共查询到20条相似文献,搜索用时 500 毫秒
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《工程设计百宝箱-热机版》软件包EDInBox for TDE是为电力,热力,能源工程的设计人员开发的大型设计计算绘图一体化软件包,它包括《水和水蒸气表计算程序》,《锅炉燃烧制粉系统空气阻力计算程序》和大量绘图程序,运行于最流行的微机Windows操作系统平台和AutoCADfor Windows绘图平台。 相似文献
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浅析整体煤气化燃气-蒸汽循环(IGCC)的水蒸气热力系统:IGCC的余热锅炉(HRSG)、蒸汽轮机(ST)及其余热回收和热力系统的特点,为优化参数与配置作参考。 相似文献
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《工业锅炉》2016,(6)
锅炉冷凝式换热器能深度回收锅炉尾部烟气的水分和热量,在燃气锅炉以及加装了湿法脱硫塔的电站锅炉中得到了一定的应用。对数平均温压法适用于传统非冷凝式换热器的热力计算,但不适用于锅炉冷凝式换热器的热力计算。在目前尚不存在通用性强的锅炉冷凝式换热器热力计算方法的情况下,提出了一种适用于锅炉冷凝式换热器的热力计算方法。采用该方法可分别求出换热器的显热换热量、潜热换热量和冷凝水流量,预测换热器内工质温度、水蒸气体积分数等参数的分布,并判断水蒸气开始发生冷凝的位置。采用文献中的实验数据对该热力计算方法的正确性进行了验证,结果表明烟温和冷凝水流量的计算值和实验值的变化趋势一致,且二者最大偏差在20%以内。该热力计算方法可为锅炉冷凝式换热器的设计和优化提供参考。 相似文献
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本文介绍了热能系统分析与优化程序系统的几个桩模块一水蒸气与燃气热工参数计算模型。利用本文介绍的几种模型,可建立满足不同精度要求的水蒸气与燃气热力参数计算的通用程序。 相似文献
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用面向对象的方法实现了最新水和水蒸气热力性质工业公式IAPWS-IF97(2007.8修订版),对其各区的计算模型进行了详细地分析并设计了相应的实现算法。实现了其所有区的基本方程、导出方程、各种属性的计算公式、反推方程。实现了2区的亚稳态蒸汽区的补充方程、B23方程和B2bc方程。给出了区域区分算法、2区子区域区分算法和3区通过压力p和温度T求密度ρ的牛顿迭代算法。详细地介绍了最新IAPWS-IF97的实现方法、注意事项、相关推导过程并且补充了等容比热容cv的计算机程序验证值。提高了B23与Ts(p)边界和B2bc与ps(T)边界的一致性。通过在造纸工业中的应用,表明该实现算法具有全面、精确、快速和自动测试等优点。 相似文献
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在1台5MW3级实验汽轮机上进行了湿蒸汽两相流的实验研究,实验在3种不同进汽温度下进行,用联合探针测量了末级叶片前后沿径向和周向的流场、蒸汽湿度、水滴尺寸等参数,并分别用2种方法确定了末级前后的蒸汽参数,获得了3个级的级效率。比较发现,发生凝结的第2级的级效率低于其它2级,这表明凝结过程存在很大的热力学损失。 相似文献
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A two-phase model capable of predicting the performance of fluidized bed biomass air-steam gasification reactor during dynamic and steady state operations was developed based on the two phase theory of fluidization. Material and energy balances were taken into consideration and the minimization of free energy technique was used to calculate the gas mole fractions. The fluidized bed was divided into three zones (jetting, bubbling and slugging) and the mass and heat transfer coefficients were calculated for each zone in both bubble and emulsion phases. The model includes the hydrodynamics, transport and thermodynamic properties of fluidized bed. The finite element method was used to solve the partial differential equations. The input variables of the computer program included fluidization velocity, steam flow rate and biomass to steam ratio. The model is capable of predicting the bed temperature, gas mole fractions, higher heating value and production rate. 相似文献
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将低压缸、凝汽器以及与低压缸抽汽相对应的回热加热器视为一开口热力系,根据该开口系的能量平衡提出了一种在线计算排汽焓和低压缸效率计算方法。该方法采用改进型弗留格尔公式计算排汽量,根据高中压缸抽汽参数计算低压缸进汽量,避开了对低压缸湿蒸汽区的计算,计算精度较高。 相似文献
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Grzegorz Nowak Włodzimierz Wróblewski Iwona Nowak 《International Journal of Heat and Mass Transfer》2012,55(17-18):4511-4520
This paper discusses the problem of blade cooling system optimization connected with conjugate heat transfer (CHT) analysis for reliable thermal field prediction within a steam cooled component. Since the full CHT solution, which involves the main flow, blade material and the coolant flow domains is computationally expensive from the point of view of optimization process, it was decided to reduce the problem by fixing the boundary conditions at the blade surface and solving the task for the interior only (both solid material and coolant). Such assumption, on one hand, makes the problem computationally feasible, and on the other, provides more reliable thermal field prediction than it used to be with the empirical relationships.The analysis involves shape optimization of internal cooling passages within an airfoil. The cooling passages are modeled with a set of four Bezier splines joined together to compose a closed contour. Each passage is fed with cooling steam of constant parameters at the inlet. In the present study the airfoil profile is taken as aerodynamically optimal. The search problem is solved with evolutionary algorithm and the final configuration is to be found among the Pareto optimal cooling candidates. 相似文献
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To achieve hydrogen‐rich and low‐tar producer gas, multi‐stage air‐blown and air‐steam gasification processes were studied in this research. Results showed that the tar content from multi‐stage air‐blown and air‐steam gasification were lower, compared to the average value of that from downdraft gasification. In the cases of air supplies of 80, 100 l min?1 and 100, 100 l min?1 with steam, hydrogen yields were increased by 40.71 and 41.62%, respectively, compared to that without steam. These were about 1.6 times of hydrogen flow rate of the base case (S/B = 0). However, it was found that too much steam added to the process was disadvantageous. The equilibrium model was also applied to predict the hydrogen production and the composition of producer gas obtained from the multi‐stage air‐blown and air‐steam gasification processes. The predicted result showed a better match for the case of multi‐stage air‐blown gasification process. Copyright © 2010 John Wiley & Sons, Ltd. 相似文献