共查询到17条相似文献,搜索用时 250 毫秒
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为考察超声速引射器直接引射超声速二次流时的性能,采用纹影技术和压力测量手段对一等截面超-超引射器的流场结构及其引射性能进行了实验研究。研究结果表明:一、二次流交汇后在混合室前段形成了复杂的超声速流场结构。根据二次流在混合室入口流动状态的不同,可将超-超引射划分为非饱和超-超引射和饱和超-超引射两种工作状态;二次流在混合室入口处产生的激波提高了引射器的压力匹配性能;在给定的引射系数下,引射器的增压性能随二次流马赫数的增大而降低,而引射马赫数对引射器压力恢复性能的影响不大。 相似文献
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搭建了二维超-超引射器实验系统,进行了二次喉道型式引射器启动特性和负载特性实验,获得了引射器混合室内流场纹影图,结果表明:超声速引射器临界启动状态下,混合室内存在反压引起的激波系;引射器完全启动状态下,主激波系可始于混合室后段,无需被完全吞入二次喉道内;二次流对引射器启动有助推效果,可使混合室内激波系后移;一次流对二次流有压缩作用,且一次流工作压力越高,压缩作用越强;一次流、二次流之间会形成明显的混合层,当一次流、二次流静压不匹配时,一次流喷管出口内端壁处将形成较强斜激波,其在固壁与混合层之间反射、交叉,并向下游延伸,会降低一次流引射性能。 相似文献
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为研究不同结构参数与来流参数下变截面超-超引射器的启动特性,用于指导超-超引射器设计与工况调试,采用二维雷诺平均Naiver-Stokes方程,数值研究了引射器混合室不同收缩比、一次流和二次流的不同总压比、总温比下超-超引射器的启动规律,并定义了“启动系数”来判别超-超引射流场是否建立。研究结果表明:随着收缩比(范围0.7~0.9)的增加,超-超引射器启动的临界总压比、总温比均先降低后升高,收缩比0.8时,存在最佳总压比5.88,最佳总温比0.21。结构参数一定,超-超引射器随总温比升高启动难度增加。当超-超引射器处于启动状态下,室压不随总温比、总压比变化而变化,引入的启动系数较引射系数可不依赖具体工况而直接判别超-超引射器是否启动。 相似文献
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《低温与超导》2016,(2)
文章对采用两段式喷嘴的引射器及其两相流引射制冷系统在不同工况、不同几何尺寸条件下进行了实验研究。实验结果表明,在实验工况固定的条件下,采用两段式喷嘴的CO_2两相流引射制冷系统的COP随引射器第一喉部直径的增大而增大,引射比随第一喉部直径的增大而减小;系统COP和引射比随引射器中间连接直径的增大而减小。对于固定几何尺寸的引射器,系统COP随气冷器出口压力的升高而增大,引射比随气冷器出口压力的升高先减小后增大,在9MPa时引射比最小。与传统的CO_2制冷系统相比,采用两段式喷嘴的CO2两相流引射制冷系统的COP在不同工况的条件下均高于传统系统的COP,最大可提高约15%。 相似文献
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直排型DF/HF化学激光器双喷管模型启动特性 总被引:2,自引:1,他引:1
建立了一套直排型DF/HF化学激光器气流通道双喷管小型实验装置,通过选择不同副气流总压(模拟燃烧室气流)进行实验,研究了副气流总压对双喷管实验装置启动特性的影响。实验结果表明:随着副气流总压的增大,装置的启动压力降低,盲腔条件下的启动压力明显高于有副气流时的启动压力。因此,先通入燃烧室气流,再开通引射气流,对直排型连续波DF/HF化学激光器的启动是有利的。采用1维处理方法,建立了从引射气流喷管入口、副气流喷管入口到扩压器出口的理论模型,得到了与实验一致的规律。由于1维理论中采用了一些近似处理,实际启动压力比理论数据高20%~31%。 相似文献
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《低温与超导》2020,(5)
为了进一步优化系统,提升引射比,重新设计并制造了汽液分离器,将其增设于系统引射器之前,测试了不同工况下引射器及系统的性能,并将实验结果与传统系统进行了比较。实验证实,系统增设初级汽液分离器后可使引射效果得到提升,使主引射流以近乎单相流的状态进入引射器,从而使引射比增大,使制冷量和COP得到提高。当系统在只改变蒸发温度的工况下正常运行时,引射比可得到约22.4%~66.4%的提高,在蒸发温度为-2℃~3℃范围内,COP提高了约2%~26.9%;当系统在只改变气冷器出口温度的工况下正常运行时,系统COP可提高约1%~19%,在气冷器出口压力约为8.75 MPa时,系统性能达到最佳且引射比最大。 相似文献
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The present study deals with the visualization of the air flow inside a supersonic ejector. Our attention is more precisely
focused on the choked flow phenomenon which occurs along the mixing chamber of the secondary nozzle and which can be visualized
by CFD. Laser tomography visualizations are used to validate the CFD model. The evolution of flow configuration in the ejector
with the primary stagnation pressure is examined both in the case of zero secondary flow and in the case of free entrainment
of induced air. 相似文献
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Classical supersonic chemical oxygen iodine laser (SCOIL) systems operate under a low total pressure of nearly 18 Torr (2400 Pa) with cavity pressure being in the range 3 Torr (400 Pa) and Mach number of 1.7. These systems handle high flow rates and hence an efficient supersonic diffuser (SD) is a critical first step towards an open-cycle operation, which may be followed by a multi-stage ejector system. The present study discusses the various aspects in the design of a supersonic diffuser for a twin 10 kW COIL module source which employs flow rates of 100 gs−1 in each module. The results of computational studies based on 3-D, viscos compressible flow, k-ε turbulence formulation for the supersonic diffuser geometry have also been discussed. The experimental results from a single-module test of the supersonic diffuser show that a total recovered pressure of nearly 7 Torr is achieved at the diffuser exit. 相似文献
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Gaurav Singhal P.M.V. Subbarao R. Rajesh Mainuddin R.K. Tyagi A.L. Dawar 《Optics & Laser Technology》2007,39(3):577-585
