旋风两相流动和燃烧数值模拟理论及流场预报

本文提出一种适用于极强旋流的代数应力湍流模型与连续介质-轨道的有反应颗粒相模型相结合的理论及数值解法,用于模拟旋风炉内两相流动及煤粉燃烧。利用全套程序中流场子程序对旋风流化床炉稀相的强旋流场进行了预报,得到了合理结果,揭示了各向异性湍流的特点。     

高温空气燃烧炉内耦合传热的数值模拟

用自行开发的三维湍流流动、燃烧、辐射传热和NO_x湍流生成的计算程序,用离散坐标方法(DOM)模拟炉内的辐射传热并与其它传热方式相耦合,与各个输运方程共同求解,对燃烧室内的温度场进行了数值模拟.通过改变高温空气的预热温度,数值分析了高温空气燃烧炉内采用燃气直接喷射技术(FDI)的温度分布特性,检验了所采用的耦合数值模拟技术的有效性.模拟计算结果表明,提高空气预热温度,炉内温度的峰值相应增大,温度梯度降低,温度分布更均匀,火焰更长.相关的实验结果与数值预报的结果对比表明了相一致的规律.     

四角切向燃烧煤粉锅炉炉膛内空气动力场的数值研究

1前言四角切向燃烧煤粉锅炉是目前应用较为广泛的一种炉型，在实际运行中有一些较为突出的优点。为深入研究煤粉在炉内的燃烧特性，炉内空气动力场的研究至关重要，本文数值模拟了四角切向燃烧煤粉锅炉炉内冷、热态情况下的流场，对其时均、湍流特性进行了分析，对气流的分布特性进行了研究．2研究对象本文的研究对象是锦州电厂二期工程的HG－670／14ty9型煤粉锅炉，燃烧器为多层四角切向布置，每角有4个一次风喷口，6个二次风喷口，1个三次风喷口。锅炉各部分尺寸及燃烧器的布置见图1、图2。热态流场的模拟对象是实际锅炉。模拟工况基本按…     

炉内两相流动和煤粉燃烧的双流体-轨道模型

本文首次用双流体一轨道（连续介质－轨道ＣＴ）模型对大尺寸四角喷燃炉内气粒两相流动及煤粉燃烧进行了模拟。该模型基于欧拉气相方程组、欧拉颗粒连续方程和动量方程以及拉氏颗粒能量和质量变化的方程,对各子模型用ｋ－ε－ｋｐ两相湍流模型,ＥＢＵ－Ａｒｒｈｅｎｉｕｓ湍流燃烧模型,煤粉颗粒的水分蒸发,热解挥发和焦炭燃烧的扩散－动力模型,ＤＯ（离散坐标）辐射模型。采用了将坐标扭转一定角度的方法减小入口射流和网格斜交造成的伪扩散。编制了ＬＥＡＧＡＰ－ＦＵＲＮＡＣＥ－３程序,分别对冷态模型炉内两相流动和大尺寸炉内三维两相流动和煤粉燃烧进行了模拟,并与颗粒轨道（ＳＴ）模型的模拟结果进行了对照。采用ＰＤＰＡ对冷态模型炉内气粒两相流场进行了测量。冷态两相流动的模拟与实验结果的对比表明ＣＴ模型的模拟结果和实验符合较好,ＳＴ模型所得颗粒浓度分布和实验山入较大。热态模拟的结果给出了两相速度,气相温度,组分浓度和壁面热流分布。模拟结果定性合理。模拟结果显示在出口处由于气流旋转,有一局部高温区存在。     

旋流对煤粉燃烧NO排放影响的数值模拟

本文用基于HCN释放的简化Solomon模型的NO生成湍流反应的统一二阶矩代数模型(AUSM)和煤粉燃烧的双流体模型,对不同旋流数下煤粉燃烧器内两相流动,煤粉燃烧和NO生成进行了数值模拟。模拟结果和文献中实验结果符合很好。模拟结果指出,随着旋流数的增加,NO的排放先减少后增加,燃尽率先增加后减小,和气体燃烧中得到的规律类似。     

