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Interpretable machine learning optimization(InterOpt)for operational parameters:A case study of highly-efficient shale gas development 被引量:3
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作者 Yun-Tian Chen Dong-Xiao Zhang +1 位作者 Qun Zhao De-Xun Liu 《Petroleum Science》 SCIE EI CAS CSCD 2023年第3期1788-1805,共18页
An algorithm named InterOpt for optimizing operational parameters is proposed based on interpretable machine learning,and is demonstrated via optimization of shale gas development.InterOpt consists of three parts:a ne... An algorithm named InterOpt for optimizing operational parameters is proposed based on interpretable machine learning,and is demonstrated via optimization of shale gas development.InterOpt consists of three parts:a neural network is used to construct an emulator of the actual drilling and hydraulic fracturing process in the vector space(i.e.,virtual environment);:the Sharpley value method in inter-pretable machine learning is applied to analyzing the impact of geological and operational parameters in each well(i.e.,single well feature impact analysis):and ensemble randomized maximum likelihood(EnRML)is conducted to optimize the operational parameters to comprehensively improve the efficiency of shale gas development and reduce the average cost.In the experiment,InterOpt provides different drilling and fracturing plans for each well according to its specific geological conditions,and finally achieves an average cost reduction of 9.7%for a case study with 104 wells. 展开更多
关键词 Interpretable machine learning operational parameters optimization Shapley value Shale gas development Neural network
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Optimization of Operating Parameters for Underground Gas Storage Based on Genetic Algorithm
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作者 Yuming Luo Wei Zhang +7 位作者 Anqi Zhao Ling Gou Li Chen Yaling Yang Xiaoping Wang Shichang Liu Huiqing Qi Shilai Hu 《Energy Engineering》 2025年第8期3201-3221,共21页
This work proposes an optimization method for gas storage operation parameters under multi-factor coupled constraints to improve the peak-shaving capacity of gas storage reservoirs while ensuring operational safety.Pr... This work proposes an optimization method for gas storage operation parameters under multi-factor coupled constraints to improve the peak-shaving capacity of gas storage reservoirs while ensuring operational safety.Previous research primarily focused on integrating reservoir,wellbore,and surface facility constraints,often resulting in broad constraint ranges and slow model convergence.To solve this problem,the present study introduces additional constraints on maximum withdrawal rates by combining binomial deliverability equations with material balance equations for closed gas reservoirs,while considering extreme peak-shaving demands.This approach effectively narrows the constraint range.Subsequently,a collaborative optimization model with maximum gas production as the objective function is established,and the model employs a joint solution strategy combining genetic algorithms and numerical simulation techniques.Finally,this methodology was applied to optimize operational parameters for Gas Storage T.The results demonstrate:(1)The convergence of the model was achieved after 6 iterations,which significantly improved the convergence speed of the model;(2)The maximum working gas volume reached 11.605×10^(8) m^(3),which increased by 13.78%compared with the traditional optimization method;(3)This method greatly improves the operation safety and the ultimate peak load balancing capability.The research provides important technical support for the intelligent decision of injection and production parameters of gas storage and improving peak load balancing ability. 展开更多
关键词 Underground gas storage operational parameter optimization extreme peak-shaving constraints genetic algorithm MODEL
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Radial Basis Function Neural Networks-Based Modeling of the Membrane Separation Process: Hydrogen Recovery from Refinery Gases 被引量:7
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作者 Lei Wang Cheng Shao +1 位作者 Hai Wang Hong Wu 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2006年第3期230-234,共5页
Membrane technology has found wide applications in the petrochemical industry, mainly in the purification and recovery of the hydrogen resources. Accurate prediction of the membrane separation performance plays an imp... Membrane technology has found wide applications in the petrochemical industry, mainly in the purification and recovery of the hydrogen resources. Accurate prediction of the membrane separation performance plays an important role in carrying out advanced process control (APC). For the first time, a soft-sensor model for the membrane separation process has been established based on the radial basis function (RBF) neural networks. The main performance parameters, i.e, permeate hydrogen concentration, permeate gas flux, and residue hydrogen concentration, are estimated quantitatively by measuring the operating temperature, feed-side pressure, permeate-side pressure, residue-side pressure, feed-gas flux, and feed-hydrogen concentration excluding flow structure, membrane parameters, and other compositions. The predicted results can gain the desired effects. The effectiveness of this novel approach lays a foundation for integrating control technology and optimizing the operation of the gas membrane separation process. 展开更多
关键词 membrane separation hydrogen recovery soft sensor RBF neural networks REFINERY operation optimization
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Power optimization of gas pipelines via an improved particle swarm optimization algorithm 被引量:5
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作者 Zheng Zhiwei Wu Changchun 《Petroleum Science》 SCIE CAS CSCD 2012年第1期89-92,共4页
In past decades dynamic programming, genetic algorithms, ant colony optimization algorithms and some gradient algorithms have been applied to power optimization of gas pipelines. In this paper a power optimization mod... In past decades dynamic programming, genetic algorithms, ant colony optimization algorithms and some gradient algorithms have been applied to power optimization of gas pipelines. In this paper a power optimization model for gas pipelines is developed and an improved particle swarm optimization algorithm is applied. Based on the testing of the parameters involved in the algorithm which need to be defined artificially, the values of these parameters have been recommended which can make the algorithm reach efficiently the approximate optimum solution with required accuracy. Some examples have shown that the relative error of the particle swarm optimization over ant colony optimization and dynamic programming is less than 1% and the computation time is much less than that of ant colony optimization and dynamic programming. 展开更多
关键词 gas pipeline operation optimization particle swarm optimization algorithm
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Optimization strategy and procedure for coal bed methane separation 被引量:3
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作者 Gaobo Zhang Shuanshi Fan +3 位作者 Ben Hua Yanhong Wang Tianxu Huang Yuhang Xie 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2013年第3期533-541,共9页
Coal bed methane (CBM) has a huge potential to be purified to relieve the shortage of natural gas meanwhile to weaken the greenhouse effect. This paper proposed an optimal design strategy for CBM to obtain an integr... Coal bed methane (CBM) has a huge potential to be purified to relieve the shortage of natural gas meanwhile to weaken the greenhouse effect. This paper proposed an optimal design strategy for CBM to obtain an integrated process configuration consisting of three each single separation units, membrane, pressure swing absorption, and cryogenics. A superstructure model was established including all possible network configurations which were solved by MINLP. The design strategy optimized the separation unit configuration and operating conditions to satisfy the target of minimum total annual process cost. An example was presented for the separation of CH4/N2 mixtures in coal bed methane (CBM) treatment. The key operation parameters were also studied and they showed the influence to process configurations. 展开更多
