1,025 research outputs found

    Blade row interaction in radial turbomachines

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    A computational study has been performed to investigate the effects of blade row interaction on the performance of radial turbomachines, which was motivated by the need to improve our understanding of the blade row interaction phenomena for further improvement in the performance. High-speed centrifugal compressor stages with three settings of radial gap are configured and simulated using a three-dimensional Navier-Stokes flow method in order to investigate the impact of blade row interaction on stage efficiency. The performance predictions show that the efficiency deteriorates if the gap between blade rows is reduced to intensify blade row interaction, which is in contradiction to the general trend for stage axial compressors, hi the compressors tested, the wake chopping by diffuser vanes, which usually benefits efficiency in axial compressor stages, causes unfavourable wake compression through the diffuser passages to deteriorate the efficiency. Similarly, hydraulic turbine stages with three settings of radial gap are simulated numerically. A new three-dimensional Navier-Stokes flow method based upon the dual-time stepping technique combined with the pseudo-compressibility method has been developed for hydraulic flow simulations. This method is validated extensively with several test cases where analytical and experimental data are available, including a centrifugal pump case with blade row interaction. Some numerical tests are conducted to examine the dependency of the flow solutions on several numerical parameters, which serve to justify the sensitivity of the solutions. Then, the method is applied to performance predictions of the hydraulic turbine stages. The numerical performance predictions for the turbines show that, by reducing the radial gap, the loss generation in the nozzle increases, which has a decisive influence on stage efficiency. The blade surface boundary layer loss and wake flow mixing loss, enhanced with a higher level of flow velocity around blading and the potential flow disturbances, are responsible for the observed trend

    Rotating stall in wide vaneless diffusers

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    LES ๋ฐ URANS๋ฅผ ์ด์šฉํ•œ ์›์‹ฌํŽŒํ”„ ๋‚ด๋ถ€์˜ ๋‚œ๋ฅ˜ ์œ ๋™ํ•ด์„

