LNG船用BOG再液化装置工艺流程模拟

文中运用工程模拟计算软件ASPEN PLUS对LNG船用蒸发气体(BOG)再液化装置工艺流程进行了较全面和深入的模拟计算.通过对模拟计算结果进行分析,得到用丙烯预冷的再液化工艺流程中的主要工艺设备运行参数:海水冷凝器冷凝温度、BOG压缩机出口压力、丙烯压缩机出口压力以及混合制冷剂压缩机出口压力对再液化效率和能耗有着不同...     

燃煤过程中碱金属迁移规律的模拟研究与预测分析

基于ASPEN PLUS 平台,对燃煤过程中碱金属迁移规律进行了模拟研究和预测。模拟结果表明,在850K~1650K气态碱金属物质随反应温度的升高而增加;1400K以下,气相中以NaCl、KCl为主,Na2SO4蒸气量明显高于K2SO4;1500K以下,气态碱金属释放量随着煤中氯质量分数的增加而增加;一定温度下,气态碱金属质量分数随压力的升高而降低;常压下煤中氯的质量分数0.1%,温度降到972K时气态碱金属的质量分数可降到2.4×10－8;而当氯的质量分数分别为0.05%和0.01%时,为达到同样的气态碱金属质量分数,温度需分别降到990K和1025K。模拟结果为燃煤联合循环发电系统的设计和优化提供了参考依据。     

MAX+PLUSⅡ在EDA中的应用

介绍了MAX+PLUSⅡ软件在EDA中的应用,以正交解码/计数器的设计为例,说明了对Altera公司的FPGA进行图形设计、编译以及在系统编程(ISP)的方法和步骤。     

A process economic approach to develop a dilute-acid cellulose hydrolysis process to produce ethanol from biomass

Successful deployment of a bioethanol process depends on the integration of technologies that can be economically commercialized. Pretreatment and fermentation operations of the traditional enzymatic bioethanol-production process constitute the largest portion of the capital and operating costs. Cost reduction in these areas, through improved reactions and reduced capital, will improve the economic feasibility of a large-scale plant. A technoeconomic model was developed using the ASPEN Plus^TN modeling software package. This model in cluded a two-stage pretreatment operation with a co-current first stage and countercurrent second stage, a lignin adsorption unit, and a cofermentation unit. Data from kinetic modeling of the pretreatment reactions, verified by bench-scale experiments, were used to create the ASPEN Plus base model. Results from the initial pretreatment and fermentation yields of the two-stage system correlated well to the performance targets established by the model. The ASPEN Plus model determined mass and energy-balance information, which was supplied, to an economic module to determine the required selling price of the ethanol. Several pretreatment process variables such as glucose yield, liquid: solid ratio, additional pretreatment stages, and lignin adsorption were varied to determine which parameters had the greatest effect on the process economics. Optimized values for these key variables became target values for the bench-scale research, either to achieve oridentify as potential obstacles in the future commercialization process. Results from this modeling and experimentation sequence have led to the design of an advanced two-stage engineering-scale reactor for a dilute-acid hydrolysis process.     

Cao吸附CO2系统能耗分析及热集成系统研究

本文以通用流程模拟软件Aspen为平台,对一个600 MW电厂排放的CO₂吸收过程进行了模拟,分析了关键参数对吸收系统性能影响。研究了采用余热锅炉回收系统热量后对整个电厂性能的影响规律,比较了采用25MPa,566/566℃;28MPa,580/580℃和30 MPa,600/600℃三种不同蒸汽参数时整个电厂性能。研究结果表明,采用钙法回收电厂CO₂并合理利用余热后系统效率下降约5个百分点。本文研究成果为基于火电站脱除CO₂提供有益的参考。