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基于CFD的循環(huán)生物絮團(tuán)系統(tǒng)渦旋分離器結(jié)構(gòu)參數(shù)優(yōu)化
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“十二五”國家科技支撐計(jì)劃項(xiàng)目(2014BAD08B09),、國家自然科學(xué)基金青年基金項(xiàng)目(31402348)、中國水產(chǎn)科學(xué)研究院漁業(yè)機(jī)械儀器研究所重點(diǎn)實(shí)驗(yàn)室開發(fā)基金項(xiàng)目(2015)和中國博士后科學(xué)基金項(xiàng)目(2014M551747)


Structural Parameter Optimization of Hydraulic Vertox Separator in Recirculating Biofloc Technology System Based on Computational Fluid Dynamics
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    摘要:

    為提高循環(huán)生物絮團(tuán)系統(tǒng)渦旋分離器分離效率,,以歐拉-歐拉多相湍流模型為理論框架,運(yùn)用計(jì)算流體力學(xué)技術(shù),,對(duì)3種不同筒徑比α渦旋分離器內(nèi)固液兩相三維流動(dòng)進(jìn)行了數(shù)值模擬,,并分析了相關(guān)速度云圖、速度矢量云圖,、流體跡線云圖,、內(nèi)部固相分布以及出口處固相體積分?jǐn)?shù)變化等。模擬結(jié)果表明:在進(jìn)水口進(jìn)水速度為0.36m/s時(shí),,隨著筒徑比α的增大,,3種渦旋分離器套筒外側(cè)以及進(jìn)水口以下部分速度流場(chǎng)差別較小,但套筒內(nèi)流場(chǎng)湍流逐漸加劇,,同時(shí),,套筒外側(cè)附近和套筒內(nèi)部,渦旋逐漸加劇,,增加能耗,,且不利于固體顆粒的沉積,總體而言,,渦旋分離器在α為1.5之后分離效率下降,,并保持相對(duì)穩(wěn)定,具體表現(xiàn)為,,當(dāng)渦旋分離器α為1.5時(shí),,內(nèi)部固相體積分?jǐn)?shù)相對(duì)較高,而出口處固相體積分?jǐn)?shù)較低,,隨著α增大,,其分離效率由α為1.5時(shí)的27%降至α為2.0時(shí)的17%,,并隨著α再次增至2.5時(shí),分離效率保持基本不變,。渦旋分離器流場(chǎng)速度的實(shí)測(cè)結(jié)果與模擬結(jié)果基本一致,,而分離效率存在一定差異,但是變化規(guī)律相同,,表明數(shù)值模擬在優(yōu)化渦旋分離器結(jié)構(gòu)方面是可行的,。

    Abstract:

    With the aim to improve the separation efficiency of hydraulic vortex separator (HDVS) in recirculating biofloc technology (RBFT) system, three HDVSs with different structural parameters were studied by using numerical method of computational fluid dynamics (CFD). The simulations of the solid-liquid phase flow in HDVSs were conducted based on an Eulerian-Eulerian multi-phase turbulence 3-D model combined with the kinetic theory of granular flow, which specifically analyzed the velocity contours, vector contours, streamlines of liquid phase, inner and outlet distribution characters of solid phase. The simulation results showed that with the increase of α, the velocity field below the inlet part and surrounding area of the sleeve had small difference at the inlet velocity of 0.36m/s. But the difference of results of inner region of sleeve was stark and the turbulence was enhanced in this regions. In addition, some swirls occurred in the inner zone of the sleeve, which added energy waste and had negative effect on the flocs separation. The separation efficiency of HDVS had a negative correlation with the increase of α. When α was 1.5, the removal efficiency was 27%, which was more effective than 17% (α was 2.0). But when α was increased from 2.0 to 2.5, the HDVSs almost had the same solid phase volume fraction at the outlet and the separation efficiencies only had a small change. To validate the accuracy of simulation results, the simulation values and experimental data were compared. The good agreement of the flow velocity and change law of the separation efficiency proves that the mentioned two fluid model (TFM) can be used to optimize the structure of HDVS.

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史明明,朱松明,葉章穎,韓志英,李建平,阮贇杰.基于CFD的循環(huán)生物絮團(tuán)系統(tǒng)渦旋分離器結(jié)構(gòu)參數(shù)優(yōu)化[J].農(nóng)業(yè)機(jī)械學(xué)報(bào),2017,48(9):287-294,278. SHI Mingming, ZHU Songming, YE Zhangying, HAN Zhiying, LI Jianping, RUAN Yunjie. Structural Parameter Optimization of Hydraulic Vertox Separator in Recirculating Biofloc Technology System Based on Computational Fluid Dynamics[J]. Transactions of the Chinese Society for Agricultural Machinery,2017,48(9):287-294,,278.

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  • 收稿日期:2017-01-18
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  • 在線發(fā)布日期: 2017-09-10
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