关键词 coal bed methane gas separation DESIGN MODULES optimization
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CFD studies on the separation performance of a new combined gas–solid separator used in TMSR-SF 被引量:2
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作者 Mengdan Wu Ning Zhang +2 位作者 Jinguo Zhai Guo-Yan Zhou Shan-Tung Tu 《Nuclear Science and Techniques》 SCIE CAS CSCD 2019年第9期61-72,共12页
In order to comply with discharge standards, a gas–solid separator is used to remove solid particles from the thorium molten salt reactor-solid fuel (TMSR-SF) system. As a key component, it directly determines system... In order to comply with discharge standards, a gas–solid separator is used to remove solid particles from the thorium molten salt reactor-solid fuel (TMSR-SF) system. As a key component, it directly determines system energy efficiency. However, current gas–solid separators, based on activated carbon adsorption technology, result in high pressure drops and increased maintenance costs. In the present study, a new combined gas–solid separator was developed for the TMSR-SF. Based on a simplified computational fluid dynamics (CFD) model, the gas–solid twophase flow and the motion trajectory of solid particles were simulated for this new separator using commercial ANSYS 16.0 software. The flow and separation mechanism for this structure were also been discussed in terms of their velocity effects and pressure field distributions, and then the structure was optimized based on the influence of key structural parameters on pressure and separation efficiency. The results showed that the standard k–ε model could be achieved and accurately simulated the new combined separator. In this new combined gas–solid separator, coarse particles are separated in the first stage using rotating centrifugal motion, and then fine particles are filtered in the second stage, giving a separation efficiency of up to 96.11%. The optimum blade inclination angle and numbers were calculated to be 45° and four, respectively. It implicated that the combined separator could be of great significance in a wide variety of applications. 展开更多
关键词 COMBINED SEPARATOR gas–solid TWO-PHASE flow Structure optimization CFD TMSR-SF
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Evolutionary Computation for Realizing Distillation Separation Sequence Optimization Synthesis 被引量:2
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作者 Dong Hongguang Qin Limin Wang Kefeng Yao Pingjing 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2005年第4期52-59,共8页
Evolutionary algorithm is applied for distillation separation sequence optimization synthesis problems with combination explosion. The binary tree data structure is used to describe the distillation separation sequenc... Evolutionary algorithm is applied for distillation separation sequence optimization synthesis problems with combination explosion. The binary tree data structure is used to describe the distillation separation sequence, and it is directly applied as the coding method. Genetic operators, which ensure to prohibit illegal filial generations completely, are designed by using the method of graph theory. The crossover operator based on a single parent or two parents is designed successfully. The example shows that the average ratio of search space from evolutionary algorithm with two-parent genetic operation is lower, whereas the rate of successful minimizations from evolutionary algorithm with single parent genetic operation is higher. 展开更多
关键词 evolutionary algorithm coding method based on the binary tree crossover operator mutation operator distillation separation sequence optimization synthesis
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Desulfurization characteristics of slaked lime and regulation optimization of circulating fluidized bed flue gas desulfurization process--A combined experimental and numerical simulation study
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作者 Jing Chen Wenqi Zhong +2 位作者 Guanwen Zhou Jinming Li Shasha Ding 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2024年第9期163-175,共13页
