针对当前在制品库存控制研究较少考虑系统瓶颈的现状,从最优化生产技术(Optimized Production Technology,OPT)的思想出发,在辨别出系统瓶颈的基础上,设计以瓶颈为中心驱动的推、拉结合(Push&Pull)的生产控制方式,以有效减少整个系...针对当前在制品库存控制研究较少考虑系统瓶颈的现状,从最优化生产技术(Optimized Production Technology,OPT)的思想出发,在辨别出系统瓶颈的基础上,设计以瓶颈为中心驱动的推、拉结合(Push&Pull)的生产控制方式,以有效减少整个系统的在制品库存;建立面向瓶颈的在制品库存前-反馈集成控制(B-WFFIC)模型,稳定并减少瓶颈工序前的在制品库存;最后通过实例应用和仿真验证取得了较优的结果。展开更多
Cytosine-substituted mildiomycin analogue (MIL-C) was produced effectively by supplementing cytosine into the culture of Streptoverticillium rimofaciens. In order to improve the yield of MIL-C, statistically-based e...Cytosine-substituted mildiomycin analogue (MIL-C) was produced effectively by supplementing cytosine into the culture of Streptoverticillium rimofaciens. In order to improve the yield of MIL-C, statistically-based experimental designs were applied to optimize the fermentation medium for S. rimofaciens ZJU 5119. Fifteen culture conditions were examined for their significances on MIL-C production using Plackett-Burman design. The Plackett-Burrnan design and one-variable-at-a-time design indicated that glucose and rice meal as the complex carbon sources, and peanut cake meal and NH4NO3 as the complex nitrogen sources were beneficial for MIL-C production in S. rimofaciens ZJU 5119. The results of further central composition design (CCD) showed that the optimal concentration of glucose, rice meal and peanut cake meal were 18.7 g/L, 64.8 g/L and 65.1 g/L, respectively. By using this optimal fermentation medium, the MIL-C concentration was increased up to 1336.5 mg/L, an approximate 3.8-fold improvement over the previous concentration (350.0 mg/L) with un-optimized medium. This work will be very helpful to the large-scale production of MIL-C in the future.展开更多
A model of grade transition is presented for a commercialized fluidized bed gas-phase polyethylene production process. The quantity of off-specification product and the time of grade transition can be minimized by the...A model of grade transition is presented for a commercialized fluidized bed gas-phase polyethylene production process. The quantity of off-specification product and the time of grade transition can be minimized by the optimization of operating variables, such as polymerization temperature, the ratio of hydrogen to ethylene, the ratio of co-monomer to ethylene, feed rate of catalyst, and bed level. A new performance index, the ratio of melt flow (MFR), is included in the objective function, for restraining the sharp adjustment of operation variables and narrowing the distribution of molecular weight of the resin. It is recommended that catalyst feed rate and bed level are decreased in order to reduce the grade transition time and the quantity of off-specification product. This optimization problem is solved by an algorithm of sequential quadratic programming (SQP) in MATLAB. There is considerable difference between the forward transition and reverse transition of grade with regard to the operating variables due to the non-linearity of the system. The grade transition model is extended to a high space time yield (STY) process with the so-called condensed model operation. In the end, an optimization strategy for multi-product transition is proposed with two-level optimization of the objective function J(x,u) on the basis of the optimal grade transition model. A sequential transition of six commercial polyethylene grades is illustrated for an optimal multi-product operation.展开更多
最优化生产技术(Optimized Production Technology,OPT)是一种全新的生产管理方法,其根据是一个简单的概念:生产最大化未必是利润最大化的最佳途径。OPT于七十年代出现在以色列,随后很快被移植到美国。目前,美国有20多家大公司采用了以...最优化生产技术(Optimized Production Technology,OPT)是一种全新的生产管理方法,其根据是一个简单的概念:生产最大化未必是利润最大化的最佳途径。OPT于七十年代出现在以色列,随后很快被移植到美国。目前,美国有20多家大公司采用了以OPT为基础的生产管理制度。OPT的内容主要有以下三点: 1.最大限度地挖掘“瓶颈”的潜力。所谓“展开更多
Manufacturing plants are increasingly complex and integrated, requiring control systems able to identify the interactions between the various operating units. Production planning and control design of a process are to...Manufacturing plants are increasingly complex and integrated, requiring control systems able to identify the interactions between the various operating units. Production planning and control design of a process are tools that, if combined, bring many economic benefits to the processes since they aim to identify and maintain optimal decision operations to a system. This work uses such integration between production planning and plantwide control to propose a control system for the Williams-Otto plant from the definition of the operating optimal point for coordinated decentralized optimization, in which the original optimization problem decomposition into smaller coordinated problems ensure that the found local optimum also meets the requirements of the global system. The results for decentralized optimization are satisfactory and very similar to the global optimum problem and to the control system response proposed based on the optimal obtained. It is effective taking smooth actions, working with (economic) optimal set points (economically) of operation. The unification of production planning techniques and plantwide control techniques is an effective tool for the control system design for entire plants.展开更多
The multi-stage supply chain optimization problem is an important subject for research. Syaxif et al. have studied the problem formulated by a 0-1 mixed integer linear programming model, and presented a st-GA (spanni...The multi-stage supply chain optimization problem is an important subject for research. Syaxif et al. have studied the problem formulated by a 0-1 mixed integer linear programming model, and presented a st-GA (spanning tree-based genetic algorithm) by using Priifer number representation as the solution method of the model. On the basis of the work done by Syarif et al., a rst-GA (revised st-GA ) to solve the multi-stage supply chain optimization problem, is presented in this paper by means of introducing new sym- metric encoding & decoding procedures of Priifer number, and adopting new chromosome's decoding strategy, etc. To facilitate building related decision-making support system, a C language implementation method of the rst-GA is also presented in this paper. Numerical experiments have validated that the rst-GA has better performance than the st-GA.展开更多