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    ํ•™์œ„๋…ผ๋ฌธ(๋ฐ•์‚ฌ) -- ์„œ์šธ๋Œ€ํ•™๊ต๋Œ€ํ•™์› : ๊ณต๊ณผ๋Œ€ํ•™ ๊ธฐ๊ณ„ํ•ญ๊ณต๊ณตํ•™๋ถ€, 2021.8. ์ตœํ•ด์ฒœ.์›์‹ฌํŽŒํ”„๋Š” ๊ฐ€์žฅ ๋„๋ฆฌ ์ด์šฉ๋˜๋Š” ํŽŒํ”„๋กœ์„œ ์ €์••์—์„œ ๋‹ค์–‘ํ•œ ์‚ฐ์—… ๋ถ„์•ผ์—์„œ ๋งŽ์€ ์œ ๋Ÿ‰์„ ์ด์†กํ•˜๊ธฐ ์œ„ํ•ด ์‚ฌ์šฉ๋˜๊ณ  ์žˆ๋‹ค. ์›์‹ฌํŽŒํ”„๋Š” ๋‹ค์–‘ํ•œ ๋ฒ”์œ„์˜ ์••๋ ฅ ์ƒ์Šน ๋ฐ ์œ ๋Ÿ‰ ์กฐ๊ฑด์„ ๋งŒ์กฑํ•˜๊ธฐ ์œ„ํ•ด ์„ค๊ณ„ ์กฐ๊ฑด๋ฟ ์•„๋‹ˆ๋ผ ํƒˆ์„ค๊ณ„ ์กฐ๊ฑด์—์„œ๋„ ํ”ํžˆ ์ž‘๋™ํ•œ๋‹ค. ํƒˆ์„ค๊ณ„ ์กฐ๊ฑด์—์„œ๋Š” ํŽŒํ”„ ๋‚ด๋ถ€์—์„œ ๋” ๋ณต์žกํ•œ ๋‚œ๋ฅ˜ ์œ ๋™ ํŠน์„ฑ์ด ๋ฐœ๋‹ฌํ•˜์—ฌ ๋„๋ฆฌ ์‚ฌ์šฉ๋˜๋Š” ๋น„์ •์ƒ Reynolds ํ‰๊ท  Navier-Stokes ๋‚œ๋ฅ˜ ๋ชจ๋ธ(unsteady Reyonolds Navier-Stokes: URANS)๊ฐ€ ๋ถ€์ •ํ™•ํ•œ ๊ฒฐ๊ณผ๋ฅผ ๋„์ถœํ•  ์ˆ˜ ์žˆ๋‹ค๋Š” ๊ฒƒ์ด ์ž˜ ์•Œ๋ ค์ ธ ์žˆ๋‹ค. ๋”ฐ๋ผ์„œ ์ด๋Ÿฌํ•œ ํƒˆ์„ค๊ณ„ ์กฐ๊ฑด ํ•ด์„์„ ์œ„ํ•ด์„œ๋Š” ํฐ์—๋””๋ชจ์‚ฌ(large eddy simulation: LES)์™€ ๊ฐ™์€ ๋ณด๋‹ค ์ •ํ™•ํ•œ ์ˆ˜์น˜ ํ•ด์„ ๋ฐฉ๋ฒ•์ด ์š”๊ตฌ๋œ๋‹ค. 1์žฅ์—์„œ๋Š” ์›์‹ฌํŽŒํ”„ ๋‚ด๋ถ€ ๋‚œ๋ฅ˜ ์œ ๋™ ํ•ด์„์„ ์œ„ํ•ด LES๋ฅผ ์ˆ˜ํ–‰ํ•˜๊ณ  ์„ค๊ณ„ ์กฐ๊ฑด ๋ฐ ํƒˆ์„ค๊ณ„ ์กฐ๊ฑด์—์„œ์˜ ์œ ๋™ ํŠน์„ฑ์„ ๋ถ„์„ํ•˜์˜€๋‹ค. ์ž„ํŽ ๋Ÿฌ ๋ธ”๋ ˆ์ด๋“œ์˜ ์••๋ ฅ ๋ฐ ํก์ž…๋ฉด ๋ชจ๋‘์—์„œ ์œ ๋™ ๋ฐ•๋ฆฌ๊ฐ€ ๋ฐœ์ƒํ•˜์˜€๊ณ , ํŠนํžˆ ํƒˆ์„ค๊ณ„ ์กฐ๊ฑด์—์„œ๋Š” ๋ธ”๋ ˆ์ด๋“œ ์••๋ ฅ๋ฉด์˜ ๋ฐ•๋ฆฌ ๊ธฐํฌ๊ฐ€ ๋น„์ •์ƒ ํŠน์„ฑ์„ ๋‚˜ํƒ€๋‚ด๋ฉฐ ๋ณผ๋ฃจํŠธ ํ˜€ ๋ถ€๊ทผ์—์„œ ๋” ํฌ๊ฒŒ ๋ฐœ๋‹ฌํ•˜์˜€๋‹ค. ๋ธ”๋ ˆ์ด๋“œ ํšŒ์ „์— ๋”ฐ๋ผ ๋ธ”๋ ˆ์ด๋“œ ํ›„๋‹จ์œผ๋กœ๋ถ€ํ„ฐ ์™€๋ฅ˜ ๊ตฌ์กฐ๊ฐ€ ๋ฐœ์ƒํ•˜์˜€๊ณ  ํƒˆ์„ค๊ณ„ ์กฐ๊ฑด์—์„œ๋Š” ์ด๋“ค์ด ๋‹ค์Œ ๋ธ”๋ ˆ์ด๋“œ ํ›„๋‹จ ์™€๋ฅ˜์™€ ๊ฐ•ํ•˜๊ฒŒ ์ƒํ˜ธ ์ž‘์šฉํ•˜์—ฌ ๋ณผ๋ฃจํŠธ ๋‚ด๋ถ€์—์„œ ๋” ๊ฐ•ํ•œ ์™€๋„์žฅ์„ ์ƒ์„ฑํ•˜์˜€๋‹ค. ์ž„ํŽ ๋Ÿฌ ์ฃผ๋ณ€ ์••๋ ฅ ์„ญ๋™์„ ์‚ดํŽด๋ณด๊ธฐ ์œ„ํ•ด์„œ ์‚ผ์ค‘ ๋ถ„ํ•ด๋ฅผ ์ˆ˜ํ–‰ํ•˜์˜€๋‹ค. ์••๋ ฅ์˜ ๋‚œ๋ฅ˜ ์„ญ๋™์€ ๋ณผ๋ฃจํŠธ ํ˜€ ๋ถ€๊ทผ์—์„œ ํฌ๊ฒŒ ์ฆ๊ฐ€ํ•˜์˜€๊ณ  ํŠนํžˆ ํƒˆ์„ค๊ณ„ ์กฐ๊ฑด์—์„œ๋Š” ์ฃผ๊ธฐ์  ์„ญ๋™๋ณด๋‹ค ๊ฐ•ํ•˜๊ฒŒ ๋ฐœ๋‹ฌํ•˜์˜€๋‹ค. ๋ณผ๋ฃจํŠธ ํ˜€์—์„œ๋Š” ์œ ๋™ ๋ฐ•๋ฆฌ๊ฐ€ ๋ฐœ์ƒํ•˜์˜€๋‹ค. ํŠนํžˆ ํƒˆ์„ค๊ณ„ ์กฐ๊ฑด์—์„œ๋Š” ๋งŽ์€ ์œ ๋Ÿ‰์ด ์ถœ๊ตฌ ํŒŒ์ดํ”„๋กœ ํ๋ฅด์ง€ ์•Š๊ณ  ์ž„ํŽ ๋Ÿฌ-๋ณผ๋ฃจํŠธ ๊ฐ„๊ทน์„ ๋”ฐ๋ผ ๋ณผ๋ฃจํŠธ ์ƒ๋ฅ˜๋กœ ๋ˆ„์„ค๋˜์—ˆ๋‹ค. ์ด๋Š” ๋ธ”๋ ˆ์ด๋“œ ์••๋ ฅ๋ฉด์— ๊ฐ•ํ•œ ์—ญ์••๋ ฅ ๊ตฌ๋ฐฐ๋ฅผ ํ˜•์ƒํ•˜์—ฌ ๋ฐ•๋ฆฌ๊ธฐํฌ์˜ ์žฌ๋ถ€์ฐฉ์„ ์ง€์—ฐ์‹œํ‚ค๊ณ  ๋น„์ •์ƒ์ ์ธ ์œ ๋™๋ฐ•๋ฆฌ ํ˜„์ƒ์„ ์ƒ์„ฑํ•˜์˜€๋‹ค. ๋˜ํ•œ ๋ณผ๋ฃจํŠธ์—์„œ์˜ ๋†’์€ ์••๋ ฅ์€ ์ถ• ๋ฐฉํ–ฅ์œผ๋กœ์˜ ์••๋ ฅ ๊ตฌ๋ฐฐ๋ฅผ ํ˜•์„ฑํ•˜๊ณ  ๋ฐ˜๊ฒฝ ๋ฐฉํ–ฅ ๊ฐ„๊ทน์œผ๋กœ ๋ˆ„์„ค ์œ ๋™์„ ์•ผ๊ธฐํ•˜์˜€๋‹ค. ํƒˆ์„ค๊ณ„ ์กฐ๊ฑด์—์„œ๋Š” ๋ณผ๋ฃจํŠธ ๋‚ด๋ถ€์—์„œ ๋” ๋†’์€ ์••๋ ฅ์ด ํ˜•์„ฑ๋˜์–ด ๋ˆ„์„ค ์œ ๋™์ด ๊ฐ•ํ•˜๊ฒŒ ๋ฐœ๋‹ฌํ•˜๋ฉฐ ๋ณผ๋ฃจํŠธ ๋‚ด๋ถ€์—์„œ์˜ ์ด์ฐจ ์œ ๋™์˜ ๋ฐœ๋‹ฌ์— ๊ธฐ์—ฌํ•˜์˜€๋‹ค. ์ด๋Ÿฌํ•œ ์›์‹ฌํŽŒํ”„ ๋‚ด๋ถ€์˜ ๋‹ค์–‘ํ•œ ์†์‹ค์œ ๋™์€ ์ž„ํŽ ๋Ÿฌ-๋ณผ๋ฃจํŠธ ์ƒํ˜ธ์ž‘์šฉ์— ์˜ํ•ด ์˜ํ–ฅ์„ ๋ฐ›์•„ ํƒˆ์„ค๊ณ„ ์กฐ๊ฑด์—์„œ ๋” ํฌ๊ฒŒ ๋ฐœ๋‹ฌํ•˜์˜€๋‹ค. 2์žฅ์—์„œ๋Š” URANS ํ•ด์„์„ ์ˆ˜ํ–‰ํ•˜๊ณ  ์ด๋ฅผ LES์—์„œ์˜ ์œ ๋™ ํŠน์„ฑ๊ณผ ๋น„๊ตํ•˜์˜€๋‹ค. LES๋Š” ๋‘ ์œ ๋Ÿ‰ ์กฐ๊ฑด์—์„œ ํŽŒํ”„์˜ ์••๋ ฅ ์ƒ์Šน ๋ฐ ํšจ์œจ์„ ์ž˜ ์˜ˆ์ธกํ•˜์˜€์ง€๋งŒ, URANS๋Š” ์ด๋“ค์„ ๊ณผ๋‹ค ์˜ˆ์ธกํ•˜์˜€๋‹ค. URANS์˜ ๋ธ”๋ ˆ์ด๋“œ ํ›„๋‹จ ์™€๋ฅ˜ ๊ตฌ์กฐ๋Š” LES์˜ ์ˆœ๊ฐ„ ์œ ๋™ ๊ตฌ์กฐ๋ฅผ ์ž˜ ๋‚˜ํƒ€๋‚ด์ง€ ๋ชป ํ•˜์˜€๊ณ , ์˜คํžˆ๋ ค LES์˜ ์ƒํ‰๊ท  ์œ ๋™ ๊ตฌ์กฐ์™€ ์œ ์‚ฌํ•œ ์™€๋„์žฅ์„ ๋‚˜ํƒ€๋‚ด์—ˆ๋‹ค. ์„ค๊ณ„์ ์—์„œ LES ๋ฐ URANS๋Š” ๋ธ”๋ ˆ์ด๋“œ ํ‘œ๋ฉด์„ ๋”ฐ๋ผ ์œ ์‚ฌํ•œ ์••๋ ฅ ๋ฐ ๋งˆ์ฐฐํ•ญ๋ ฅ ๋ถ„ํฌ๋ฅผ ๋‚˜ํƒ€๋‚ด์—ˆ๋‹ค. ํ•˜์ง€๋งŒ ํƒˆ์„ค๊ณ„์ ์—์„œ๋Š” LES๋Š” ๋ณผ๋ฃจํŠธ ํ˜€ ๋ถ€๊ทผ ๋ธ”๋ ˆ์ด๋“œ ์••๋ ฅ๋ฉด์„ ๋”ฐ๋ผ ๋ฐ•๋ฆฌ๊ธฐํฌ์˜ ์žฌ๋ถ€์ฐฉ์ด ์ง€์—ฐ๋˜์–ด ๋” ํฐ ๋ฐ•๋ฆฌ๊ธฐํฌ๊ฐ€ ํ˜•์„ฑ๋˜์—ˆ๋Š”๋ฐ, URANS๋Š” ์ด๋ฅผ ์˜ˆ์ธกํ•˜์ง€ ๋ชป ํ•˜์˜€๋‹ค. ์ž„ํŽ ๋Ÿฌ ์ฃผ๋ณ€์—์„œ์˜ ์••๋ ฅ ์„ญ๋™์€ URANS๊ฐ€ ์ฃผ๊ธฐ์  ์„ญ๋™ ์„ฑ๋ถ„์€ ๋น„๊ต์  ์ž˜ ์˜ˆ์ธกํ•˜์ง€๋งŒ, ๋‚œ๋ฅ˜ ์„ญ๋™์„ ์ž˜ ์˜ˆ์ธกํ•˜์ง€ ๋ชป ํ•˜๋Š” ๊ฒƒ์„ ๋ณด์—ฌ์ฃผ์—ˆ๋‹ค. ๋”ฐ๋ผ์„œ ๋‚œ๋ฅ˜ ์„ญ๋™์ด ์ค‘์š”ํ•ด์ง€๋Š” ํƒˆ์„ค๊ณ„์ ์—์„œ๋Š” URANS๋ฅผ ํ†ตํ•œ ์••๋ ฅ ์„ญ๋™ ์˜ˆ์ธก์ด ๋ถ€์ •ํ™•ํ•œ ๊ฒฐ๊ณผ๋ฅผ ๋‚˜ํƒ€๋‚ด์—ˆ๋‹ค. ๋˜ํ•œ ์„ค๊ณ„์ ์—์„œ๋Š” LES ๋ฐ URANS๊ฐ€ ๋ณผ๋ฃจํŠธ ๋‚ด๋ถ€๋ฅผ ๋”ฐ๋ผ ์œ ์‚ฌํ•œ ์ „์•• ๋ถ„ํฌ๋ฅผ ๋‚˜ํƒ€๋‚ด์—ˆ๋‹ค. ํ•˜์ง€๋งŒ ํƒˆ์„ค๊ณ„์ ์—์„œ๋Š” ๋ณผ๋ฃจํŠธ ํ˜€์—์„œ ๋ฐœ์ƒํ•˜๋Š” ์œ ๋™๋ฐ•๋ฆฌ๊ฐ€ ์†์‹ค์„ ์•ผ๊ธฐํ•˜๊ณ  ๋ณผ๋ฃจํŠธ ์ƒ๋ฅ˜์—์„œ ์ „์••์ด ํฌ๊ฒŒ ๊ฐ์†Œํ•˜์˜€๋‹ค. URANS๋Š” ์ด๋Ÿฌํ•œ ์†์‹ค์„ ์ž˜ ์˜ˆ์ธกํ•˜์ง€ ๋ชป ํ•˜์˜€์ง€๋งŒ ์ด์™ธ ์˜์—ญ์—์„œ๋Š” ์ „์•• ๋ถ„ํฌ๋ฅผ ์ž˜ ์˜ˆ์ธกํ•˜์˜€๋‹ค. ๋˜ํ•œ ๋ณธ ์—ฐ๊ตฌ์—์„œ์˜ ํŽŒํ”„์—์„œ๋Š” ํ† ์ถœ ํŒŒ์ดํ”„์˜ ๊ณก๋ฅ  ๋ฐ ๋ฉด์  ์ฆ๊ฐ€๋กœ ์ธํ•ด ๊ฐ•ํ•œ ์™€๋ฅ˜ ์œ ๋™์ด ๋ฐœ์ƒํ•˜์˜€๋‹ค. ์ด๋Ÿฌํ•œ ์™€๋ฅ˜ ์œ ๋™์€ ํฐ ์†์‹ค์„ ์•ผ๊ธฐํ•˜๊ณ  ์ด๋Š” ์„ค๊ณ„ ์กฐ๊ฑด์—์„œ ๋†’์€ ์œ ๋Ÿ‰์œผ๋กœ ์ธํ•ด ๋” ํฌ๊ฒŒ ๋ฐœ๋‹ฌํ•˜์˜€๋‹ค. LES๋Š” ์ด๋Ÿฌํ•œ ์™€๋ฅ˜ ์œ ๋™ ๋ฐ ์†์‹ค์„ ์ž˜ ์˜ˆ์ธกํ•˜์—ฌ ์‹คํ—˜์—์„œ์˜ ์••๋ ฅ ์ƒ์Šน ๋ฐ ํšจ์œจ์„ ์ž˜ ์˜ˆ์ธกํ•˜์˜€์ง€๋งŒ, URANS๋Š” ์ด๋ฅผ ์˜ˆ์ธกํ•˜์ง€ ๋ชป ํ•˜์—ฌ ํŽŒํ”„ ์„ฑ๋Šฅ์„ ๊ณผ๋‹ค์˜ˆ์ธกํ•˜์˜€๋‹ค.Centrifugal pumps, which are the most common type of pumps, are widely used in various industrial applications. Centrifugal pumps often operate at off-design conditions as well as at the design condition to meet various ranges of pressure rise and flow rates required. At off-design conditions, more complex and unsteady flows develop inside pumps making an accurate prediction of the flow challenging. Commonly used Reynolds-averaged Navier-Stokes (RANS) turbulence model often inaccurately predict turbulent flow inside centrifugal pumps at off-design conditions. Therefore, more accurate numerical method like large eddy simulation (LES) is demanding. In part 1, we perform LES to investigate turbulent flow inside a volute-type centrifugal pump for the design and off-design condition. Along the pressure and suction sides of impeller blades, separation bubbles are generated. At the off-design condition, the blade pressure side near the tongue contains a larger separation bubble with highly unsteady characteristics due to the impeller-volute interaction. The trailing vortices shed from rotating blades strongly interact with those from the following blade at the off-design condition, generating stronger vorticity field in a wider region inside the volute. On the other hand, this mutual interaction of vortices shed from consecutive blades is weak at the design condition. Triple decomposition of pressure fluctuations along the impeller periphery demonstrates that turbulent fluctuations are small at the design condition, whereas they become significant at the off-design condition especially near the tongue. Flow separation also occurs at the volute tongue. At the off-design condition, a large amount of volute flow does not follow the main stream to the discharge pipe but re-enters into the volute upstream near the tongue. This pressurized fluid forms a high adverse pressure gradient on the blade pressure side, resulting