堵塞和煤粉浓缩器对旋流两相流动影响的研究

旋流煤粉燃烧器加进口堵塞和煤粉浓缩器可以影响湍流,燃烧温度以及煤粉浓度的分布,从而影响NO的生成与排放。本文用三维相位多普勒颗粒测速仪(PDPA)测量和双流体模型数值模拟研究了堵塞和煤粉浓缩器对旋流煤粉燃烧器内两相流动的影响。实验结果和数值模拟结果基本符合。实验和模拟结果都表明,无论是进口堵塞还是煤粉浓缩器都会增加旋流燃烧器的进口湍流度,同时增加进口轴线附近的颗粒浓度,后者将有利于降低NO排放。     

贝塞尔高斯光束在各向异性湍流中的传输特性

采用随机相位屏仿真方法模拟了各向异性大气湍流及贝塞尔高斯涡旋光束在其中的强度分布、在轴闪烁指数和抖动效应,分析了各向异性湍流参数和波源参数对涡旋光束传输质量的影响.结果表明,在各向异性大气湍流中,贝塞尔高斯涡旋光束的强度分布随传输距离的变化情况与离轴距离有关,仅一级圆环处强度值单调递减,其余次级圆环处强度值均呈现先增后降的趋势.在近距离处,贝塞尔高斯涡旋光束的在轴闪烁指数随波形参数的增大而减小,随光束宽度的增大呈现先上升后下降再上升的趋势,该现象与贝塞尔高斯光束的光斑尺寸大小相关;其抖动效应随波形参数、拓扑荷数量、波长和束腰半径的增大而减弱.但在远距离处贝塞尔高斯涡旋光束的闪烁效应和抖动效应随波形参数的影响与近距离处相反,这与贝塞尔高斯光束的展宽突然增大的现象一致.贝塞尔高斯涡旋光束在各向异性湍流大气中的抖动效应小于在各向同性湍流大气中的情况,并且在远距离处大于拉盖尔高斯涡旋光束的抖动效应.     

一维炉高浓度煤粉燃烧试验研究

煤粉气流的着火过程是个非常复杂的过程,它除了受炉内传热和流动工况的影响外,还受到煤的热力特性、一次风气流速度及煤粉浓度等因素的影响。而煤粉燃烧过程的强化是人们共同要求达到的目的。采用一维流动特性试验的专项研究方法,可以得到不同热力     

涡旋光束在水下湍流中传输的闪烁因子的实验研究

为了研究涡旋光束和高斯光束在水下湍流中的闪烁特性,搭建了一套含有水下湍流的实验系统,利用循环泵控制水槽内湍流的强弱,使用闪烁仪测量光束的闪烁因子。利用这套实验系统,详细研究了涡旋光束和高斯光束在水下传输时的闪烁因子。研究结果表明,涡旋光束和高斯光束的闪烁因子随着传输距离的增大而增大,并且随着水下湍流强度增大,涡旋光束和高斯光束对应的闪烁因子也越大。在12.6m的传播距离内,拓扑电荷m=2的涡旋光束的闪烁因子远大于高斯光束的闪烁因子。另外,在不同强度的水下湍流中,拓扑荷数m=6的涡旋光束传播到5.4m时,其径向闪烁因子都先减小然后再增大。此外,拓扑荷数m=6的涡旋光束经过一定距离的传播后,其闪烁因子低于拓扑荷数m=4的涡旋光束的闪烁因子。本文研究结果对探索涡旋光束在海洋湍流中的应用具有重要价值。     

煤粉旋风燃烧过程流场特性研究

煤粉旋风燃烧器可用于工业加热过程,实现以煤代油,本论文根据旋流燃烧流动特点,采用能考虑非均向湍流应力的雷诺应力模型,对煤粉旋风燃烧器内气流流动过程场进行数值模拟计算,流场计算结果表明,燃烧室几何参数对其内部的流动特性有很大的影响。计算结果与流场实验测试相吻合。     

Spherical turbulent flame propagation of pulverized coal particle clouds in an O2/N2 atmosphere

The present study aims to clarify the effects of turbulence intensity and coal concentration on the spherical turbulent flame propagation of a pulverized coal particle cloud. A unique experimental apparatus was developed in which coal particles can be dispersed homogeneously in a turbulent flow field generated by two fans. Experiments on spherical turbulent flame propagation of pulverized coal particle clouds in a constant volume spherical chamber in various turbulence intensities and coal concentrations were conducted. A common bituminous coal was used in the present study. The flame propagation velocity was obtained from an analysis of flame propagation images taken using a high-speed camera. It was found that the flame propagation velocity increased with increasing flame radius. The flame propagation velocity increases as the turbulence intensity increases. Similar trends were observed in spherical flames using gaseous fuel. The coal concentration has a weak effect on the flame propagation velocity, which is unique to pulverized coal combustions in a turbulent field. These are the first reports of experimental results for the spherical turbulent flame propagation behavior of pulverized coal particle clouds. The results obtained in the present study are obviously different from those of previous pulverized coal combustion studies and any other results of gaseous fuel combustion research.     