文摘针对当前在制品库存控制研究较少考虑系统瓶颈的现状,从最优化生产技术(Optimized Production Technology,OPT)的思想出发,在辨别出系统瓶颈的基础上,设计以瓶颈为中心驱动的推、拉结合(Push&Pull)的生产控制方式,以有效减少整个系统的在制品库存;建立面向瓶颈的在制品库存前-反馈集成控制(B-WFFIC)模型,稳定并减少瓶颈工序前的在制品库存;最后通过实例应用和仿真验证取得了较优的结果。
基金Project supported by the Ministry of Science and Technology, China (No. 2004BA308A22-14)the Department of Science and Tech- nology of Zhejiang Province, China (No. 011102543)
文摘Cytosine-substituted mildiomycin analogue (MIL-C) was produced effectively by supplementing cytosine into the culture of Streptoverticillium rimofaciens. In order to improve the yield of MIL-C, statistically-based experimental designs were applied to optimize the fermentation medium for S. rimofaciens ZJU 5119. Fifteen culture conditions were examined for their significances on MIL-C production using Plackett-Burman design. The Plackett-Burrnan design and one-variable-at-a-time design indicated that glucose and rice meal as the complex carbon sources, and peanut cake meal and NH4NO3 as the complex nitrogen sources were beneficial for MIL-C production in S. rimofaciens ZJU 5119. The results of further central composition design (CCD) showed that the optimal concentration of glucose, rice meal and peanut cake meal were 18.7 g/L, 64.8 g/L and 65.1 g/L, respectively. By using this optimal fermentation medium, the MIL-C concentration was increased up to 1336.5 mg/L, an approximate 3.8-fold improvement over the previous concentration (350.0 mg/L) with un-optimized medium. This work will be very helpful to the large-scale production of MIL-C in the future.
文摘A model of grade transition is presented for a commercialized fluidized bed gas-phase polyethylene production process. The quantity of off-specification product and the time of grade transition can be minimized by the optimization of operating variables, such as polymerization temperature, the ratio of hydrogen to ethylene, the ratio of co-monomer to ethylene, feed rate of catalyst, and bed level. A new performance index, the ratio of melt flow (MFR), is included in the objective function, for restraining the sharp adjustment of operation variables and narrowing the distribution of molecular weight of the resin. It is recommended that catalyst feed rate and bed level are decreased in order to reduce the grade transition time and the quantity of off-specification product. This optimization problem is solved by an algorithm of sequential quadratic programming (SQP) in MATLAB. There is considerable difference between the forward transition and reverse transition of grade with regard to the operating variables due to the non-linearity of the system. The grade transition model is extended to a high space time yield (STY) process with the so-called condensed model operation. In the end, an optimization strategy for multi-product transition is proposed with two-level optimization of the objective function J(x,u) on the basis of the optimal grade transition model. A sequential transition of six commercial polyethylene grades is illustrated for an optimal multi-product operation.
文摘最优化生产技术(Optimized Production Technology,OPT)是一种全新的生产管理方法,其根据是一个简单的概念:生产最大化未必是利润最大化的最佳途径。OPT于七十年代出现在以色列,随后很快被移植到美国。目前,美国有20多家大公司采用了以OPT为基础的生产管理制度。OPT的内容主要有以下三点: 1.最大限度地挖掘“瓶颈”的潜力。所谓“
文摘Manufacturing plants are increasingly complex and integrated, requiring control systems able to identify the interactions between the various operating units. Production planning and control design of a process are tools that, if combined, bring many economic benefits to the processes since they aim to identify and maintain optimal decision operations to a system. This work uses such integration between production planning and plantwide control to propose a control system for the Williams-Otto plant from the definition of the operating optimal point for coordinated decentralized optimization, in which the original optimization problem decomposition into smaller coordinated problems ensure that the found local optimum also meets the requirements of the global system. The results for decentralized optimization are satisfactory and very similar to the global optimum problem and to the control system response proposed based on the optimal obtained. It is effective taking smooth actions, working with (economic) optimal set points (economically) of operation. The unification of production planning techniques and plantwide control techniques is an effective tool for the control system design for entire plants.
基金This work is supported by National Natural Science Foundation of China(70361002), the Jiangxi Provincial Advanced Education Reform Project (GanJiaoGaoZi[2004] 100Hao), the Project of Jiangxi Provincial Department of Education (GanJiaoJiZi[2007]10Hao), and the Science Foundation of Nanchang University (04Z02914).
文摘The multi-stage supply chain optimization problem is an important subject for research. Syaxif et al. have studied the problem formulated by a 0-1 mixed integer linear programming model, and presented a st-GA (spanning tree-based genetic algorithm) by using Priifer number representation as the solution method of the model. On the basis of the work done by Syarif et al., a rst-GA (revised st-GA ) to solve the multi-stage supply chain optimization problem, is presented in this paper by means of introducing new sym- metric encoding & decoding procedures of Priifer number, and adopting new chromosome's decoding strategy, etc. To facilitate building related decision-making support system, a C language implementation method of the rst-GA is also presented in this paper. Numerical experiments have validated that the rst-GA has better performance than the st-GA.