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61.
本文提出了确定化工用搅拌器搅拌时间的一种简单试验方法,并用正交表安排寻找最佳搅拌参数的试验和整理试验数据,得到了有实用价值的结果。 相似文献
62.
Philip K Gbor 《Chemical engineering science》2004,59(10):1979-1987
The shrinking core model (SCM) is widely used to model fluid-solid reactions such as the leaching of metals from minerals. In most cases, however, the particle size distribution (PSD) of the solid material was disregarded. In this paper the erroneous shift in the control regime when neglecting PSD was quantified and the dependence of the shift on the coefficients of variation (CV) and the type of PSD was analysed. By coupling the SCM with a Gamma PSD, it was found that neglecting the PSD would shift the control regime from chemical reaction to inert/ash layer diffusion, when the CV was between 0.7 and 1.2. For a system controlled by liquid film diffusion, neglect of the PSD, would shift the control regime to chemical reaction when CV is between 0.3 and 0.7 or to inert/ash layer diffusion when CV is greater (0.9-1.5). It was therefore postulated that some researchers had unknowingly made invalid conclusions about the control regime due to the neglect of PSD. However, an inert/ash layer diffusion-controlled process was insensitive to the neglect of PSD. When CV<0.3, neglect of the PSD would not cause any erroneous shifts, irrespective of the control regime. Experimental data confirmed the observation. For a given CV, the deviation in the fraction reacted from the mono-PSD increases with CV and decreases with time. The maximum deviation, which occurs at the beginning, is about 10% with a gamma PSD of CV=0.3. The percent deviation is dependent of the type of PSDs. Gamma PSD gives the lowest deviation while Gaudin-Schuhmann results in the largest deviation (maxi. ∼19%, with CV=0.3) in the first half of dissolution process. Log-normal distribution gives a larger deviation than gamma but quickly approaches the latter with time. The deviation for Rosin-Rammler is between log-normal and Gaudin-Schuhmann. For systems with CV less than 0.3, the SCM can be fairly used without considering PSD. When CV is greater than 0.3, particularly in the early stage of a dissolution process with a PSD other than gamma, PSD should be included to avoid substantial errors. 相似文献
63.
《Journal of Process Control》2014,24(12):7-17
In the presence of rate constraints in actuator, design of cascade controller based on the primary controller conditional integration can result into closed-loop system oscillations. Stability analysis, performed by the describing function technique and confirmed by simulation, demonstrates that the solution based on the Anti-Reset Windup Cascade Control System (ARW CCS) structure is successful. Design and tuning of the ARW CCS secondary controller is a standard ARW single-input single-output problem. In the present paper tuning is proposed for the ARW CCS primary controller. For the serial process modeling simple rules are derived and confirmed by experimental results, obtained on a drum type boiler of a 210 MWe lignite coal fired unit. General design of the ARW CCS is based on the parallel process modeling and optimization of the primary controller. Optimization is performed in the frequency domain, under constraints on the maximum sensitivity, multiplicative uncertainty bound and sensitivity to measurement noise. Simulation and experimental results on a laboratory thermal plant demonstrate effectiveness of the proposed optimization. 相似文献
64.
为使产品设计时间预测既克服小样本、异方差噪声问题,又提供除预测值以外的其他有用信息,建立概率支持向量回归(PSVR)模型。首先,在异方差回归模型基础上设计概率约束条件,以使预测值以较大概率位于真实值的某邻域,结合具有参数不敏感损失函数的支持向量回归确定优化目标,提出PSVR。然后,将最大完工时间知识嵌入进PSVR的约束条件,用以确定真实值邻域的宽度,将交叉验证与遗传算法相结合以确定PSVR的相关参数。最后,以注塑模具设计的实例进行分析,结果表明基于PSVR的时间预测方法可同时提供有效的预测值和预测区间。 相似文献
65.
