降低环空扩压器的总压损失

Dajan Mimic, C. Jätz, P. Sauer, Florian Herbst
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In extension, we provide evidence that the loss production in highly loaded vortex-stabilised diffusers, which would stall otherwise, can be brought down to the level of non-stalling diffusers. Furthermore, we present a detailed analysis of the different loss mechanisms and their response to vortex-stabilisation of the diffuser. 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引用次数: 0

摘要

燃气轮机的功率输出和效率在很大程度上取决于后续扩散器可实现的压力上升。结合将扩压器长度保持在最小的要求,寻求更陡的开口角度,同时避免扩压器失速。在扩压器压力上升方面,如果利用上一级的叶尖泄漏涡来重新加速扩压器边界层,从而延迟分离的发生,则可以进一步推动可达到的边界。这些措施也被证明可以降低总压损失。在本文中,我们通过数值和实验验证的方法表明,在更陡的开角下,涡稳定扩散器中减少总压损失的好处变得更加明显。此外,我们提供的证据表明,高负荷涡稳定扩散器的损失产生,否则将会失速,可以降低到非失速扩散器的水平。此外,我们还详细分析了不同的损失机制及其对扩散器涡稳定性的响应。符号:扩散器横截面积AR面积比扩散器,流速,压力恢复系数,比等压热容量,降低频率h焓(默认为静态)l弦长叶片子午坐标数,每分钟转数,压力(默认为静态)欧拉半径,比气体常数,温度(默认为:静态)、转速、广义空间坐标、轴向坐标、流动角、旋涡角曲线扩散器半开口角Δ扩散器效率差、总压损失系数、周向坐标、lam常数Λ损失精流数、动粘度、动能系数、精流总压损失系数、密度、广义空间矢量Σ稳定数、Ψ流量系数、载荷系数转子进/出口平面的有效系数与进/出口扩散器进出口参考相对湍流量与总量焓致膨胀剪切致热力学涡致引言不使用排气扩散器,涡轮内可实现的热气体膨胀受环境压力限制。只有随后动能转化为静压,实现在扩压器的横截面积的增加,允许相当高的膨胀比在涡轮。因此,功率输出和假设恒定的热量输入效率增加。由此产生的废气扩散器的主要气动设计目标是将尽可能多的动能转化为静压,即最大化扩散器上的静压上升与扩散器入口的动能之比。扩压器设计者倾向于称此比率为压力恢复,并将其表示为无因次压力恢复系数= - i,i - i。(1)《国际燃气轮机、推进与动力系统学报》2019年4月第10卷第2期稿件于2018年10月2日接收审稿于2019年4月10日完成版权所有©2019日本燃气轮机学会
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Total Pressure Loss Reduction in Annular Diffusers
Power output and efficiency of gas turbines depend strongly upon the achievable pressure rise in the subsequent diffuser. In combination with the requirement to keep diffuser length to a minimum, ever steeper opening angles are sought, while avoiding diffuser stall. In terms of diffuser pressure rise, the boundaries of what is achievable can be pushed further if the tip leakage vortices from the last stage are used to re-accelerate the diffuser boundary layer, thus delaying separation onset. Such measures have been shown to decrease total pressure losses as well. In this paper, we show that the benefit of total pressure loss reduction in vortex-stabilised diffusers becomes more pronounced for steeper opening angles by means of a numerically and experimentally validated approach. In extension, we provide evidence that the loss production in highly loaded vortex-stabilised diffusers, which would stall otherwise, can be brought down to the level of non-stalling diffusers. Furthermore, we present a detailed analysis of the different loss mechanisms and their response to vortex-stabilisation of the diffuser. NOMENCLATURE Symbols � cross-sectional area of the diffuser AR area ratio of the diffuser �, � flow velocity �� pressure recovery coefficient �� specific isobaric heat capacity �r reduced frequency h enthalpy (default: static) l chord length meridional coordinate number of blades � rotational speed in revolutions per minute � pressure (default: static) Euler radius � specific gas constant � temperature (default: static) � rotational velocity � generalised spatial coordinate � axial coordinate � flow angle, whirl angle curve diffuser half-opening angle Δ difference diffuser effectiveness total pressure loss coefficient circumferential coordinate Lamé constant Λ loss rectification number dynamic viscosity � kinetic energy coefficient � rectified total pressure loss coefficient � density � generalised spatial vector Σ stabilisation number , Ψ flow coefficient, loading coefficient Subscripts I, II rotor inlet/outlet plane eff effective corr correlated in, out diffuser inlet/outlet ref reference rel relative t turbulent quantity tot total quantity enthalpy-induced dilatational shearing-induced thermodynamic � vorticity-induced INTRODUCTION Without the use of exhaust diffusers, the expansion of hot gas achievable in turbines is bounded by the ambient pressure. Only the subsequent conversion of kinetic energy into static pressure, realised by an increase in cross-sectional area in the diffuser, allows for considerably higher expansion ratios in the turbine. As a consequence, the power output and—assuming constant heat input—efficiency increase. The resulting main aerodynamic design goal of exhaust gas diffusers is to convert as much kinetic energy as possible into static pressure, i.e., maximise the ratio of the static pressure rise over the diffuser to the kinetic energy at diffuser inlet. Diffuser designers tend to call this ratio pressure recovery and express it in terms of the non-dimensional pressure recovery coefficient �� = � − �i � ,i − �i . (1) International Journal of Gas Turbine, Propulsion and Power Systems April 2019, Volume 10, Number 2 Manuscript Received on October 2, 2018 Review Completed on April 10, 2019 Copyright © 2019 Gas Turbine Society of Japan
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