精馏塔

精细化学品间歇精馏塔的改进及应用

Improvement and Application of Intermittent Rectifying Column of Fine Chemical Products

乙烯生产中精馏塔的专家控制系统

Expert Control System for Rectifying Column System in Ethylene Production

连续精馏塔中理论塔板数NT的分析计算法

Analysis for the number of theoretical plate in a continual rectifer

专家PID在精馏塔控制中的应用

Expert PID and Its Application in Distillation Column Control System

基于模糊神经元PID解耦的精馏塔温度控制

Design of Fuzzy-neuron PID Decoupling Controller for Distillation Column Temperature

用自由度N（C+2）同时校正法解内联精馏塔系统

N ( c + 2 ) degrees of freedom simultaneous correction method for interlinked distillation columns

自适应预测PID控制在理想物系内部热耦合精馏塔上的应用

Application of Adaptive Predictive PID Control to Ideal Internal Thermally Coupled Distillation Columns

用Excel电子表格确定精馏塔灵敏板位置

Determination the Position of Sensitive Plate Using Excel in Distillation

Excel填充柄在精馏塔逐级计算中的应用

Application of Excel filling handle in distillation tower step-by-step calculation

内部热耦合精馏塔的初步设计（II）控制分析和参数优化

Principium design of ideal internal thermally coupled distillation columns ( ii ) control analysis and parameter optimization

用Excel对精馏塔灵敏板位置确定的数值分析

Numerical analysis of determining position of sensitive plates in distillation tower using Excel

利用PRO/Ⅱ和Excel求解精馏塔最优回流比

Determination of optimum reflux ratio of distillation column using PRO / ⅱ and Excel

aspenplus在工业精馏塔故障诊断与参数寻优中的应用

Application of ASPEN Plus on the Operation Analysis of Industrial Distillation Column

CFD优化精馏塔板的液流状况

Improving liquid flow on distillation tray with CFD

AutoCAD在精馏塔设计中的应用

Application of AutoCAD in Rectification Tower Design

最近的研究使用aNN来确定原油精馏塔的操作条件。

Recent research used an aNN to determine the operating conditions for a crude oil distillation column .

利用MonteCarlo方法预测精馏塔板上气泡尺寸分布及相界面积

The Prediction of the Bubble Size Distribution and the Interfacial Area on a Distillation Tray by Monte Carlo Method

PTA装置共沸精馏塔脱水系统

Dehydration system in azeotropic rectification tower of PTA plant

基于结构化类比的时间序列预测算法研究及其在PTA共沸精馏塔建模中的应用

Research on Structured-Analogy-Based Prediction Algorithm for Time Series and Its Application on PTA Solvent System

PTA装置溶剂回收工段精馏塔再沸器设计探讨

Discussion on Design of Reboiler of Distillation Tower in Solvent Recovery Section of PTA Plant

重点是以PLC替代巡检仪对精馏塔的开关量进行控制，通过PLC软件程序简化了原有的硬件逻辑电路。

PLC focus on alternative data logging devices on the distillation of the switching control through simplified procedures PLC software of the original hardware logic circuits .

基于Hopfield网络的多变量动态矩阵控制及其在精馏塔系统中的应用

The Dynamic Matrix Control Based on Hopfield Neural Network and Its Application in a Distillation Column

介绍了用Excel对精馏塔理论塔板数的计算方法，不需要编程就可方便地得到计算结果。

This paper introduces a calculating method for the rectification column 's theoretical plate number by using Excel , which is easy-to-use without programming .

介绍了用Excel图解法求精馏塔理论塔板数，并给出了VBA程序。

This paper introduce an Excel-based graphic solution to the theoretical plate numbers of a rectification column and a VBA program .

IGCC电站空分系统精馏塔的分段简化模型

Simplified model for distillation tower of air separation unit in IGCC plant by comparting method

讨论了精馏塔MESH方程组的求解方法，介绍了相平衡系数简化模型及构造的双重迭代算法。

This paper discusses the methods for solving MESH equation groups for a distillation tower . A phase equilibrium coefficient simplified model and a binary iteration algorithm are proposed .

利用成熟的化工模拟软件aspenplus和Pro／Ⅱ，对常规精馏塔序列应用于碳五分离系统，采用两种设计方案进行了模拟计算。

Two different projects to simulate the Carbon 5 separation unit using the simulator ASPEN PLUS and Pro / II with the conventional distillation process were actualized .

Broyden法用于深冷净化装置精馏塔的模拟计算

The simulated calculation of cryogenic purifier distillation by broyden method

对主要的气泡尺寸的测量方法进行了总结，并应用CCD法对精馏塔中的气泡尺寸分布进行了测量。

In this paper all kind of measurement methods are summarized , and the CCD method is applied to measure the bubble size distribution on a tray of the distillation tower .

该控制器与常规PI控制器在某精馏塔双组分控制中的对比实验结果表明自适应解耦控制的性能优越于常规PI控制。

Experimental results of adaptive decoupling control and conventional PI control to a binary distillation column show that the performences of adaptive decoupling control are better than those of conventional PI control .