共查询到18条相似文献,搜索用时 156 毫秒
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针对模糊控制器隶属函数的设计与优化缺乏自学习能力的缺点,将模糊核聚类算法与TrustRegion(信赖域)方法结合起来。首先利用模糊核聚类算法对模糊控制输入、输出样本集进行聚类,然后用Trust-Region最优化方法对聚类结果进行曲线拟合,实现了模糊控制输入、输出空间的划分、隶属函数类型的确定和参数的优化。在Matlab中的仿真结果表明:模糊控制器经过笔者提出的算法优化后控制品质有较大的改善和提高。 相似文献
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对基于XY平台的平面二级倒立摆进行运动学和动力学分析,得到系统状态方程。通过构造综合误差E和综合误差变化率EC,减少输入变量维数设计模糊控制器,使模糊控制器的控制:觇则更为简单、有效,同时对量化因子参数进行优化。 相似文献
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多组分精馏分离过程,可能存在许多种塔序结构的型式。从这些塔序结构型式中寻求、选择其中的最优者,是化学工程中一个重要的课题。本文采用模糊数学的聚类分析方法,对多组分精馏主流塔序进行优化,它的要点是建立各组分在分离性能上的模糊分布,按照各组分的这种模糊分布的亲疏关系进行分类,然后再根据相对挥发度大小顺序建立主流塔序。 相似文献
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基于模糊多准则决策理论,建立了化工设备待选材料主要评价因素的模糊决策矩阵,采用模糊折衷型评价方法进行材料优劣排序,实现了选材的优化。 相似文献
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针对化学工程学的传统研究方法之局限性,本文采用模糊优化建模及相应的模糊优化方法,有效地解决了化工中含多种形式的非确定性信息的两个实际问题. 相似文献
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为在过程早期获取HSE综合性质优良的反应路径,提出了基于模糊HSE评价的多目标反应路径综合方法。全面考虑HSE因素,形成了HSE指标结构,通过设定指标的隶属度函数,建立模糊推理系统,应用层次分析法(analytic hierarchy process,AHP)确定指标的权重因子,形成了模糊HSE评价方法。基于模糊HSE评价体系,建立以安全、环境和健康为目标函数的多目标优化模型,求解得到优良的反应路径组合。应用于萘甲胺反应路径综合实例,定量得到了反应路径及其HSE目标函数值,为过程早期的路径优选提供定量数据。 相似文献
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IMMOBILIZED PLANT CELL CULTURE IN BIOREACTOR WITH NYLON CLOTH CASSETTE AND ITS FUZZY OPTIMAL DESIGN 下载免费PDF全文
A self-made bioreactor with a nylon cloth cassette immobilized C.roseus plant cells was used tostudy the indole alkaloid production in the“production phase”.The results show this bioreactor provided agood microenvironment for plant cells and was suitable for the culture of C.roseus cells to synthesize the indolealkaloids.A fuzzy multicritical optimal method was used to optimize the constructional and operating parametersof the immobilized plant cell reactor.The fuzzy optimization provide useful information for exploiting thelarge scale alkaloid production process. 相似文献
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为在过程早期获取本质安全性较好的反应路径,将模糊安全评价集成于反应路径综合形成有效方法。根据反应路径综合阶段信息选择指标,通过设定指标的隶属度函数,建立模糊推理系统,且应用层次分析法(analytic hierarchy process,AHP)求得指标的权重因子,形成了模糊评价方法。为消除中间变量的影响,分别建立单、双输入变量的模糊推理系统。将它集成于反应路径综合,通过原料筛选规则,模糊安全评价,建立以安全为目标的优化模型,求解得到优良的反应路径组合。应用于萘甲胺反应路径综合实例,定量得到了反应路径及其目标函数值,并对两种模糊系统的综合结果进行了比较。 相似文献
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The decomposition of natural gas hydrates is a phase change process, which involves the consumption and conversion of various forms of energy, such as electrical energy, chemical energy, and thermal energy. In order to evaluate the economy capacity of natural gas hydrates exploitation, an exergy model was established to calculate the energy efficiency ratio (EER) of hydrate production method. The CO2 replacement method is taken as a case study to introduce the calculation equation and flow chart of energy efficiency ratio in any production period. The amount of CO2 injection, gas production and mole fraction of methane in produced gas are three key parameters in the process of CO2 replacement. The ratio between the amount of gas production and CO2 injection is defined as production injection ratio to eliminate the influence of deposit size. This work studied the influence of production injection ratio and the mole fraction of methane in produced gas on EER. The results show that the EER of gas hydrates production by CO2 replacement is between 0.31 and 6.4 under the set conditions, and it increases with the increase of production injection ratio. In addition, increasing the mole fraction of methane in produced gas can reduce the energy consumption for gas separation and increase EER. Therefore, there are two effective ways to increase EER of CO2 replacement through controlling the amount of gas production and the mole fraction of methane in produced gas. The EER model is established to provide guidance for the optimization of gas hydrate mining process. 相似文献
