multicomponent distillation
英 [ˌmʌltɪkəmˈpəʊnənt dɪstɪˈleɪʃn]
美 [ˌmʌltikəmˈpoʊnənt dɪstɪˈleɪʃn]
网络 多元精馏
双语例句
- In this paper, the pinch point zone in a multicomponent batch distillation process is studied, furthermore, the batch distillation process with a side withdrawal is developed based o.
本文主要进行了多组元分批精馏夹紧区的研究，在此基础上开发了带有侧线出料的分批精馏过程。 - Heat Integration of Multicomponent Distillation System with Intermediate Reboiler anb Condenser
具有中间再沸器和中间冷凝器的多组份精馏系统的热集成 - A generalized dynamic mathematical model was developed, for multicomponent distillation process. Stiff problem of distillation dynamic mathematical model was studied. Furthermore, dynamic simulation for the stiff extractive distillation system which has 47 ideal plates and 8 components was studied.
建立了适用于多组元精馏过程动态模拟的通用数学模型，对精馏动态模型的刚性问题进行了研究，并对8组分、47块理论板的萃取精馏体系进行了动态模拟。 - Study on tray efficiency in multicomponent distillation process
多组分物系精馏过程级效率的研究 - A fuzzy synthesis method for multicomponent distillation sequences
多组分精馏序列的模糊合成方法 - Study on Solving Contact Stress by Hybrid Method A HYBRID ALGORITHM FOR MULTICOMPONENT DISTILLATION
接触应力的混合求解法求解多组分蒸馏过程的混合算法 - A nonequilibrium stage model of multicomponent distillation columns and simulation ──ⅰ. model description and method of solution
多元精馏塔非平衡级模型与仿真&Ⅰ.模型的建立与求解 - Thus, the method has overcome the shortcomings of Underwood formula, and provides a sound basis for short-cut design of multicomponent batch distillation column.
该方法并不要求相对挥发度为常数，并且能准确计算顶浓，克服了通常所采用的Underwood公式法的缺陷，为多元分批精馏的简捷设计奠定了基础。 - Studies on Multicomponent Distillation Design Method Using Stage Composition Lines
基于塔板组成线的多组分精馏设计方法研究 - A New Computation Method for Multicomponent Distillation Columns
多组分精馏计算的新方法 - Simulation of Batch Distillation of Multicomponent Solution Advances in Batch Extractive Distillation Process
多组分间歇精馏过程模拟间歇萃取精馏技术和进展 - A HYBRID ALGORITHM FOR MULTICOMPONENT DISTILLATION Study on the Ordinary Temperature Transportation Process of Multi-Blended Crude
求解多组分蒸馏过程的混合算法多组分混合原油常温输送技术 - The bizarre behaviour of Murphree point efficiencies and its relations with the concentration profiles in a multicomponent distillation column
多元系蒸馏中Murphree点效率奇异性及其与浓度分布极值的关系 - A Shortcut Design Method for Multicomponent Complex Distillation Flowsheets
多组分复杂精馏流程的简捷设计法 - Study on the Nonideal Multicomponent System Distillation
多组分非理想物系精馏研究 - An improved dynamic model of nonideal multicomponent distillation column is presented in this paper, in which the simultaneous effects of mass and heat transfer, tray hydraulics, tray efficiency and reboiler dynamics are taken into account.
综合了精馏塔的物料及能量平衡、塔板水力学方程、塔板效率及再沸器动态特性，给出一种改进的非理想多元物系精馏塔通用动态数学模型。 - Study on Solving Dynamic Mathematical Model of Multicomponent Distillation and its Stiff Problems
多组元精馏动态数学模型的求解及其刚性研究 - Multicomponent Batch Distillation Yield and Controlled Holdup Operation
多组分间歇精馏塔的收率及控制持液量操作过程的研究 - An improved dynamic model of multicomponent distillation column
一种改进的多元精馏塔动态模型 - This paper reviews the application and development of mathematical optimization techniques, mainly MINLP formulation and stochastic optimization, for the synthesis of multicomponent distillation system.
数学最优化技术在过程系统综合中起着重要作用。本文综述了混台整数非线性规划（MINLP）和随机优化两类最优化方法在多组分精馏过程综合中的应用及取得的新成果。 - A New Plate-to-plate Method for Calculating Distillation Processes(ⅳ) Design calculation of multicomponent distillation processes
精馏过程的新逐板计算法（Ⅳ）多元精馏过程的设计型计算 - This dissertation is focused on the theory and experiment of mass transfer in nonideal multicomponent distillation.
本文进行多组分非理想物系精馏传质过程的理论和试验研究。 - Research on the Feasibility of High-purity Separation of Multicomponent Distillation
高精度多组分精馏分离可能性探讨 - Simulation of multicomponent complex distillation flowsheets with sequential modular approach(ⅰ) models and algorithm
用序贯模块法模拟多组分完全复杂的精馏流程（Ⅰ）模型与算法策略 - Effect of feed temperature and reflux ratio on energy consumption in multicomponent distillation tower& computer design and simulation
进料温度和回流比对多元精馏塔能耗的影响&计算机设计与模拟 - Especially for complicated multicomponent distillation processes, such as three-phase distillations in this work, the equilibrium model will lead to a significant error in the distillation modelling.
尤其对于复杂的多组份精馏过程，例如本文所讨论的三相精馏过程，平衡模型对过程的描述会造成较大误差。