单只水平浓缩煤粉燃烧器在1MW燃烧试验台上的试验研究

单只水平浓缩煤粉燃烧器在１ＭＷ燃烧试验台上的试验研究孙绍增，吴少华，李争起，杨明新，王新雷，陈力哲，庞丽君，邢春礼，朱彤，孙恩召，秦裕琨（哈尔滨工业大学动力工程系哈尔滨１５０００１）关键词：水平浓淡燃烧，煤粉燃烧器，稳燃，低ＮＯ_ｘ一、引言电力工业对?..     

Effect of ammonia/oxygen/nitrogen equivalence ratio on spherical turbulent flame propagation of pulverized coal/ammonia co-combustion

Because ammonia is one of the most promising candidates for energy carrier in the future, various applications of ammonia as a fuel are currently considered. One medium for utilizing ammonia is by introducing it to coal-fired boilers. To the best of our knowledge, this paper is the first to report the fundamental mechanism of the flame propagation phenomenon for pulverized coal/ammonia co-combustion. The effects of the equivalence ratio of the ammonia-oxidizer mixture on the flame propagation velocity of pulverized coal/ammonia co-combustion in turbulent fields were clarified by the experiments employing a unique fan-stirred constant volume chamber. The flame propagation velocities of pulverized coal/ammonia co-combustion, pure ammonia combustion, and pure pulverized coal combustion were compared. As expected, the flame propagation velocity of pulverized coal/ammonia was higher than that of the pure pulverized coal combustion for all conditions. However, the comparison of the flame propagation velocities of pulverized coal/ammonia co-combustion and that of the pure ammonia combustion, revealed that whether the flame propagation of the pulverized coal/ammonia was higher than that of the pure ammonia combustion was dependent on the equivalence ratio of the ammonia-oxidizer. This unique feature was explained by a mechanism including three competing effects proposed by the authors. In the ammonia lean condition, the positive effects, which are the strong radiation from the luminous flame and the increment of local equivalence ratio by the addition of volatile matter, are larger than the negative effect, which is the heat absorption by coal particles in preheat zone. In the ammonia rich condition, the effect of an increment of the local equivalence ratio by the addition of volatile matter turns into a negative effect. Consequently, the negative effects overcome the positive effect in the ammonia rich condition resulting in a lower flame propagation velocity of pulverized coal/ammonia co-combustion.     

A three mixture fraction flamelet model for multi-stream laminar pulverized coal combustion

A three mixture fraction flamelet model is proposed for multi-stream laminar pulverized coal combustion. The technique of coordinate transformation is utilized to map the flamelet solutions from a unit pyramid space into a unit cubic space to improve the stability of the simulation. The validity of the three mixture fraction flamelet model was assessed on different configurations, including a laminar counterflow pulverized coal/methane flame and a laminar piloted pulverized coal jet flame. The flamelet predictions were compared to the reference results of the detailed chemistry solutions. For the counterflow flame, it was found that the flame temperature and major species mass fractions are correctly predicted by the three mixture fraction flamelet model. However, discrepancies are observed for combustion-mode-sensitive species such as CO and H₂ in the premixed combustion region. The thermo-chemical quantities in the char surface reaction zone cannot be correctly predicted if the mixing between the char off-gas stream and other streams is neglected. For the piloted jet flame, it was shown that the stable thermo-chemical variables can be correctly predicted at the upper and middle stream locations. However, at the downstream location, discrepancies can be observed in certain regions. Overall, the validity of the three mixture fraction flamelet model for multi-stream pulverized coal combustion is confirmed and its performance in turbulent pulverized coal combustion will be tested in future work.     

