共查询到19条相似文献,搜索用时 156 毫秒
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为寻求简单可靠的预冷方法作为氢液化高能耗替代,提出一种基于氮气逆布雷顿循环预冷的氢液化流程,相比于混合工质预冷循环,该流程结构简单,成本较低,适用于中小型氢液化系统。利用MATLAB软件建立了该流程的热力学模型,并利用Globalsearch求解器进行了优化分析;经对各种预冷方式的计算比较,氮气循环的能耗(2.68 kWh/kg)介于混合工质及液氮预冷之间,但其总热流比混合工质预冷更少。通过进行优化计算,该流程在传统液化系统的基础上能耗显著降低,能够达到8.33 kWh/kg。 相似文献
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引用经济学中"边际成本"的概念,提出了空分设备生产低温液体产品的"边际能耗"概念,计算出内压缩流程空分设备中液氧和液氮产品在各种情况下的边际能耗,并将计算结果与液化装置的液化单耗进行比较,提出适当增加内压缩流程空分设备的液体产量,可以提高空分设备的流程效率。 相似文献
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简单介绍了现有钢厂用液化设备流程的分类 ,主要从液化流程本身的特点和降低液化装置能耗两方面来探讨低压氧液化流程和中压氧液化流程。 相似文献
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流程计算模块是中压空分装置CAD的重要组成部分。介绍流程计算模块的总体结构、输入窗口、流程计算与优化模型、流程计算与换热器计算模块和精馏塔计算模块的关系以及输出窗口。这对于更好地运用该CAD和开发新的你 液化分离系统CAD具有理论和实际意义。 相似文献
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针对中国宁夏银川某一提氦工厂液化天然气蒸发气(LNG-BOG)提氦液化流程,采用Aspen Hysys构建BOG提氦气系统和氦气液化系统的流程模型,首先分析了BOG提氦气流程中关键参数对能耗设备的影响情况。之后采用遗传算法,以系统单位能耗为目标函数,分别对BOG提氦气系统和氦气液化系统中关键能耗参数进行优化。同时采用■分析方法,分析优化前后氦气液化系统的■效率以及■损失情况。结果表明,BOG提氦气系统和氦气液化系统经优化后系统单位能耗分别为8.351 5 kWh/Nm3和0.751 9 kWh/Nm3,相比优化前分别下降7.09%和14.71%,且氦气液化系统■效率较优化前提高了18.54%,■损失下降12.79%,换热器换热总量约上升2.54%。因此整个系统在优化后单位能耗有所降低,系统运行经济性得到提高。 相似文献
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《低温学》2014
This paper reviews the status of magnetic refrigeration system for hydrogen liquefaction. There is no doubt that hydrogen is one of most important energy sources in the near future. In particular, liquid hydrogen can be utilized for infrastructure construction consisting of storage and transportation. When we compare the consuming energy of hydrogen liquefaction with high pressurized hydrogen gas, FOM must be larger than 0.57 for hydrogen liquefaction. Thus, we need to develop a highly efficient liquefaction method. Magnetic refrigeration using the magneto-caloric effect has potential to realize not only the higher liquefaction efficiency >50%, but also to be environmentally friendly and cost effective. Our hydrogen magnetic refrigeration system consists of Carnot cycle for liquefaction stage and AMR (active magnetic regenerator) cycle for precooling stages. For the Carnot cycle, we develop the high efficient system with >80% liquefaction efficiency by using the heat pipe. For the AMR cycle, we studied two kinds of displacer systems, which transferred the working fluid. We confirmed the AMR effect with the cooling temperature span of 12 K for 1.8 T of the magnetic field and 6 s of the cycle. By using the simulation, we estimate the efficiency of the hydrogen liquefaction plant for 10 kg/day. A FOM of 0.47 is obtained for operation temperature between 20 K and 77 K including LN2 work input. 相似文献
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Accurate caloric data of mixtures are required for the process calculation of gas separation or liquefaction plants. Available methods for the prediction of enthalpies tend to become less accurate in mixtures containing hydrogen, in the two-phase region, and at high pressure pressures and low temperatures. Therefore an apparatus was designed to measure the specific heat capacity over a wide range of temperatures and pressures. 相似文献
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能量桩储热技术是以太阳能和混凝土桩作为复合热源的热泵系统,在混凝土桩内部埋设换热管,利用太阳能集热板将热量通过混凝土桩中的换热管储存在土壤中。本文采用柱热源模型对桩群进行180天的连续储热过程模拟计算,对地下土壤温度场进行分析,得出4 m的桩间距下,能量桩间的储热相互影响较小,效果较佳。 相似文献
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Renewable Energy Sources (RES) exploitation for electric energy and hydrogen production has been identified as one of the leading ways towards a future sustainable energy system. Hydrogen can be stored and transported in gaseous (GH2) or liquid form (LH2). When large hydrogen storage is required, liquefaction can be convenient with respect to compression, because of its higher storage density. LH2 can also be used as a coolant for superconducting lines, acting at the same time as energy vector and cryogen. In particular, in this paper we focus on the MgB2 material mainly due to economic considerations and working temperature match with LH2. A system for large scale RES exploitation allowing flexible and controlled delivery of electric energy and LH2 is presented. For the thermo-hydraulic design, a method is proposed which resorts to compressible fluid equations put in a convenient simplified form. A case application with 20 km distance between cooling stations is considered, and the need of taking into account LH2 compressibility for pipeline design is shown. 相似文献
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通过对一种新颖的高压氮膨胀液化液氧泵内压缩常温分子筛净化空分流程的组织构思和对换热、制冷、精馏系统全面的计算,为开拓化工企业高压用氧(9.5MPaA)的新型空分流程探索出了一条可行的路。根据计算,新流程和原有的高压氮节流液化液氧泵内压缩切换式换热器冻结空分流程相比,氧提取率可提高9%,单位氧能耗可下降2%,流程组织大大简化,高压氧的生产安全可靠,显示了新流程的生机。 相似文献