in strong unsteady separation there. Also, a high pressure gradient in the axial direction at the radial gaps is formed especially near the tongue, creating the leakage into the cavities. Inside the volute, secondary vortices grow along the volute passage. A secondary motion induced by these vortices also significantly affects the leakage to the cavities. All of these flow losses show unsteady features that are strongly influenced by impeller-volute interactions, especially at the off-design condition. In part 2, we conduct unsteady Reynolds-averaged Navier-Stokes (URANS) simulation and compare the flow characteristics with that by LES. URANS overpredicts the head coefficient and efficiency of the pump, whereas LES shows very good agreement with experiments. Vorticity fields inside the impeller and volute show that URANS does not resolve the instantaneous nature of turbulent flows. Rather, URANS displays similar magnitude and distribution of vorticity to phase-averaged fields by LES, indicating it provides phase-averaged flow features to some degree. Inside the impeller passage, for the design condition, LES and URANS show homogeneous characteristics for pressure and skin friction between five blades. On the other hand, along the blade pressure side for the off-design condition, LES reveals that higher pressure is induced near the tongue than the other four blades, delaying the reattachment of the separation bubble there. However, URANS does not show this larger separation bubble near the tongue. Along the impeller periphery, pressure fluctuations by LES and URANS are compared. For both flow conditions, URANS predicts periodic fluctuations well, whereas turbulent fluctuations are largely underestimated. Therefore, total fluctuations by LES and URANS exhibit satisfactory agreement at the design condition, whereas those at the off-design condition shows significant difference because of increased turbulent fluctuations for the latter condition. The time-averaged total pressure coefficient by LES and URANS shows good agreement at the design condition inside the volute. However, at the off-design