共查询到18条相似文献,搜索用时 109 毫秒
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IGCC空气侧整体综合优化的研究 总被引:4,自引:1,他引:3
主要符号表X。。氮气回注系数如空分整体化系数E。;c燃气轮机压气机效率G。l回注氮气流量万燃气轮机透平前温尼。”系统相对效率G。。煤气氮气掺混流量Ea;,c空气专用压缩机效率N。”系统相对功率1前言整体煤气化联合循环(IGCC)系统模拟与优化逐步受到重视,开展了许多相关研究[‘-‘]。但是,现有的方法[‘,‘]一个突出的问题,它是在设定的具体流程方案下的数值分析,这常常导致落入“局部优化掩盖了整体最优”的误区。本文是研究以空分系统为中心的空气侧子系统的整体优化,阐述基本概念,尝试新方法,并结合大型商业化装… 相似文献
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水煤浆与干粉给料方式两种IGCC系统的(火用)分析 总被引:5,自引:0,他引:5
通过将煤气化过程与联合循环系统相结合,IGCC成为目前最有发展前途的洁净煤技术之一.但以往对IGCC系统的研究多集中联合循环或气化过程本身,而忽略了气化效率对系统整体性能的影响.为揭示气化过程与系统性能之间联系,本文对Texaco与Shell公司的两个IGCC系统实例分别进行了流程模拟和(火用)分析,并着重从热力学角度比较了系统煤气化部分的差异对系统整体性能的影响,得出结论:Shell煤气化技术与Texaco煤气化技术相比,气化过程的(火用)损失相对减小15%,冷煤气效率提高2.6个百分点,系统热转功效率上升2.1个百分点.本文研究成果为IGCC系统进一步改进提供了热力学基础理论支撑. 相似文献
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用于IGCC的燃气轮机技术方案与性能预测 总被引:4,自引:2,他引:2
主要符号表T温度G质量流量。压气机压比。压气机进口导叶安装角N功率X。压损系数X。。氮气回注系数X。;,空分整体化系数下标a空气cg煤气0烧天然气时设计工况。氮气as空分装置f燃料O。氧气1Bu8整体煤气化联合循环(IGCC)燃气轮机与常规的燃机有很大的差异[“l。它改烧中低热值的合成煤气,其燃料量比烧高热值的油气时要增大几倍;不同空分方案和采用不同的NZ回注掺混量时,情况就更为复杂。透平工质流量比压气机空气流量相差很多,燃气轮机总是处于复杂的变工况状态。2IGCC中燃气轮机技术方案归纳IGCC中燃气轮机可行的技术方案… 相似文献
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IGCC系统多目标性能统一量化评价准则 总被引:3,自引:1,他引:2
本文探讨能够综合评估IGCC系统热力、经济和环保性能的统一量化多目标评价准则,提出采用综合性能指标(CPI)作为评价准则来评估IGCC系统的综合性能。文中对该指标进行深入分析并推导出它与热力特性参数、经济因素及环保特性等关联的系统综合性能指标方程,并在IGCC综合性能的评估与优化中首次将环保变量(CO2回收率)作为系统独立设计变量进行研究。基于新的评价准则,本文开展对回收CO2的新型IGCC系统的实例研究,揭示IGCC系统综合性能与独立设计变量的关联规律,开拓系统多目标综合优化的新方法。本文研究成果为IGCC系统综合性能的评估和设计优化提供了新的思路与准则。 相似文献
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400MW级IGCC机组变工况性能计算 总被引:3,自引:0,他引:3
1引言一个多世纪以来,煤一直是世界上主要的发电燃料,这一趋势将在较长的时间内一直保持下去。对于中国这样一个以煤作为一次能源的国家,这一现象尤为突出。特别是随着全球性能源危机的出现以及环境保护要求的提高,使得洁净煤技术(CCT)受到普遍关注。在众多的洁净煤发电技术中,IGCC技术以其特有的高效率、低污染等特点,被认为是下世纪最有发展前途的洁净煤发电技术之一。鉴于IGCC系统结构与组态非常复杂,涉及煤的气化、净化、燃气轮机、余热锅炉、蒸汽轮机、空气分离等关键技术,因此建立IGCC系统的性能模型,对IGCC机组的… 相似文献
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Thermal power plant is one of the important thermodynamic devices, which is very common in all kinds of power generation systems. In this paper, we use a new concept, entransy loss, as well as exergy destruction, to analyze the single reheating Rankine cycle unit and the single stage steam extraction regenerative Rankine cycle unit in power plants. This is the first time that the concept of entransy loss is applied to the analysis of the power plant Rankine cycles with reheating and steam extraction regeneration. In order to obtain the maximum output power, the operating conditions under variant vapor mass flow rates are optimized numerically, as well as the combustion temperatures and the off-design flow rates of the flue gas. The relationship between the output power and the exergy destruction rate and that between the output power and the entransy loss rate are discussed. It is found that both the minimum exergy destruction rate and the maximum entransy loss rate lead to the maximum output power when the combustion temperature and heat capacity flow rate of the flue gas are prescribed. Unlike the minimum exergy destruction rate, the maximum entransy loss rate is related to the maximum output power when the highest temperature and heat capacity flow rate of the flue gas are not prescribed. 相似文献
