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复杂体系的汽液相平衡 被引量:1
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作者 李君发 殷桃荣 《化学工程》 CAS CSCD 北大核心 1992年第6期25-30,共6页
本文综述了近年来计算复杂体系汽液相平衡的立方型状态方程、扰动硬链理论(PHCT)及基团贡献型状态方程的进展情况,并对每一方程的适用范围和偏差情况进行了讨论。
关键词 立方状态方程 扰动硬链理论 基团贡献型 状态方程 汽液相平衡
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Correlating thermal conductivity of pure hydrocarbons and aromatics via perceptron artificial neural network (PANN) method 被引量:2
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作者 Mostafa Lashkarbolooki Ali Zeinolabedini Hezave Mahdi Bayat 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2017年第5期547-554,共8页
Accurate estimation of liquid thermal conductivity is highly necessary to appropriately design equipments in different industries. Respect to this necessity, in the current investigation a feed-forward artificial neur... Accurate estimation of liquid thermal conductivity is highly necessary to appropriately design equipments in different industries. Respect to this necessity, in the current investigation a feed-forward artificial neural network(ANN) model is examined to correlate the liquid thermal conductivity of normal and aromatic hydrocarbons at the temperatures range of 257–338 K and atmospheric pressure. For this purpose, 956 experimental thermal conductivities for normal and aromatic hydrocarbons are collected from different previously published literature.During the modeling stage, to discriminate different substances, critical temperature(Tc), critical pressure(Pc)and acentric factor(ω) are utilized as the network inputs besides the temperature. During the examination, effects of different transfer functions and number of neurons in hidden layer are investigated to find the optimum network architecture. Besides, statistical error analysis considering the results obtained from available correlations and group contribution methods and proposed neural network is performed to reliably check the feasibility and accuracy of the proposed method. Respect to the obtained results, it can be concluded that the proposed neural network consisted of three layers namely, input, hidden and output layers with 22 neurons in hidden layer was the optimum ANN model. Generally, the proposed model enables to correlate the thermal conductivity of normal and aromatic hydrocarbons with absolute average relative deviation percent(AARD), mean square error(MSE), and correlation coefficient(R^2) of lower than 0.2%, 1.05 × 10^(-7) and 0.9994, respectively. 展开更多
关键词 Thermal conductivity Artificial neural network Critical properties Hydrocarbons Aromatics
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Thermodynamic Performances of[mmim]DMP/Methanol Absorption Refrigeration 被引量:3
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作者 Wei Chen Shiqiang Liang +3 位作者 Yongxian Guo Keyong Cheng Xiaohong Gui Dawei Tang 《Journal of Thermal Science》 SCIE EI CAS CSCD 2012年第6期557-563,共7页
In order to study the theoretical cycle characteristic of [mmim]DMP (1-methyl-3-methylimidazolium dimethyl- phosphate)/methanol absorption refrigeration, the modified UNIFAC group contribution model and the Wilson m... In order to study the theoretical cycle characteristic of [mmim]DMP (1-methyl-3-methylimidazolium dimethyl- phosphate)/methanol absorption refrigeration, the modified UNIFAC group contribution model and the Wilson model are established through correlating the experimental vapor pressure data of [mmim]DMP/methanol at T= 280~370 K and methanol mole fraction x= 0.529-0.965. Thermodynamic performances of absorption refrigera- tion utilizing [mmim]DMP/methanol, LiBr/H20 and H20/NH3 are investigated and compared with each other under the same operating conditions. From the results, some conclusions are obtained as follows: 1) the circula- tion ratio of the [mmim]DMP/methanol absorption refrigeration is higher than that of the LiBr/H2O absorption refrigeration, but still can be acceptable and tolerable. 2) The COP of the [mmim]DMP/methanol absorption refrigeration is smaller than that of the LiBr/H2O absorption refrigeration, while it is higher than that of the H2O/NH3 absorption refrigeration under most operating conditions. 3) The [mmim]DMP/methanol absorption refrigeration are still available with high COP when the heat source temperature is too high to drive LiBr/H2O absorption refrigeration. 展开更多
关键词 Modified UNIFAC model Wilson model Thermodynamic performances Absorption refrigeration
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