condition, total pressure decreases at the volute upstream due to flow separation at the tongue. URANS does not predict these losses, overestimating total pressure there. Inside the discharge pipe for the present pump, strong flow separation and swirls are observed by LES due to the curvature and area expansion of the pipe. The losses by these swirls are larger for the design condition because of the higher mean flow rate. However, URANS does not capture strong swirls and subsequent losses, resulting in overprediction of the pressure rise and efficiency.Part I Large eddy simulation of turbulent flow in a centrifugal pump 1 1 Introduction 2 2 Numerical details 5 2.1. Pump specifications and operating conditions 5 2.2. Governing equations and computational setup 6 2.3. Resolution studies and comparison to experiments 8 3 Results and discussions 15 3.1. Overall flow structures in a centrifugal pump 15 3.2. The flow characteristics inside the impeller 17 3.2.1. Relative eddy and equations of motion in a noninertial frame 17 3.2.2. Qualitative analysis of flow structures inside the impeller 18 3.2.3. Quantitative analysis of flow characteristics inside the impeller 21 3.3. Impeller-volute interaction 23 3.3.1. Trailing vortices shed from blades and flow separation at the tongue 23 3.3.2. Pressure fluctuations along the impeller periphery 25 3.3.3. Leakage through the radial gaps 27 4 Summary and concluding remarks 43 Part II LES vs. URANS: turbulent flow in a centrifugal pump 46 1 Introduction 47 2 Numerical details of URANS 53 3 Results and discussions 55 3.1. Resolution studies and comparison to experiments 55 3.2. Flow near the interface between the impeller blade and volute 57 3.3. Flow characteristics inside the impeller 59 3.4. Radial thrust and pressure fluctuations along the impeller periphery 62 3.5. Flow features inside the volute 65 3.6. Flow characteristics inside the discharge pipe 68 4 Summary and concluding remarks 86 References 90 A Modified volute casing to reduce the leakage to cavities 98 B Circumferential grooves to reduce the leakage to the pump inlet 101 Abstract (in Korean) 104๋ฐ•