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天然气水合物分解是一个相变过程,开采时涉及各种形式能量的消耗和转化,如电能、化学能、热能等。为了科学地评价天然气水合物开采技术的经济性,建立了以有效能(?)为核心的能源效率计算方程,并以CO2置换法开采天然气水合物为例,介绍任意生产周期内能源效率的计算方法和流程框图。在CO2置换开采天然气水合物的工艺过程中,注气量、产气量和产气中甲烷含量是三个关键参数,将产气量与注气量之比定义为采注比,分析采注比及产气中甲烷含量对能源效率的影响。结果表明:在设定条件下CO2置换开采天然气水合物的整体能源效率介于0.31~6.4之间;增大采注比,有利于提高能源效率;产气中甲烷的摩尔分率越高,气体分离的能耗越低,能源效率也可显著提高。因此,调控产气量和产气中甲烷摩尔分率是提高CO2置换法能源效率的主要途径。通过所建立的能效计算方程为天然气水合物开采工艺的优化提供指导。 相似文献
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Hydrogen and light hydrocarbon components are essential resources of the refinery. The optimization of the refinery hydrogen system and recovery of the light hydrocarbon components contained in the gas streams are key strategies to reduce the operating costs for sustainable development. Many research efforts have been focused on the optimization of single impurity hydrogen network, and the flowrates of the hydrogen sources and sinks are assumed to be constant. However, their flowrates vary along with the quality of crude oil and refinery processing plans. A general superstructure of multicomponent refinery hydrogen network is proposed, which considers four components, namely H2, H2S, CH4 and , as well as the flowrate variations of hydrogen source and hydrogen sink. The mathematical model based on the superstructure is developed with objective functions, including the minimization of total annualized cost and the maximization of overall satisfaction of the hydrogen network. Moreover, the model considers the removal of hydrogen sulfide and the recovery of light hydrocarbon components (i.e.C2+, ) in the optimization. To verify the applicability of the proposed mathematical model, a simplified industrial case study with four scenarios is solved. The optimization results show that the economic benefit can be maximized by considering both the direct reuse of gas streams from high-pressure separator (HP gas stream) and from low-pressure separator (LP gas stream) and the recovery of the light hydrocarbon streams. The fuzzy optimization method can be used to guide the optimal design of the refinery hydrogen system with multi-period variable flowrates. 相似文献
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A new optimization model and a customized solution method for natural gas production network design and operation 下载免费PDF全文
This article proposes to tackle integrated design and operation of natural gas production networks under uncertainty, using a new two‐stage stochastic programming model, a novel reformulation strategy, and a customized global optimization method. The new model addresses material balances for multiple key gas components, pressure flow relationships in gas wells and pipelines, and compressor performance. This model is a large‐scale nonconvex mixed‐integer nonlinear programming problem that cannot be practically solved by existing global optimization solvers or decomposition‐based optimization methods. With the new reformulation strategy, the reformulated model has a better decomposable structure, and then a new decomposition‐based global optimization method is developed for efficient global optimization. In the case study of an industrial naturals production system, it is shown that the proposed modeling and optimization methods enable efficient solution, and the proposed optimization method is faster than a state‐of‐the‐art decomposition method by at least an order of magnitude. © 2016 American Institute of Chemical Engineers AIChE J, 63: 933–948, 2017 相似文献