共查询到19条相似文献,搜索用时 93 毫秒
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提出了一种系统化的基于逻辑与启发性知识的MINLP过程优化综合方法 .该方法将超结构图的拓扑结构分解成特定的几种设备连接类型 ,通过组合形成基于逻辑的混合整数规划模型 ,克服了数学规划法在建模方面所存在的不直观、难于系统化地实现、复杂的超结构模型难于建立等缺点 .模型中还以硬逻辑或启发的形式引入工程经验 ,减小了搜索空间 ,加快了求解速度 .通过化工厂公用工程系统综合的实例 ,将本方法与传统的层次分解法、数学规划法进行了比较 ,证明了其实用性和优越性 相似文献
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提出了过程全局夹点分析与超结构混合整数非线性规划 (MINLP)相结合的能量集成最优综合法 .各单过程内部换热优化匹配后 ,进行各过程剩余冷、热负荷与公用工程系统的全局夹点分析 ,确定全局热集成目标 ,在此基础上建立包含过程剩余热负荷产生各等级蒸汽、剩余冷负荷使用各等级蒸汽加热的各种可能匹配方案的公用工程换热网络超结构及其MINLP模型 ,采用混合连续进化算法求解得到过程与公用工程换热网络最优改造方案 .大型乙烯装置能量集成应用算例表明 ,可充分发挥全局夹点分析法确定改造目标的简洁实用性和超结构MINLP寻求最佳方案的优点 相似文献
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Steady-state non-dominated sorting genetic algorithm (SNSGA), a new form of multi-objective genetic algorithm, is implemented by combining the steady-state idea in steady-state genetic algorithms (SSGA) and the fitness assignment strategy of non-dominated sorting genetic algorithm (NSGA). The fitness assignment strategy is improved and a new self-adjustment scheme of crame is proposed. This algorithm is proved to be very efficient both computationally and in terms of the quality of the Pareto fronts produced with five test problems including GA difficult problem and GA deceptive one. Finally, SNSGA is introduced to solve multi-objective mixed integer linear programming (MILP) and mixed integer non-linear programming (MINLP) problems in process synthesis. 相似文献
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化工过程流体机械教学中学生综合能力的培养 总被引:3,自引:0,他引:3
根据化工过程生产对化工过程装备与控制专业应用型人才多方面能力的要求,我们利用案例教授数学模型、优化理论、现代设计理论及方法的相关内容,培养学生分析和解决实际问题的能力,提高学生的综合素质。 相似文献
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针对带有等式约束的混合整数非线性规划(MINLP)问题,建立了一种改进的粒子群优化(PSO)算法--简约空间法.利用等式约束将问题的维数降低,使带有等式约束的优化问题转化为无等式约束优化问题.通过测试函数和过程综合的实例对该算法进行了测试并与其他算法所得的结果进行了比较,结果表明,PSO算法在使用的普遍性、求解的准确性等方面都优于一般的算法,尤其对于非凸的MINLP问题,PSO算法是一种有效的求解方法. 相似文献
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基于随机型最优化策略,针对包含简单塔、带有侧线蒸出及侧线汽提塔的复杂塔、全热耦合(或Petlyuk)塔的热耦合复杂精馏塔系统的综合问题,提出一种模型化方法.针对热耦合复杂精馏流程系统所需塔段数目以及冷凝器和再沸器数目的不确定性,提出了一种分解求解策略,将原问题分解成一系列具有不同塔段数的子问题分别求解;针对流程结构的优化提出一种流程结构的编码表达法,该方法将问题的分离序列结构和热耦合方式分别用两组编码表示,对分离序列的编码采用了数据结构理论中的二叉树排序方法,使流程结构的描述变得更加简便;最后以预分馏塔组分回收率及回流比为连续变量,建立了热耦合复杂精馏系统优化的[JP+1]混合整数非线性规划(MINLP)模型,该模型用改进的模拟退火算法求解,可同时得到优化的流程结构和操作参数. 相似文献
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化工分析工作对于生产企业、科研单位有着重要的价值,特别在工业现代化的建设过程中,更应该建立全面化工分析工作体系。本研究立足于化工分析的实际,对化工分析工作的价值展开了论述,阐述了化工分析的概念,说明了化工分析工作的主要作用,描述了当前化工分析工作存在的素质、质量、操作、仪器等方面的问题,提供了新时期以素质提升、终点误差控制、分析过程加强、节能环保等方法,提升化工分析工作精度和质量的措施。 相似文献
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遗传算法在过程综合混合整数非线性规划中的应用 总被引:7,自引:0,他引:7
针对过程综合混合整数非线性规划问题提出了一种混合遗传算法,该算法对整数变量进行编码,而对连续变量则采用连续化遗传算子进行处理,使得算法与原问题的对应更加自然,也更有效。另外,还针对常见的提前收敛或局部最小现象提出几种算子,实例表明本算法具有较强的全局优化能力。相对于传统遗传算法具有速度快、精度高、可操作性强等特点。 相似文献
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本文建立了一个多目的间歇过程短期排程柔性的模型,并开发了一个实用的计算程序求解此MINLP模型。通过例证研究说明,应用此模型进行短期排程可实现快速有效的间歇化工厂生产管理。 相似文献
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改进的自适应模拟退火算法及其在过程综合中的应用 总被引:5,自引:0,他引:5
为有效解决化工过程综合中的MINLP问题,针对连续变量的模拟退火算法搜索慢的缺点,提出了一种改进的自适应模拟退火算法(Adaptive Simulated Algorithms,ASA),采取自适应调整温度和搜索步长两种策略,大大加快搜索速度,提高最优解的质量。实算结果充分体现了所提出算法的优点,并很好地应用于化工过程综合问题。 相似文献
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Process synthesis using block superstructure with automated flowsheet generation and optimization
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Jianping Li Salih Emre Demirel M. M. Faruque Hasan 《American Institute of Chemical Engineers》2018,64(8):3082-3100