Circulating fluidized bed flue gas desulfurization(CFB-FGD) process has been widely applied in recent years. However, high cost caused by the use of high-quality slaked lime and difficult operation due to the complex ... Circulating fluidized bed flue gas desulfurization(CFB-FGD) process has been widely applied in recent years. However, high cost caused by the use of high-quality slaked lime and difficult operation due to the complex flow field are two issues which have received great attention. Accordingly, a laboratory-scale fluidized bed reactor was constructed to investigate the effects of physical properties and external conditions on desulfurization performance of slaked lime, and the conclusions were tried out in an industrial-scale CFB-FGD tower. After that, a numerical model of the tower was established based on computational particle fluid dynamics(CPFD) and two-film theory. After comparison and validation with actual operation data, the effects of operating parameters on gas-solid distribution and desulfurization characteristics were investigated. The results of experiments and industrial trials showed that the use of slaked lime with a calcium hydroxide content of approximately 80% and particle size greater than 40 μm could significantly reduce the cost of desulfurizer. Simulation results showed that the flow field in the desulfurization tower was skewed under the influence of circulating ash. We obtained optimal operating conditions of 7.5 kg·s^(-1)for the atomized water flow, 70 kg·s^(-1)for circulating ash flow, and 0.56 kg·s^(-1)for slaked lime flow, with desulfurization efficiency reaching 98.19% and the exit flue gas meeting the ultraclean emission and safety requirements. All parameters selected in the simulation were based on engineering examples and had certain application reference significance. 展开更多
关键词 Circulating fluidized bed flue gas desulfurization(CFB-FGD) Desulfurization characteristics Computational particle fluid dynamics (CPFD)numerical simulation operational optimization gasesolid flow
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Gas Turbine Performance Optimization Using Compressor Online Water Washing Technique
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作者 Ezenwa A. Ogbonnaya 《Engineering(科研)》 2011年第5期500-507,共8页
The ability to predict the behaviour of a gas turbine engine and optimize its performance is critical in eco-nomic, thermal and condition monitoring studies. Having identified fouling as one of the major sources of co... The ability to predict the behaviour of a gas turbine engine and optimize its performance is critical in eco-nomic, thermal and condition monitoring studies. Having identified fouling as one of the major sources of compressor and therefore gas turbine deterioration, a computer-based engine model was developed to optimize the performance of gas turbines. The paper thus presents an analysis of compressor hand cleaning, on and offline compressor washing to actualize the technique using a computer program in Visual Basic programming language with data collected over a period of fifteen weeks for 2 gas turbine plants GT1 and GT2. The results of the data collected, when collated, shows that after washing, the overall operational efficiency changed from 39.2% to 46.25%. To optimize the performance of gas turbine engines, it is therefore recommended that operators should perform a combination of compressor hand cleaning, offline and online washing simultaneously. 展开更多
关键词 gas TURBINE TURBOMACHINERY Components FOULING Performance optimization operational PRACTICES COMPRESSOR Water WASHING
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First membrane unit for separating CO_2 from natural gas operational
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《Bulletin of the Chinese Academy of Sciences》 2007年第1期57-57,共1页
After a more-than-two-week trial operation, a new membrane unit based on the technology developed by researchers from the CAS Dalian Institute of
关键词 CO First membrane unit for separating CO2 from natural gas operational
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Processing capacity allocation of multiple production system for gas field multi-stage development
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作者 Bing-Yuan Hong Zhi-Wei Chen +5 位作者 Hai-Feng Chen Meng-Xi Zhou Jing Gong Yu-Peng Xu Zhen-Yu Zhu Xiao-Ping Li 《Petroleum Science》 2025年第11期4766-4780,共15页
