蒸馏过程

蒸馏法

application process───应用进程

consultation process───咨询过程

distillation column───[化工]蒸馏柱

distillation columns───蒸馏塔

selection process───选拔过程

rehabilitation process───康复过程

crude oil distillation process───原油蒸馏过程

The reactive distillation process is an important operation in the tower with reaction.───反应精馏是伴有化学反应的精馏过程,具有设备紧凑、能量集成等优点.

This is the first step in it. In a distillation process.───这是蒸馏的第一步。

So far, chemical process dominates even though distillation process is already put into production successfully.───虽然蒸馏法已成功投产,但至今为止是化学法起主要作用.

In this paper, the development and research status of adsorptive distillation process are briefly summarized.───本文简述了吸附蒸馏的设备和流程,提出了吸附蒸馏过程实现工业化的条件.

I begin the distillation process.───开始提取过程。

Thus, the optimal operating points of this distillation process are solved off line.───据此，离线求得了该精馏过程的静态最优工作点。

The factory also undertake pyridine derivatives and various solvent distillation process.───本厂还可承接吡啶类系列化合物及各种溶剂精馏加工.

With the help of equivalent simple distillation process, the objective value, that is the fitness, of complex process was determined.

A method, which combined neural network and genetic algorithms, was employed to simulate the catalytic distillation process by black box model and optimize the operational parameters.

The paper introduces the current status of shale oil industry point out the existing problems of shale distillation process in China.

It makes the dynamic model of crude distillation process based on the process mechanism, then applies the Dynamic Matrix Control(DMC) algorithm to do the control simulation.

Simulation calculations were carried out of the extractive distillation process for separation of butadiene 1,3, using DMF(N, N dimethyl formamide) as solvent.

In this paper, the development and research status of adsorptive distillation process are briefly summarized.

In batch operation, the feed to the column is introduced batch-wise. That is, the column is charged with a 'batch' and then the distillation process is carried out.

A new catalytic distillation process for the endothermic reaction of the dehydrogenation of isopropanol is developed in this work.

The non-equilibrium stage model is used to simulate catalytic distillation process for cumene synthesis using low concentration propylene and benzene.