    3D numerical simulation of pump cavitating behavior

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    The quasi-steady cavitating behavior of three pumps was investigated by 3D unsteady viscous computations. The numerical model is based on the commercial code FINE/TURBOโ„ข, which was adapted to take into account the cavitation phenomenon. The resolution resorts to a time-marching algorithm initially devoted to compressible flows. A low-speed preconditioner is applied to treat low Mach number flows. The vaporization and condensation processes are controlled by a barotropic state law that links the void ratio evolution to the pressure variations. A radial pump, a centrifugal pump, and a turbopump inducer were calculated and the cavitating behaviors obtained by the computations were compared to experimental measurements and visualizations. A reliable agreement is obtained for the two pumps concerning both the head drop charts and the extension of the vapor structures. A qualitative good agreement with experiments is also observed in the case of the turbopump inducer. The accuracy of the numerical model is discussed for the three geometries. These simulations are a first attempt to simulate the complete 3D cavitating flows in turbomachinery. Results are promising, since the quasi-steady behaviors of the pumps in cavitating condition are found quantitatively close to the experimental ones. A continuing effort is pursued to improve the prediction accuracy, and to simulate unsteady effects observed in experiments, as, for example, rotating cavitation

    Numerical Simulation and Erosion Prediction for an Electrical Submersible Pump

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    Electrical Submersible Pumps (ESP) are widely used in the oil industry to lift oil and gas at the same time with high efficiency. Many ESPs operate with multiphase flow โ€“ liquid, gas and a low concentration of sand, thus having problems of pressure degradation and erosion. To investigate these problems, a numerical method can be used, which provides details of the inner flow field. Using the commercial software ANSYS Fluent, 3D transient multiphase simulations are conducted for a Baker Hughes made ESP MVP-G400. The simulations focus on three parts: secondary flow path in multiphase flow, pressure degradation due to gas volume fraction and erosion prediction. Aside from the main flow path, the clearances and balancing holes inside the ESP create a secondary path which enables the flow to recirculate. Although the volume flow rate in this path is low compared with the main flow path, the erosion in the secondary path cannot be neglected and can result in pump failure. In this research, a water-air-sand three phase simulation is performed on dual stages of the ESP, with all secondary path included. Second part of this research focuses on the pressure degradation due to the presence of a gas phase, especially at the first stage near the pump inlet. The compressibility of gas and the bubble break-up and coalescence effects are considered using the Population Balancing Module in ANSYS Fluent. The last part is the erosion prediction. A low concentration of sand is often inevitable during the operation of an ESP, causing erosion and reducing the life span of the ESP. This erosion becomes more severe with the existence a of gas phase. The three-phase simulations with both Eulerian multiphase and particle tracking explain the erosion and the role of gas in this process, giving a reasonable qualitative prediction on the erosion of the ESP

    Enhancement of synthetic jets by means of an integrated valve-less pump Part II. Numerical and experimental studies

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    The paper studies the performance of the new fluid jet actuator based on the novel principle of the generation of fluid jet, which has been presented in [Z. Travnicek, A.I. Fedorchenko, A.-B. Wang, Enhancement of synthetic jets by means of an integrated valve-less fluid pump. Part I. Design of the actuator, Sens. Actuators A, 120 (2005) 232-240]. The fluid jet actuator consists of a synthetic jet actuator and a valve-less pump. The resulting periodical fluid jet is intrinsically non-zero-net-mass-flux, in contrast to the traditional synthetic jet. The numerical results have been compared with the laboratory experiments comprising phase-locked smoke visualization and time-mean velocity measurements. The results have confirmed the satisfactory performance of the actuator

    Experimental rotordynamics and flow visualization approach for periodically reversed flows of a Francis - Type Pump - Turbine in generating mode at off - design operating conditions

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    A non-conventional tufting visualization method along with an image processing development and specific applied technique adapted to the flow conditions is proposed and implemented on a reduced scale model of a Francis-type reversible pump-turbine in three different turbine stages such as turbine mode, runaway mode and turbine break mode, in order to visualize rotating stall phenomenon -- Fluorescent monofilament wires along with high speed image processing and pressure sensors were installed in the narrow and vane less gap between the impeller blades and guide vanes -- Pressure fluctuations were analyzed along with tuft visualization to describe the flow with and without rotating stal
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