This paper addresses the problem of finding optimal operational policies for an acetylene reactor for day to day operation. A lumped parameter model based on four main reactions is developed and used to examine the effects of the reactor manipulated variables on key reaction parameters. An optimal and a sub-optimal operational policy which minimize the ethylene loss over time are formulated and the solution techniques are presented. The results indicate that the reactor model is in good agreement with industrial plant data. The performance of the optimal control policy is very similar to the performance of the sub-optimal control policy. However, the sub-optimal formulation, while retaining the dominant features of the optimal response, reduces the computational requirements. Finally, some issues concerning the real-time implementation of an advanced acetylene reactor control scheme are presented. These include the estimation of the optimum regeneration cycle, a recursive model update algorithm, the process optimizer and their overall coordination. A preliminary analysis of the benefits associated with the advanced control scheme suggests a considerable reduction in the yearly ethylene loss. 相似文献
66.
介绍原 2 0万t/a装置增容到 2 4万t/a时的工艺参数优化。PTA平均粒径 95~ 110 μm ,n(EG) /n(PTA) =2 .6~ 2 .7,酯化液位 63 %~ 64 % ,温度 2 92~ 2 96℃ ;乙二醇锑催化剂 ,稳定EG、DEG量 ,选择TiO2 消光剂 ,滤除凝聚粒子 ;预缩聚温度 2 87~ 2 89℃ ,压力 2 .4~ 2 .8kPa,液位 42~ 48cm ;终缩聚温度 2 90~ 2 91℃ ,压力 2 .5~ 3 .0hPa,液位 60~ 62cm ,搅拌速度 2 .7r/min。 相似文献
67.
6-PRRS并联机器人的动力学建模研究 总被引:1,自引:0,他引:1
为解决并联机器人动力学模型的计算复杂性与实时准确控制之间的矛盾,采用虚功原理建立6-PRRS并联机器人各构件随参数变化的完整动力学方程,对6-PRRS并联机器人动力学模型在各种工作情况下进行仿真分析,对机器人各部分质量和转动惯量对驱动力的影响进行研究,提出动力学模型简化策略,减小了动力学计算量,提高并联机器人动力学的计算速度,为并联机器人的控制和参数识别奠定了基础. 相似文献
68.
危险传染病应急诊疗病房通风管道的优化设计 总被引:1,自引:0,他引:1
针对危险传染病的应急诊疗,研制出移动式危险传染病应急诊疗病房,为降低危险传染病应急诊疗病房的整体质量及棚顶的压力,以通风口的质量最轻为目标函数,以各个进气支路的进气量相等为约束条件,结合沿程阻力损失系数与管路横截面边长的关系式推导出通风管道约束函数关系式,利用MATLAB优化工具箱对模型求解,优化得到通风管道的最佳尺寸.根据优化设计结果设计了通风管道,满足实际使用要求. 相似文献
69.
悬挂式重力补偿系统精密跟踪方法 总被引:3,自引:0,他引:3
介绍了一种用于研究空间机器人微重力条件下的工作特性的悬挂系统——悬挂式重力补偿系统,并给出了悬挂模块的动力学模型.通过数值求解与仿真,运用非线性规化求出了一定条件下的最优控制参数;用正交试验寻优、基于时间最优控制的试凑法证明了优化模型的解正确性.该研究为空间机器人地面试验系统模拟微重力环境下精密跟踪运动提供了最优控制方法. 相似文献
70.
稳定路径的Ad hoc网络QoS路由算法 总被引:1,自引:0,他引:1
移动Ad hoc网络中节点移动或能量耗尽会使得建立的QoS路径断裂而需重构路由,造成通信中断,对实时业务造成严重影响,提出了一种基于路径稳定性的QoS路由算法.该算法采用网络探测技术,综合考虑链路和节点稳定性,选择一条最稳定的路径进行通信,并实时监测路径状态变化,有效降低通信中断的概率.仿真表明,该算法有效改善了分组传送成功率、时延抖动等网络性能. 相似文献