1) total cooling capacity
全冷量
1.
Presents two calculating method of total cooling capacity and sensible cooling capacity by a theoretical analysis,namely the efficiency method and the condition transformation method.
通过理论分析提出了风机盘管全冷量和显冷量的两种计算方法:效率法和工况转换法。
2) all-year cooling energy consumption
全年耗冷量
1.
Under the three basic kinds of different conditions, namely, different climates, different fresh air supply ways, whether distinguishing interior and exterior zones, the statistical air-conditioning design cooling load and all-year cooling energy consumption indexes in high-rise office building were got by arranging spare factors resort to orthogonal table and afterward simulating by DOE-2.
以不同的气候条件、不同的新风方式、分内外区与否为三类基本不同条件,用正交表安排剩余因素并用DOE-2软件进行模拟计算,得出高层办公建筑空调系统设计冷负荷与全年耗冷量的统计估算指标:哈尔滨、北京、上海三城市的设计冷负荷统计估算值分别为138。
3) cold energy
冷量
1.
Cryogenic pulverization process of waste rubber based on cold energy of liquefied natural gas(LNG)
基于液化天然气(LNG)冷量的废旧橡胶低温粉碎工艺流程
2.
According to the characteristics of the cold energy of liquefied natural gas(LNG),a new recovery process of light hydrocarbons from liquefied natural gas was presented based on the gradient utilization of cold energy.
根据液化天然气(LNG)冷量的特性,按照冷量梯级利用的原则,设计了一种新的LNG轻烃分离流程,其特征在于轻烃分离过程不需要使用压缩机,能耗较低,而且可利用LNG的冷量将一部分分离完轻烃的甲烷再液化过冷并低压液相储存,使轻烃分离流程具有供气调峰功能,同时使分离获得的轻烃产品保持低压液相,方便产品的储运和销售。
3.
Aimed at the shortage problem of cold energy of rectisol plant,made comprehensive analysis,found out reasons and proposed solutions.
针对低温甲醇洗冷量不足问题,进行系统分析,查找原因,并提出解决方案。
5) cool exergy
冷量
6) cool anergy
冷量
1.
Based on laws of thermodynamics and definition of exergy and anergy,in this paper computaion method for cool exergy and cool anergy was inquired.
以热力学第一、二定律为基础 ,结合、的基本定义 ,探讨了冷量、冷量的计算方法 ,指出了当前分析理论体系中存在的‘冷量、冷量计算方法不能与热力学第一定律相统一’的问题 ,提出了新的计算方法 ,使得冷量计算方法更科学、严
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