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本文基于Aspen plus软件对燃用低热值煤气的燃气蒸汽联合循环系统进行了模拟仿真。在该仿真平台上对系统设计工况进行了计算验证。在设计工况下,燃气透平进口温度为1000~1050℃,模拟计算结果为1016.2℃。燃气透平出口温度设计参数为517.2℃,模拟结果为519.2℃。结果表明仿真模型能够准确模拟系统稳态情况的各种工况。本文还运用矩阵模式热经济学的方法对系统设计工况下的(?)流成本进行了计算分析,对系统进行了技术经济评价。燃气轮机和蒸汽轮机电能耗费的能量成本分别为22.2,24.06和16.64$·GJ-1。 相似文献
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Dario Colorado-Garrido Gerardo Alcal-Perea Francisco Alejandro Alaffita-Hernndez Beatris Adriana Escobedo-Trujillo 《Entropy (Basel, Switzerland)》2021,23(9)
The purpose of this research is the calculation of the exergy destruction of the single-flash and double-flash cycles of a geothermal power plant located on the ladder of the 233 m Cerro Prieto volcano, on the alluvial plain of the Mexicali Valley, Mexico. The methodology developed in this research presents thermodynamic models for energy and exergy flows, which allows determining the contribution of each component to the total exergy destruction of the system. For the case-base, the results indicate that for the single-flash configuration the efficiency of the first and second law of thermodynamics are 0.1888 and 0.3072, as well as the highest contribution to the total exergy destruction is provided by the condenser. For the double-flash configuration, the efficiency of the first and second law of thermodynamics are 0.3643 and 0.4983. The highest contribution to the total exergy destruction is provided by the condenser and followed by the low-pressure turbine. 相似文献
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本文针对传统焦炭生产工艺的不足、并应用联产系统整合思路,研究提出新型焦炭动力联产系统.新系统取消了传统炼焦工艺中直接燃用焦炉煤气为炭化室提供炼焦热量的方式,采用外置煤炭燃烧室提供热量,从而实现用低品质煤炭替代高品质焦炉煤气;节省下来的富氢、高热值的焦炉煤气作为燃料提供给联合循环,实现高效洁净发电;改进炼焦过程烟气废热回收方式,使得排烟损失大大降低.分析结果表明,新系统具有优良的热力性能,相对节能率高达15%左右.对系统关键过程的图像(火用)分析分析表明,燃烧过程和换热过程等变革与改进是系统性能提升的关键所在.本文研究将为冶金生产的可持续发展提供新思路与新系统方案. 相似文献
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Masoomeh Bararzadeh Ledari Yadollah Saboohi Antonio Valero Sara Azamian 《Entropy (Basel, Switzerland)》2021,23(1)
This paper explains a thorough exergy analysis of the most important reactions in soil–plant interactions. Soil, which is a prime mover of gases, metals, structural crystals, and electrolytes, constantly resembles an electric field of charge and discharge. The second law of thermodynamics reflects the deterioration of resources through the destruction of exergy. In this study, we developed a new method to assess the exergy of soil and plant formation processes. Depending on the types of soil, one may assess the efficiency and degradation of resources by incorporating or using biomass storage. According to the results of this study, during different processes from the mineralization process to nutrient uptake by the plant, about 62.5% of the input exergy will be destroyed because of the soil solution reactions. Most of the exergy destruction occurs in the biota–atmosphere subsystem, especially in the photosynthesis reaction, due to its low efficiency (about 15%). Humus and protonation reactions, with 14% and 13% exergy destruction, respectively, are the most exergy destroying reactions. Respiratory, weathering, and reverse weathering reactions account for the lowest percentage of exergy destruction and less than one percent of total exergy destruction in the soil system. The total exergy yield of the soil system is estimated at about 37.45%. 相似文献