列表法计算发电厂蒸汽管道双层保温经济厚度

发电厂蒸气管道采用双层保温材料可以降低保温投资成本,改善保温结构并延长其使用寿命。双层保温材料经济厚度的计算是一个复杂过程,本文根据经济厚度原理,采用列表法计算了发电厂蒸汽管道双层保温结构的经济厚度。     

火电机组热力系统抽汽等效热降矩阵算法

在对热力系统进行局部定量分析之前首先需要确定新蒸汽的等效热降和各级抽汽的等效热降.各级抽汽等效热降的传统算法比较繁琐,通过深入研究等效热降理论,应用线性代数理论导出了一种求取火电厂热力系统抽汽等效热降的矩阵算法,利用该方法能够迅速准确计算出不同热力系统各级抽汽等效热降,具有很好的通用性.     

利用火电厂锅炉排烟废热的新方法

耐酸不锈钢制造的新型低温省煤器,配有强制性机械清灰装置,能够长期工作在露点以下烟气环境中,抗腐蚀,不堵灰,可以将发电厂锅炉排烟温度从135℃~150℃降低到74℃~84℃,提高发电厂热效率2.5%~3.0%,2年之内收回节能改造投资。根据现有引风机富余全压设计新型低温省煤器阻力,可以不改造引风机。     

Effect of Cooling Water Flow Path on the Flow and Heat Transfer in a 660 MW Power Plant Condenser

The effect of the cooling water flow path on the flow and heat transfer in a double tube-pass condenser for a 660 MW power plant unit was numerically investigated based on a porous medium model. The results were used to analyze the streamline, velocity, air mass fraction and heat transfer coefficient distributions. The simulations indicate that the cooling water flow path is important in large condensers. For the original tube arrangement, the heat transfer with the lower-upper cooling water flow path is better than that with the upper-lower cooling water flow path. The reason is that the steam cannot flow into the internal of upper tube bundle and the air fractions are higher in the upper tube bundle with the upper-lower cooling water flow path. An improvement tube arrangement was developed for the upper-lower cooling water flow path which reduced the back pressure by 0.47 kPa compared to the original scheme. Thus, the results show that the tube arrangements should differ for different cooling water flow paths and the condenser heat transfer can be improved for the upper-lower cooling water flow path by modifying the tube arrangement.     

Numerical Investigation of Forced Convection Conjugate Heat Transfer from Offset Square Cylinders Placed in a Confined Channel Covered by Solid Wall

Flow over two isothermal offset square cylinders in a confined channel is simulated for different Reynolds numbers to disclose the forced convection heat transfer from the heated square cylinders to the ambient fluid. The spacing between the cylinder in the normal direction and the blockage ratio are fixed. The channel walls are covered by solid walls of thickness equal to the size of the cylinder and conjugate heat transfer is considered by including these walls. Heat transfer from the cylinders to the ambient fluid as well as that conducted within the solid wall through the conjugate interface boundary are investigated in connection with Reynolds number and are reported for both steady and periodic flows. Simulation is carried out for Reynolds number varying from 10 to 100 with air as the fluid. The onset of the vortex begins when the Reynolds number equals 48. The conjugate interface temperature declines when the Reynolds number grows. The isotherms in the solid wall show two dimensionality near the cylinder region.