Realization of oxyfuel combustion for near zero emission power generation

Oxyfuel combustion is one of the promising carbon capture and storage (CCS) technologies for coal-fired boilers. In oxyfuel combustion, combustion gas is oxygen and recirculating flue gas (FGR) and main component of combustion gas is O₂, CO₂ and H₂O rather than O₂, N₂ in air combustion. Fundamental researches showed that flame temperature and flame propagation velocity of pulverized cloud in oxyfuel combustion are lower than that in air with the same O₂ concentration due to higher heat capacity of CO₂. IHI pilot combustion test showed that stable burner combustion was obtained over 30% O₂ in secondary combustion gas and the same furnace heat transfer as that of air firing at 27% O₂ in overall combustion gas. Compared to emissions in air combustion, NOx emission per unit combustion energy decreased to 1/3 due to reducing NOx in the FGR, and SO_x emission was 30% lower. However SO_x concentration in the furnace for the oxyfuel mode was three to four times greater than for the air mode due to lower flow rate of exhaust gas. The higher SO₃ concentration results that the sulphuric acid dew point increases 15–20 °C compared to the air combustion. These results confirmed the oxyfuel pulverized coal combustion is reliable and promising technology for coal firing power plant for CCS.In 2008, based on R&D and a feasibility study of commercial plants, the Callide Oxyfuel Project was started in order to demonstrate entire oxyfuel CCS power plant system for the first time in the world. The general scope and progress of the project are introduced here. Finally, challenges for present and next generation oxyfuel combustion power plant technologies are addressed.     

Investigation of turbulence models for computation of swirling flows

Different turbulence models were studied in application to calculation of swirling flows. The differential models of turbulent viscosity considering streamline curvature and the method of detached eddy simulation were used. Weakly and strongly swirling flows were considered at the example of concentrated vortex in a tube, swirling flow in a diffuser, and vortex breakdown through an abrupt expansion. The RANS models with correction to flow swirling represented well the experimental data for the weakly swirling flows. In case of strongly swirling flows, it was more correct to use the method of detached eddy simulation.     

Pulverized coal torch combustion in a furnace with plasma-coal system

Combustion of a pulverized coal torch has been numerically simulated on the basis of the equations of multicomponent turbulent two-phase flows. The results of three-dimensional simulation of conventional and plasma activated coal combustion in a furnace are presented. Computer code Cinar ICE was verified at coal combustion in the experimental furnace with thermal power of 3 MW that was equipped with plasma-fuel system. Operation of the furnace has been studied at the conventional combustion mode and with plasma activation of coal combustion. Influence of plasma activation of combustion on thermotechnical characteristics of the torch and decrease of carbon loss and nitrogen oxides concentration at the furnace outlet has been revealed.     

The effects of swirling partially premixed flame on scaled kinetic energy transport in a gas turbine-like combustor

The multi-scale interaction between combustion and turbulence is of great importance in modifying the small-scale flame structure and kinetic energy, especially in swirling flames under practical conditions. In the present study, direct numerical simulation of swirling partially premixed flame is conducted within a model combustor under gas turbine conditions. The reactive flow is compared to the corresponding non-reactive one to investigate the influence of combustion on the scaled kinetic energy transport. Kinetic energy spectra demonstrate that the turbulent kinetic energy is reduced in the dissipative subrange while enhanced in the energetic one by the flame. The critical scale is located in the inertial subrange and close to the estimated turbulent flame thickness. Filtering analyses show that the resolved-scale kinetic energy is augmented by the increased large-scale pressure-gradient work in the reactive flow, while the subgrid-scale kinetic energy is attenuated by the enhanced small-scale viscous dissipation. The backscatter prevails in the heat release regions when the filter size is larger than the laminar flame thickness, and this effect decreases with the swirling flow developing downstream. The interaction between the kinetic energy flux and the local dilatation as well as the subgrid-scale pressure-gradient work is also investigated to achieve a comprehensive understanding about the effects of combustion on the backscatter.     

径向浓淡旋流煤粉燃烧器气流湍流特性的冷态试验研究

本文利用ＩＦＡ３００型一维热膜风速仪系统对径向浓淡旋流煤粉燃烧器单相冷态湍流流场进行了试验研究,测量了流场内不同位置瞬时速度的数值,同时测量了脉动速度均方根、湍流度、平坦因子和偏斜因子在流场内的分布,得到了新型旋流燃烧器气流湍流特性参数的分布规律,可以用于研究径向浓淡旋流煤粉燃烧器的燃烧特性。