The multi-stage development strategy is often adopted in the gas field.However,when the productivity decline occurs,many large processing stations will be severely idle and underutilized,significantly reducing operati... The multi-stage development strategy is often adopted in the gas field.However,when the productivity decline occurs,many large processing stations will be severely idle and underutilized,significantly reducing operating efficiency and revenue.This study proposes a novel operation mode of multiple gathering production systems for gas field multi-stage development,integrating the decisions about processing capacity allocation and infrastructure construction to share processing stations and improve multi-system operating efficiency.A multi-period mixed integer linear programming model for multisystem operation optimization is established to optimize the net present value(NPV),considering the production of gas wells,time-varying gas prices,and the capacity of processing stations.The decision of processing capacity,location,construction timing,and capacity expansion of processing stations,as well as transmission capacity of pipelines and processing capacity allocation schemes,can be obtained to meet long-term production demand.Furthermore,a real case study indicates that the proposed processing capacity allocation approach not only has a shorter payback period and increases NPV by 4.8%,but also increases the utilization efficiency of processing stations from 27.37% to 48.94%.This work demonstrates that the synergy between the processing capacity allocation and infrastructure construction can hedge against production fluctuations and increase potential profits. 展开更多
关键词 gas filed Infrastructure construction MILP operation optimization Processing capacity allocation
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Separation process study of liquid phase catalytic exchange reaction based on the Pt/C/PTFE catalysts 被引量:2
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作者 Peilong Li Li Guo +7 位作者 Renjin Xiong Junhong Luo Ming Wen Yong Yao Zhi Zhang Jiangfeng Song Yan Shi Tao Tang 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2019年第8期1837-1845,共9页
The liquid phase catalytic exchange(LPCE) reaction is an effective process for heavy water detritiation and production of deuterium-depleted potable water. In the current study, hydrophobic carbon-supported platinum c... The liquid phase catalytic exchange(LPCE) reaction is an effective process for heavy water detritiation and production of deuterium-depleted potable water. In the current study, hydrophobic carbon-supported platinum catalysts(Pt/C/PTFE) with high efficiency as reported previously for LPCE were prepared and comprehensive performance evaluation method is applied to evaluate the separation behaviors of LPCE systematically. Experimental results indicate that the optimum reaction temperature of 60–80℃ and the molar feed ratio G/L of 1.5–2.5 would lead to higher separation efficiencies. As to the packing method, a random packing mode with a packing ratio of hydrophobic catalysts 0.25 is recommended. In addition, thermodynamic analysis corresponds well with experimental results under lower temperature and G/L, while the suppression of kinetic factors should not be neglected when T > 80℃ and G/L > 1.5. 展开更多
关键词 Liquid phase CATALYTIC exchange(LPCE) HYDROPHOBIC carbon-supported PLATINUM CATALYSTS separation behaviors Optimal operating condition Water DETRITIATION
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Integrated asset management:a case study of technical and economic optimization of surface and well facilities 被引量:1
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作者 Arman Darvish Sarvestani Ali Moazami Goodarzi Ali Hadipour 《Petroleum Science》 SCIE CAS CSCD 2019年第5期1221-1236,共16页
