管式換熱器為研究對(duì)象,,基于場(chǎng)協(xié)同與熱力學(xué)理論優(yōu)化螺旋槽管關(guān)鍵部件,探究螺旋槽管參數(shù)對(duì)換熱性能的影響,。以螺距,、槽深及內(nèi)外徑比為試驗(yàn)因素,以努塞爾數(shù)和阻力系數(shù)為評(píng)價(jià)指標(biāo),,進(jìn)行三因素五水平二次正交旋轉(zhuǎn)組合試驗(yàn),,采用多目標(biāo)優(yōu)化方法確定最優(yōu)參數(shù)組合,,當(dāng)螺距為24.845 mm、槽深為1.753 mm,、內(nèi)外徑比為0.897時(shí),,Nu為164.637,〖KG*4〗f為0.348,。對(duì)優(yōu)化結(jié)果進(jìn)行驗(yàn)證試驗(yàn),,試驗(yàn)結(jié)果與優(yōu)化結(jié)果基本一致。螺旋槽管平均場(chǎng)協(xié)同角β相較于圓管降低約2°,,揭示了置于殼程內(nèi)的螺旋槽管管束進(jìn)口,、出口及中間截面內(nèi)場(chǎng)協(xié)同角的分布特征,整體范圍內(nèi)的場(chǎng)協(xié)同效果有所增加,,結(jié)論符合場(chǎng)協(xié)同原理,。利用強(qiáng)化換熱綜合性能指數(shù)(Performance evaluation criteria, PEC)進(jìn)行評(píng)價(jià),結(jié)果表明氣相旋轉(zhuǎn)螺旋槽管式換熱器PEC在1.031~1.267之間,,驗(yàn)證了螺旋槽管在換熱器應(yīng)用的合理性,。

    Abstract:

    During the grain drying production, the heat transfer loss was great, and flue gas heat can not be efficiently transferred, resulting in low heat transfer efficiency and other problems. The gas-phase rotary heat exchanger integrating shell-and-shell and shell-and-tube heat exchanger was taken as the research object, and the key components of the spiral grooved tube were optimized based on the field synergy and thermodynamic theory. The influence of spiral grooved tube parameters on heat transfer performance was investigated. Pitch, groove depth and inner/outer diameter ratio were taken as test factors, and nussle number and resistance coefficient were used as evaluation indexes. Three-factor five-level quadratic orthogonal rotary combination experiments were carried out. Multi-objective optimization method was used to determine the optimal parameter combination, and nussle number was 164.637 and resistance coefficient was 0.348 when the pitch was 24.845 mm, the groove depth was 1.753 mm, and the inner/outer diameter ratio was 0.897. Verification experiments were carried out on the optimization results, and the experimental results were basically consistent with the optimization results. The average field synergy angle of the spiral grooved tube was decreased by about 2° compared with that of the circular tube, revealing the distribution characteristics of the field synergy angle in the inlet, outlet and intermediate sections of the spiral grooved tube bundle placed in the shell range, and the field synergy effect was increased in the overall range, which was concluded to be in line with the field synergy principle. The enhanced heat transfer comprehensive performance index was utilized for evaluation, and the results showed that the thermal performance factor of spiral grooved tube heat exchanger was between 1.031 and 1.267, which verified the rationality of spiral grooved tube in heat exchanger application.

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萬(wàn)霖,黃宇佳,車剛,王洪超,李俊鵬,鄭宇,田金凱.氣相旋轉(zhuǎn)螺旋槽管式換熱器結(jié)構(gòu)優(yōu)化與性能試驗(yàn)[J].農(nóng)業(yè)機(jī)械學(xué)報(bào),2024,55(10):422-432. WAN Lin, HUANG Yujia, CHE Gang, WANG Hongchao, LI Junpeng, ZHENG Yu, TIAN Jinkai. Structural Optimization and Performance Test of Gas-phase Rotating Spiral Grooved Tube Heat Exchanger[J]. Transactions of the Chinese Society for Agricultural Machinery,2024,55(10):422-432.

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  • 收稿日期:2024-07-08
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  • 在線發(fā)布日期: 2024-10-10
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