Conventional supersonic chemical oxygen–iodine lasers (SCOIL) are not only low-pressure systems, with cavity pressure of 2–3 Torr and Mach number of approximately 1.5, but also are high-throughput systems with a typical laser power per unit evacuation capacity of nearly 1 J/l, thus demanding high capacity vacuum systems which mainly determine the compactness of the system. These conventional nozzle-based systems usually require a minimum of a two-stage ejector system for realization of atmospheric pressure recovery in a SCOIL. Typically for a 500 W class SCOIL, a first stage requires a motive gas flow (air) of 120 gm/s to entrain a laser gas flow of 3 g/s and is capable of achieving the pressure recovery in the range of 60–80 Torr. On the other hand, the second stage ejector requires 4.5 kg/s of motive gas (air) to achieve atmospheric pressure recovery. An advanced nozzle, also known as ejector nozzle, suitable for a 500 W-class SCOIL employing an active medium flow of nearly 12 g/s, has been developed and used instead of a conventional slit nozzle. The nozzle has been tested in both cold as well as hot run conditions of SCOIL, achieving a typical cavity pressure of nearly 10 Torr, stagnation pressure of approximately 85 Torr and a cavity Mach number of 2.5. The present study details the gas dynamic aspects of this ejector nozzle and highlights its potential as a SCOIL pressure recovery device. This nozzle in conjunction with a diffuser is capable of achieving pressure recovery equivalent to a more cumbersome first stage of the pressure recovery system used in the case of a conventional slit nozzle-based system. Thus, use of this nozzle in place of a conventional slit nozzle can achieve atmospheric discharge using a single stage ejector system, thereby making the pressure recovery system quite compact. 相似文献
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The paper presents the numerical simulation results of the surface roughness influence on gas-dynamic processes inside flow parts of a supersonic ejector. These simulations are performed using two commercial CFD solvers (Star- CCM+ and Fluent). The results are compared to each other and verified by a full-scale experiment in terms of global flow parameters (the entrainment ratio: the ratio between secondary to primary mass flow rate - ER hereafter) and local flow parameters distribution (the static pressure distribution along the mixing chamber and diffuser walls). A detailed comparative study of the employed methods and approaches in both CFD packages is carried out in order to estimate the roughness effect on the logarithmic law velocity distribution inside the boundary layer. Influence of the surface roughness is compared with the influence of the backpressure (static pressure at the ejector outlet). It has been found out that increasing either the ejector backpressure or the surface roughness height, the shock position displaces upstream. Moreover, the numerical simulation results of an ejector with rough walls in the both CFD solvers are well quantitatively agreed with each other in terms of the mean ER and well qualitatively agree in terms of the local flow parameters distribution. It is found out that in the case of exceeding the “critical roughness height” for the given boundary conditions and ejector’s geometry, the ejector switches to the “off-design” mode and its performance decreases considerably. 相似文献
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Results of a numerical study of performance characteristics of supersonic ejectors with nozzles of different types are reported. The work was carried out with the aim of developing a high-performance ejector for pressure recovery systems of supersonic chemical lasers. A specific feature of the operation of ejectors in pressure recovery systems consists in that, in this case, the ejecting and ejected gases, as they undergo mixing, have different thermodynamic properties, and the ejection coefficient depends on the ratio between the temperatures of the gases and on the ratio of their molecular masses. Since the operation of an ejector is based on the mixing process, the task consisted in intensification of this process using nozzles of special geometries. The performance of ejectors was judged considering an integral parameter, the product of induction by compression ratio. The calculations of the 3D viscous gas flow in the ejector channel were performed using ANSYS software. In verifying the numerical model, a comparison with experimental data obtained earlier on a model ejector facility and during tests of real pressure recovery systems in operation with supersonic chemical lasers was performed. 相似文献