Prediction of Flooding in Packed Liquid-Liquid and High-Pressure Extraction Columns Using a Gaussian Process

Reliable prediction of flooding conditions is needed for sizing and operating packed extraction columns. Due to the complex interplay of physicochemical properties, operational parameters and the packing-specific properties, it is challenging to develop accurate semi-empirical or rigorous models with a high validity range. State of the art models may therefore fail to predict flooding accurately. To overcome this problem, a data-driven model based on Gaussian processes is developed to predict flooding for packed liquid-liquid and high-pressure extraction columns. The optimized Gaussian process for the liquid-liquid extraction column results in an average absolute relative error (AARE) of 15.23 %, whereas the algorithm for the high-pressure extraction column results in an AARE of 13.68 %. Both algorithms can predict flooding curves for different packing geometries and chemical systems precisely.     

Nonlinear dynamic behaviors and control based on simulation of high-purity heat integrated air separation column

In this paper, the dynamic behaviors on the basis of simulation for high-purity heat integrated air separation column (HIASC) are studied. A nonlinear generic model control (GMC) scheme is proposed based on the nonlinear behavior analyses of a HIASC process, and an adaptive generic model control (AGMC) scheme is further presented to correct the model parameters online. Related internal model control (IMC) scheme and multi-loop PID (M-PID) scheme are also developed as the comparative base. The comparative researches are carried out among these linear and nonlinear control schemes in detail. The simulation research results show that the proposed AGMC schemes present advantages in both servo control and regulatory control for the high-purity HIASC.     

浅谈延迟焦化装置露天栈桥的设计

根据延迟焦化装置露天栈桥的工程设计实践,围绕一炉两塔(一个加热炉两个焦炭塔)的焦化装置,分析了露天栈桥设计中的要点及难点,对其在平面布置、基础安排和吊车梁选型等设计方面做一些介绍和论述。     

规整填料和新型塔板设计参数选取的质疑及分析

笔者指出了目前规整填料和新型塔板设计计算中若干尚未完全解决的、有争议或值得进一步完善的设计参数。如:规整填料的每米理论板数、最小液体喷淋密度、最小气体空塔动能因子、新型塔板开孔率等,并提出了具体的设计方案供与同行切磋。     

费萨姆工艺无水氨精馏塔的模拟计算

本文以ＮＨ３－Ｈ２Ｏ系统Ｇｉｂｂｓ自由能、熵、焓和汽液相平衡的热力学模型为基础，用松弛法进行了无水氨精馏塔的模拟计算。改变无水氨采出比、回流比（直汽量）和进料板位置均影响蒸馏效果。     

双塔脱丙烷工艺技术

对扬子乙烯装置双塔脱丙烷系统低压塔液泛、高压塔再沸器堵塞等问题进行了技术分析,提出了工艺流程修改方案,完善了双塔脱丙烷技术,对同类装置有参考价值。     

铜铅锌银多金属矿湿法分离新工艺

依据不同金属硫化物氧化分解电位的差异 ,针对某含铜、铅、锌、银复杂多金属硫化矿的难选冶特性 ,对浮选获得的混合精矿采取在线控制浸出过程氧化还原电位的方法 ,分步选择性氯化浸出各有价元素 ,并辅之以沉淀、置换、萃取等工艺 ,使有价金属以较高的回收率得到了有效的分离提取 ,在各工序最佳条件下 ,Cu、Pb、Zn、Ag各金属的浸出率均大于 99 0 % ,元素硫的回收率大于 76%