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Further refining of acetic acid at a low concentration range wouled bring a bout a great increase in theoretical stages for distillation.

在较低乙酸浓度范围内,进一步精制乙酸,采用精馏方法所需理论级数大大增加。

In chapter 3, in view of the control problems of the distillation columns in the butadiene plant, the advanced control strategy based on soft-sensing technology is designed, and the implementing method based on OPC technology is proposed. Firstly, the control system is reconstructed.

第3 章针对某石化企业丁二烯装置的精馏工段中组分浓度的控制难题,设计了基于软测量技术的先进控制方案,提出了基于OPC 技术的先进控制实现方法。

1 M packed with Mellapak SM-250 under vacuum in batch process to obtain fractions rich in such components as pinenes, camphene, limonene as well as p-cymene, terpenol s, respectively.

松轻油先用碱液进行预处理,再用工业SM-250型孔板波纹填料塔(300mm、高10.1m),以真空间歇操作方式进行一次性精馏分离,分别得到富含蒎烯、莰烯、苧烯及对-伞花烃、萜烯醇等的馏分。

The investment is 148 million Yuan RMB with fixed capital of 128 million Yuan RMB and circulating capital of 20 million yuan RMB.

该项目主要设备有反应器、精馏塔、换热设备、自动控制系统、防暴仪表、容器、储罐等。

A scheme for compactification of ammonia water absorption refrigerators, especially for the reduction of the height of the generating rectification column is proposed, which includes using spiral sheet heat exchangers as the generator and the partial condenser of the refrigerator instead of the tube shell ones.

提出了一种氨水吸收式制冷机紧凑化的方案,特别是采用螺旋板式换热器作为发生器和分凝器以降低发生精馏器高度的新设计,给出了采用上述改进方案所研制的乙醇蒸馏装置的实验结果。

In our work, a new continuous thermodynamics method for petroleum fraction phase equilibrium calculation has been proposed, in which true boiling point distillation curves for petroleum fractions were considered to be a continuous distribution function and the distribution variable was TBP temperature, and at the same time, a spline method was used in the distribution function calculation.

在以上工作的基础上,建立了具有普遍实用性的常压塔精馏计算的数学模型,并对多个工业装置进行了实际的模拟,模拟结果与装置的实际情况符合良好,在预测塔的抽出温度,抽出产品的性质,以及各个侧线产品收率等方面都得到满意的结果。

Combined with the temperature control system of the rectifying tower, the algorithm is verified in simulation.

并结合精馏塔温度控制系统,仿真验证算法。

The author briefly introduces technological process and control principle of the rectification tower, with an emphasis on structure and programming method of the software system.

作者简述了精馏塔的工艺流程和控制原理,着重描述了软件系统的结构和编程方法。

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

对苯与低浓度丙烯合成异丙苯的催化精馏过程建立非平衡级模型。

In addition, the low-temperature heat utilization in deaeration of desahed water and temperature elevation of deaerated water is explored on the basis of refinery system integration and optimization.

其次从炼油厂系统整合优化角度探讨除盐水在除氧环节以及除氧水在升温环节低温热利用的途径,通过技术改进和系统低温热利用相结合,探讨芳烃精馏塔实现回收低温热和消除装置瓶颈的可行性,提出利用区域除盐水集中升温除氧以及区域除氧水先集中升温再进汽包产汽的芳烃脱庚烷塔低温热利用方案,不仅能回收67%的低温热,产生的1.4MPa低压蒸汽(10t/h)还可代替连续重整装置脱已烷塔重沸器的中压蒸汽。

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