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distillation method相关的网络例句

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与 distillation method 相关的网络例句 [注:此内容来源于网络,仅供参考]

Molecular laser follows in ArF (193 Nm) and laser of solid of Nd ∶ YAG (213 Nm) differs two kinds the laser of wavelengh denudes in the system, factor of elemental fractional distillation all compares groovy mode to fall to be close to more at 1, make clear use medium to hold back discharge to be opposite gas collosol beforehand effect of fractional distillation of the element after ionization is able to restrain effectively.

在ArF准分子激光(193 nm)和Nd∶YAG固体激光(213 nm)两种不同波长的激光剥蚀系统中,元素分馏因子均比常规模式下更接近于1,表明采用介质阻挡放电对气溶胶预电离后元素分馏效应得以有效抑制。

In this paper, on the base of powerful calculation and diagramming ability of MATLAB, the typical examples in distillation are analyzed and the corresponding ideas and methods of computer-aided calculation in distillation are given.

本文利用MATLAB语言强大的运算与图形表达功能,通过剖析精馏计算过程中的典型例题,给出了计算机辅助计算精馏过程的具体思路和方法。

This paper aimed at the Daqing region based sauce, sweet paraffin base crude oil, the main tasks and objectives will be: 4 million tons / year, 330 days a year, total starts, top of the tower to take heat, the first mid-back to take heat, second heat to take the middle back the distribution of 5:2:3, based on the given crude true boiling point distillation data and products Engler distillation data to calculate the product of various complex decision to cut the program data to calculate the product yield, full-tower heat balance calculation, rendering the whole tower of steam , liquid load distribution.

本文设汁主要针对大庆地区低硫石蜡基原油,主要任务及目标为:400万吨/年,按每年开工330天计,塔顶取热、第一中段回流取热、第二中段回流取热分配为 5:2:3,依据所给的原油实沸点蒸馏数据及产品的恩氏蒸馏数据,计算产品的各物性数据决定切割方案,计算产品收率,进行全塔热平衡计算,绘制全塔汽、液相负荷分布图。

Based on the fundamental of distillation, MESH model including equations of mass balance, phase equilibrium, mole fraction summations and heat balance for atmosphere-vacuum distillation column was established. The key parameter such as temperature and pressure of product was obtained through solution of the model on Pro/Ⅱ platform. The comparison of simulation results with requirement of spot technology was analyzed.

基于蒸馏原理,对常减压蒸馏塔建立包含质量平衡、相平衡、摩尔分数归一化和能量平衡等方程构成的MESH模型,在Pro/Ⅱ平台上进行流程模拟,获得各塔侧线产品的温度和压力等关键参数,并与现场工艺要求进行对比。

Based on the fundamental of distillation,MESH model including equations of mass balance,phase equilibrium,mole fraction summations and heat balance for atmosphere-vacuum distillation column was established.

稳态流程与时间无关,是化工流程模拟中应用最为普遍的重要技术之一,需要建立质量平衡、相平衡、摩尔分数归一化和能量平衡等(MESH—Massbalances,Equilibrium relations,mole fractionSummations and Heat balances)方程构成的数学模型来描述其工艺流程中状态参数的分布情况[6,8-9]。

Vacuum transfer line is one of the most important pipelines of atmospheric vacuum distillation plant which starts from the exit of heaters and extends to entrance of distillation tower.

减压转油线是炼油厂常减压蒸馏装置中加热炉出口到蒸馏塔底入口的管道,它是炼油装置中最重要的管道之一。

Results show that the three-effect concurrent distillation can save energy consumption by 57.8%, 57.5% and 58.0% respectively, compared with mono-column distillation when treating 70%, 80% and 85% mass concentration methanol.

研究结果表明,该工艺与单塔工艺相比,处理浓度分别为70%、80%和85%的甲醇物料时,节能分别为57.8%、57.5%和58.0%。

The results show that the three-effect concurrent distillation is the best separation technology in response to the objective function of the ratio of multi-effect distillation expenditures to mono-column expenditures.

并以多效精馏与单塔精馏总费用的相对值最低为目标函数,确定分离甲醇-水体系的最佳方案为三效顺流精馏工艺。

The paper summarized the principle of Molecule distillation technology and the difference from the general vacuum distillation.

阐述了分子蒸馏的基本原理及其区别于普通真空蒸馏的主要特点。

The corrosion phenomenon and mechanism of atmospheric distillation unit processing thick oil have been analyzed to provide a feasible theory basis for guaranteeing stable,safe and long period running of atmosphere distillation equipments.

对加工稠油的常压装置各部位的腐蚀现象和腐蚀机理作了分析,为保证常压设备平稳安全长周期运行提供切实可行的理论依据。

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