Oil production could be increased by using optimization techniques in each stage of oil production system from field to production unit.However,the maximum profit will be obtained once integrated optimization of surfa... Oil production could be increased by using optimization techniques in each stage of oil production system from field to production unit.However,the maximum profit will be obtained once integrated optimization of surface and subsurface components of the oil production system is implemented.In addition,when using high-tech equipment and facilities,an integrated study of well and surface facilities affects the economic benefits significantly.In this work,one of the Iranian brown fields(mature or declining production fields)was studied to find the best renovation plan with maximum profits.The base scenario was designed with four stages of separation,and the high-pressure gases from the first and the second separator were planned to be sold,while the low-pressure gases from subsequent stages were supposed to be flared.In this paper,two additional scenarios,namely separator optimization and full optimization,were proposed and 12 cases were defined.In the full optimization scenario,low-pressure gases were prevented from being flared.It was observed that by stopping the flaring systems,gas production rate increases as high as 20%and 150 to 200 MW power will be generated in all cases during the next 20 years.Finally,economic evaluation for all of the cases was done and different cases were compared in terms of incremental annual worth and payback period. 展开更多
关键词 SEPARATOR ELECTRICITY gas lift FLARE NPV optimization
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Medium oxygen enriched blast furnace with top gas recycling strategy 被引量:4
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作者 Wei Zhang Zheng-liang Xue +3 位作者 Ju-hua Zhang Wei Wang Chang-gui Cheng Zong-shu Zou 《Journal of Iron and Steel Research International》 SCIE EI CAS CSCD 2017年第8期778-786,共9页
Top gas recycling oxygen blast furnace(TGR-OBF)process is a promising ironmaking process.The biggest challenge of the TGR-OBF in operation is the dramatic decrease of top gas volume(per ton hot metal),which once l... Top gas recycling oxygen blast furnace(TGR-OBF)process is a promising ironmaking process.The biggest challenge of the TGR-OBF in operation is the dramatic decrease of top gas volume(per ton hot metal),which once led to hanging-up and shutdowns in practice of the Toulachermet.In order to avoid this weakness,the strategy of medium oxygen blast furnace was presented.The maneuverable zone of the TGR-OBF was determined by the top gas volume,which should not be far from the data of the traditional blast furnace.The deviation of ±12.5% was used,and then the maneuverable blast oxygen content is from 0.30 to 0.47 according to the calculation.The flame temperature and the top gas volume have no much difference compared to those of the traditional blast furnace.The minimum carbon consumption of 357 kg per ton hot metal in the maneuverable zone occurs at the oxygen content of 0.30(fuel saving of 14%).In the unsteady evolution,the N2 accumulation could approach nearly zero after the recycling reached 6 times.Thus far,some TGR-OBF industrial trials have been carried out in different countries,but the method of medium oxygen enriched TGR-OBF has not been implemented,because the accumulation of N2 was worried about.The presented strategy of medium oxygen enriched TGR-OBF is applicable and the strategy with good operational performance is strongly suggested as a forerunner of the full oxygen blast furnace. 展开更多
关键词 Oxygen blast furnace Top gas recycling Top gas volume Carbon consumption operation Emission optimization
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基于响应面法的小型井下油水分离器操作参数优化
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作者 曹砚锋 邱浩 +4 位作者 文敏 王通 赵军伟 邹明华 潘豪 《石油机械》 北大核心 2025年第5期125-132,共8页
油水分离器不仅可以有效分离油水混合物,还可提高生产效率、减轻环境污染,并降低生产成本。为了进一步提升油水分离器的分离效率,降低溢流压力损失,以设计的小型井下油水分离器为研究对象,基于响应面法,建立了油相密度、处理量和分流比... 油水分离器不仅可以有效分离油水混合物,还可提高生产效率、减轻环境污染,并降低生产成本。为了进一步提升油水分离器的分离效率,降低溢流压力损失,以设计的小型井下油水分离器为研究对象,基于响应面法,建立了油相密度、处理量和分流比3种操作参数与分离效率及压降之间的数学关系,分析了油相密度、处理量和分流比对分离效率和压降的单独影响,探讨了它们之间的交互影响关系,确定了最佳的操作参数组合形式,并对响应模型进行了验证。研究结果表明:方差分析与显著性检验显示模型的线性回归决定系数R~2分别为0.9729、0.9911,表明响应模型的相关性较好;当油相密度为800 kg/m^(3)、来液处理量为1.413 m^(3)/h及分流比为39.419%时,分离效果最优;优化后分离器分离效率由初始操作参数的79.56%提升至96.37%;操作参数优化后的分离器底流附近油相体积分数明显降低,溢流附近(油相出口)的含油体积分数提升了5个百分点。所得结果和研究方法可为井下油水分离器的结构再优化及现场应用提供指导。 展开更多
关键词 油水分离器 响应面法 操作参数 结构优化 分离效率 数值模拟
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大型空分装置预防粗氩塔氮塞的优化操作