An alternative method for chemical process synthesis using a block‐based superstructure representation is proposed. The block‐based superstructure is a collection of blocks arranged in a two‐dimensional grid. The assignment of different equipment on blocks and the determination of their connectivity are performed using a mixed‐integer nonlinear formulation for automated flowsheet generation and optimization‐based process synthesis. Based on the special structure of the block representation, an efficient strategy is proposed to generate and successively refine feasible and optimized process flowsheets. Our approach is demonstrated using two process synthesis case studies adapted from the literature and one new process synthesis problem for methanol production from biogas © 2018 American Institute of Chemical Engineers AIChE J, 64: 3082–3100, 2018 相似文献
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混合分离过程的有序设计框架 总被引:2,自引:1,他引:1
The design of optimal separation flow sheets for multi-component mixtures is still not a solved problem This is especially the case when non-ideal or azeotropic mixtures or hybrid separation processes are considered. We review recent developments in this field and present a systematic framework for the design of separation flow sheets. This framework proposes a three-step approach. In the first step different flow sheets are generated. In the second step these alternative flow sheet structures are evaluated with shortcut methods. In the third step a rigorous mixed-integer nonlinear programming (MINLP) optimization of the entire flow sheet is executed to determine the best alternative. Since a number of alternative flow sheets have already been eliminated, only a few optimization runs are necessary in this final step. The whole framework thus allows the systematic generation and evaluation of separation processes and is illustrated with the case study of the separation of ethanol and water. 相似文献
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针对现有的换热器网络最优综合方法的局限性,采用分级超结构转运模型和物流吸、放热潜力的概念,提出了非等温混合线性约束的换热器网络同步最优综合混合整数非线性规划(MINLP)的改进模型.该模型不仅可以对公用工程费用、换热面积、换热设备台数及物流的匹配选择进行多目标同步优化,而且在线性约束的条件下消除了等温混合的不合理假设,只需求解一次MINLP问题就可得到包括分流情况在内的最优网络结构.算例表明,该模型优于以往的几种同步优化模型. 相似文献
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A modular approach to the formulation and a solution of mixed‐integer non‐linear programming (MINLP) problems are presented, which reduce the size of MINLP and the computational expenses effectively. The method decomposes the synthesis task into three hierarchical levels—the superstructure, the structure, and the modules, with the layer of modules being the most critical to the problem solution. The strategy has been implemented in a simulation environment in which the variables of interest are defined as implicit functions of the optimization variables. The implicit relationships are handled using a data‐oriented process simulation technique (DOPS) that significantly simplify the simulation. The method has been effectively applied to two case studies, one from literature for the synthesis of hydrodesalkylation, and another from industrial process manufacturing methylene diphenylene diisocyanates. 相似文献
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M. M. Faruque Hasan Gopalakrishnan Jayaraman I. A. Karimi H. E. Alfadala 《American Institute of Chemical Engineers》2010,56(4):930-945
Most literature on the synthesis of heat exchanger networks via mathematical programming methods has dealt with phase changes by assuming nearly isothermal conditions. Many multicomponent phase changes of practical interest (e.g., those in sub‐ambient processes) occur over ranges of temperatures and exhibit nonlinear temperature‐enthalpy relations (T‐H curve). In such cases, isothermal approximations may lead to inferior or unacceptable networks. In this article, we propose a mixed‐integer nonlinear programming formulation and a solution algorithm to incorporate nonisothermal phase changes in heat exchanger network synthesis. We approximate the nonlinear T‐H curves via empirical cubic correlations, and propose a procedure to ensure minimum temperature approach at all points in the exchangers. Our approach successfully solves two industry examples and shows promise for significant cost reductions when compared with existing processes. © 2009 American Institute of Chemical Engineers AIChE J, 2009 相似文献