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Energy Performance of Low Charge, Central Type, Dual Stage NH3 Refrigeration Systems in Practice

机译:低电荷,中央型,双级NH3制冷系统的能量性能

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Development of low charge NH3 refrigeration systems is taking place throughout the world for various applications, predominantly for refrigerated storage and packaged solutions to chill liquids and/or condition refrigerated spaces. These developments are initiated by a global phase-down of high global warming (GWP) refrigerants of the hydro fluorocarbon (HFCJ type. This phase-down is a direct result of the "top-down" emissions reduction agreement resulting from the Conference of the Parties (COP 21) in Paris, December 12, 2015. Ammonia refrigerant offers improved vapor compression cycle efficiencies in comparison with most other refrigerants. The energy performance improvements associated with the application of ammonia refrigerant in combination with other energy efficiency engineering techniques such as state-of-the-art superheat/quality (SH/X) expansion control, advanced low charge evaporator technology, extensive integration of variable frequency drives, two-stage compression, low oil carry-over compressors, low friction loss pipe lines, and genuine central plant concept have not been the subject of widespread investigations and reporting. Where compliance costs are directly proportional with NH3 inventory, favoring multiplexing as opposed to central plants is tempting for stakeholders. This, of course, risks sacrificing energy performance in return for reduction in NH3 inventory. For signatories to the COP 21 agreement, this is neither in the national interest nor is it in the commercial interest of plant owners if compliance cost increases outweigh energy cost reductions. This paper describes the energy performances of several refrigerated distribution centers with storage volumes of approximately 10,000 to 50,000 m~3 (353,000 to 1,766,000 ft~3). The performance evaluations are based on the electrical energy consumption as measured by the electrical energy providers over representative periods of time. All systems are serviced by central, state-of-the-art low charge, dual stage NH3 refrigeration systems. In the case of one plant the contribution of the photovoltaic panels to the energy requirement of the facility as a whole is shown on a month-by-month basis. An energy performance comparison is also made between two refrigerated distribution centers with a volume of approximately 10,000 m~3 (353,000 ft~3), but serviced by two different types of ammonia refrigeration systems. In one case the plant is a single-stage economized dual screw compressor based system with gravity flooded refrigerant feed. In the other case, the plant is a central, low charge NH3 dual-stage system with speed controlled semi industrial reciprocating compressors. Other features of the two facilities include general warehouse designs that are more or less identical. The energy performance comparisons are again based on the electrical energy consumption as recorded by the electrical energy provider over one calendar year.
机译:低电量NH3制冷系统的发展正在发生在世界各地的各种应用,主要用于冷藏和包装解决方案,以冷静的液体和/或条件冷藏空间。这些发展是由氢氟烃的(一个全球性的逐步减少高全球变暖(GWP)制冷剂HFCJ式开始。这个阶段下从的会议产生的“自上而下”的减排协议的直接结果方(COP 21)在巴黎,12月12日2015年氨致冷剂报价与大多数其他制冷剂相比,改善蒸汽压缩循环的效率。与氨制冷剂在组合应用与其他能源效率工程技术,诸如状态关联的能量的性能改进-of先进过热/质量(SH / X)扩展控制,先进的低电荷蒸发器技术,变频驱动器的广泛集成,双级压缩,低油结转压缩机,低摩擦损失管路,和真正的中央工厂的概念还没有被广泛的调查和报告的主题。如果守法成本与NH3库存,F成正比avoring复用,而不是中央的植物是诱人利益相关者。这,当然,风险以换取减少NH3库存牺牲节能性能。对于签署缔约方会议21协议,这既不符合国家利益,也不是植物所有者的商业利益,如果合规成本增加超过能源成本的降低。本文描述了大约10,000到50,000 m3的(353,000至1766000英尺〜3)的存储卷的几个冷藏配送中心能源性能。如由电能供应商在一段时间周期代表测得的性能评价是基于电能耗。所有的系统都通过中央,国家的最先进的低电荷,双级NH3制冷系统提供服务。在一个设备的情况下的光伏面板的设施作为一个整体的能量需求的贡献被示出在一个月逐月基础。能量性能比较也有两个冷冻配送中心之间具有大约万米的体积制成〜3(353000英尺〜3),但通过两种不同类型的氨制冷系统的维修。在一种情况下该植物是节约双螺杆式压缩机为基础的系统与重力单级制冷剂淹没饲料。在其他情况下,所述植物是中央,低电荷NH3双级系统具有速度控制的半工业往复式压缩机。这两个设施其他功能还包括普通仓的设计,都或多或少相同。能源性能比较再次基于所记录的超过历年的电能供应的电能消耗。

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