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作者 高俊刚 贾永忠 杨尚宇 《冶金动力》 2025年第1期82-85,共4页
介绍了40000m3/h空分装置整体工艺流程,阐述了空分装置氩系统发生氮塞对上、下游工序的影响,分析了氩系统发生氮塞的根本原因,制定了相应的预防措施,并优化了操作过程,保证了空分装置的产量及纯度。
关键词 空分装置 氮塞 操作过程优化
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农地制度、交易成本与农业经营规模的“适度区间”——兼论小农经济逻辑的超越
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作者 段昱兵 邓宏图 赵燕 《陕西师范大学学报(哲学社会科学版)》 北大核心 2025年第5期98-113,共16页
农户经营适度规模区间同时受农业生产函数、农地制度、影子价格、交易成本的影响,我国粮食的影子价格由市场和交易成本共同决定。在这一背景下,农户劳动力和土地的最优投入规模分别为10.98人和70.69亩。当农地制度发生变化时,劳动力和... 农户经营适度规模区间同时受农业生产函数、农地制度、影子价格、交易成本的影响,我国粮食的影子价格由市场和交易成本共同决定。在这一背景下,农户劳动力和土地的最优投入规模分别为10.98人和70.69亩。当农地制度发生变化时,劳动力和土地适度规模也会相应发生变化,分别形成8.25—11.33人和66.09—83.29亩的适度规模区间。三权分置农地制度使亩均固定交易成本增加对适度规模,产生负向影响的同时,也使可变交易成本,减少正向影响规模。这种适度规模仅基于目前的农地制度,在农业新质生产力的推动下,我国农业的最优规模将突破小农经济的局限。 展开更多
关键词 农地制度 农业经营 土地适度规模 三权分置制度 交易成本
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Operation of Off-grid Power Supply System Using IoT Monitoring Platform for Oil and Gas Pipeline Based on RESOC
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作者 Chenxing Xu Jian Wu +5 位作者 Hailin Feng Andreas Ibrom Qing Zeng Jianfeng Zhang Na Li Qiang Hu 《CSEE Journal of Power and Energy Systems》 SCIE CSCD 2020年第1期12-21,共10页
An oil and gas pipeline monitoring platform uses internet of things(IoT)to ensure safe operation in remote and unattended areas,through automatic monitoring and systematic control on equipment such as the cut-off valv... An oil and gas pipeline monitoring platform uses internet of things(IoT)to ensure safe operation in remote and unattended areas,through automatic monitoring and systematic control on equipment such as the cut-off valves and cathodic protection systems.The continuity and stability of power supplies for various equipment of an oil and gas pipeline IoT monitoring platform is crucial.There is no single universal off-grid power supply method that is optimal for an oil and gas pipeline IoT monitoring platform in all different contexts.Therefore,it is necessary to select a suitable one according to the specific geographical location and meteorological conditions.This paper proposes an off-grid power supply system comprised of a reversible solid oxide fuel cell(RESOC),photovoltaic(PV)and battery.Minimum operating costs and the reliability of system operations under constraint conditions are the key determining objectives.A“PV+battery+RESOC”system operational optimization model is established.Based on the model,three types of off-grid power supply schemes are proposed,and three geographical locations with different meteorological conditions are selected as practical application scenarios.The Matlab Cplex solver is used to solve the different power supply modes of the three regions.And finally,the power supply scheme with the best reliability and economy under different geographical environments and meteorological conditions is obtained. 展开更多
关键词 IOT oil and gas pipeline off-grid power supply system operational optimization reversible solid oxide fuel cell
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提高二甲苯精馏塔分离效率的操作优化与节能策略
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作者 邓作丁 陈兴渝 《化工管理》 2025年第17期153-155,共3页
为满足提升二甲苯精馏塔分离效率及节能需求,文章提出了一套综合性的操作优化与节能策略。通过深入探讨影响精馏塔分离效率的关键因素,如气液传质状况、进料组成稳定性、回流比、温度和压力等,并据此制定了相应的优化方案,旨在有效增强... 为满足提升二甲苯精馏塔分离效率及节能需求,文章提出了一套综合性的操作优化与节能策略。通过深入探讨影响精馏塔分离效率的关键因素,如气液传质状况、进料组成稳定性、回流比、温度和压力等,并据此制定了相应的优化方案,旨在有效增强分离效率。同时,引入低能耗换热技术,结合热回收与热集成系统,通过回收塔顶冷凝物流的热量,降低了对加热设备的依赖,进而降低系统整体能耗。经深入分析验证,所采取的这些策略不仅提高了精馏塔的分离效率,还成功实现了节能目标,为精馏塔的高效运行提供了实践支撑,对推动石化行业的节能升级改造具有重要参考价值。 展开更多
关键词 二甲苯精馏塔 分离效率 操作优化 节能策略
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旋风分离器筒体上切向接管开孔结构优化设计
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作者 倪淳 《山东化工》 2025年第17期160-162,共3页
旋风分离器筒体上的进气管必须切向设置,但承压操作的旋风分离器属于压力容器,筒体上的进气管如采用常规的完全相切结构,筒体上长圆形开孔的周向弧长就会很大,当孔的长径与短径之比大于2.0时,就不能用等面积法进行开孔补强计算,增加了... 旋风分离器筒体上的进气管必须切向设置,但承压操作的旋风分离器属于压力容器,筒体上的进气管如采用常规的完全相切结构,筒体上长圆形开孔的周向弧长就会很大,当孔的长径与短径之比大于2.0时,就不能用等面积法进行开孔补强计算,增加了设计难度。本文提出了一种优化设计方法,将进气管与筒体呈近似相切结构,可使得筒体上的长圆形开孔的弧长有所减小,至孔的长径与短径之比小于2.0,可以用等面积法进行开孔补强计算。从气体流动特性方面分析了优化后的进气管近似相切结构对气体流动的影响,分析结果表明:对气体流动略有影响,但不影响操作性能。 展开更多
关键词 旋风分离器 切向接管 承压操作 开孔补强计算 优化设计
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