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adsorption refrigeration volume
相关语句
  吸附制冷量
     Adsorption refrigeration volume of M1-9906-water pairs is 2.0~2.5 times that of 13X-water.
     M1-9906-水工质对的吸附制冷量是13X-水的2.0~2.5倍;
短句来源
     Regenerated at temperature of 60~120℃, adsorption refrigeration volume of M4-0132-water pairs is 441~924kJ?
     在60~120℃再生条件下,M4-0132-水工质对的吸附制冷量为441~924kJ?
短句来源
     3、Adsorptive working pairs of water and alcohol with composite sorbents respectively take on higher adsorption refrigeration volume and specific cooling power.
     3、水、乙醇与复合吸附剂组成的吸附工质对具有较大的吸附制冷量和制冷功率。
短句来源
     QC-1-water and QC-2 pairs which take on higher adsorption refrigeration volume and specific cooling power are two kinds of desirable working pairs, which can be applied to the adsorption refrigeration system driven by solar energy or other low-grade heat source.
     QC-1-水和QC-2-乙醇有着较大的吸附制冷量和制冷功率,是两组性能优良的吸附制冷工质对,可用于以太阳能等低温热能驱动的吸附制冷系统。
短句来源
  “adsorption refrigeration volume”译为未确定词的双语例句
     Adsorption refrigeration volume of the single-used composite adsorbent is improved about 7.5%~12.5%.
     单位质量吸附剂的制冷量提高7.5%~12.5%;
短句来源
     The adsorption refrigeration volume of the M1-9906-water working pair is 2.0~2.5 times that of 13x-water;
     M4一0132吸附剂最适宜的原料配比为:MIO一40%,M3一20%,M4一20%,其它一20%,扩孔剂为 EZ。
短句来源
     Adsorption refrigeration volume of adsorbent mixed with scrap iron is 24% higher than that of the pure adsorbent.
     混装铁屑的吸附剂制冷量比其单独使用时高24%。
短句来源
  相似匹配句对
     Solid Adsorption Refrigeration and Its Development
     固体吸附式制冷技术及其研究进展
短句来源
     Progress on Adsorption Refrigeration Technology
     固体吸附式制冷技术的概况及进展
短句来源
     The Volume P.T.
     T.
短句来源
     Adsorption refrigeration volume of adsorbent mixed with scrap iron is 24% higher than that of the pure adsorbent.
     混装铁屑的吸附剂制冷量比其单独使用时高24%。
短句来源
     STUDY ON ADSORPTION THEORY OF VOLUME FILLING OF MICROPORES
     微孔容积填充吸附理论的研究
短句来源
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A new technology,adding materials of strong thermal conductivity for preparation adsorbents or mixing with adsorbents in the adsorber, for enhancing thermal conductivity of adsorbent, were studied. Adsorption isotherms of composite adsorbents were obtained by high-vacuum gravimetric method. Adsorption and desorption performance of adsorbents were determined through differential thermal anaylysis (DTA). Estimation for heat transfer properties of adsorbent was carried out in simulation device of adsorption...

A new technology,adding materials of strong thermal conductivity for preparation adsorbents or mixing with adsorbents in the adsorber, for enhancing thermal conductivity of adsorbent, were studied. Adsorption isotherms of composite adsorbents were obtained by high-vacuum gravimetric method. Adsorption and desorption performance of adsorbents were determined through differential thermal anaylysis (DTA). Estimation for heat transfer properties of adsorbent was carried out in simulation device of adsorption refrigeration cycle system. The results showed that: There is a distinct enrichment of heat conduction of adsorbents modified. Temperature difference of heat transfer for the adsorber is lowered 23%~30%. The shape of adsorption isotherms for composite adsorbents does not change, but adsorption capacity of them reduces a little. Adsorption refrigeration volume of the single-used composite adsorbent is improved about 7.5%~12.5%. Adsorption refrigeration volume of adsorbent mixed with scrap iron is 24% higher than that of the pure adsorbent.

采用混装和添加导热材料强化吸附剂的传热,在高真空重量装置上测定了复合吸附剂的吸附等温线;对吸附剂的吸附和脱附性能进行了差热分析;在吸附制冷循环模拟实验装置上评价了吸附剂传热性能。结果表明:添加导热材料制备的吸附剂导热性能得到了明显改善,吸附床层传热温差降低了23%~30%;复合吸附剂等温线形状没有发生改变,吸附质量分数有所下降;单位质量吸附剂的制冷量提高7.5%~12.5%;混装铁屑的吸附剂制冷量比其单独使用时高24%。

Composite adsorbents (M4-0132,M1-9906,M1-0001 and M2-0003), which demonstrate favorable adsorption refrigeration performance,were prepared through combining a series of main adsorptive materials, such as 13X molecular sieve, concavo-convex stick stone and strontium chloride. Adsorption isotherms of water or ethanol on composite adsorbents were determined. According to the fitting parameters of the adsorption isotherms, the calculations show that the characteristic adsorption work of self-prepared composite adsorbents-water...

Composite adsorbents (M4-0132,M1-9906,M1-0001 and M2-0003), which demonstrate favorable adsorption refrigeration performance,were prepared through combining a series of main adsorptive materials, such as 13X molecular sieve, concavo-convex stick stone and strontium chloride. Adsorption isotherms of water or ethanol on composite adsorbents were determined. According to the fitting parameters of the adsorption isotherms, the calculations show that the characteristic adsorption work of self-prepared composite adsorbents-water adsorption working pairs is about 12%~29% that of 13X molecular sieve-water pair, and that of composite adsorbents-ethanol pairs is approximately10%~20% that of activated carbon-ethanol pair. The stable state equilibrium equation for adsorption refrigeration system (liquid-vapor-adsorbent) was set up. The favorable refrigeration systems (situations) of working pairs, consisted of water and ethanol with composite adsorbents, were discussed, and the results show that: M4-0132-water and M1-0001-water pairs can be utilized for refrigeration system requiring larger cooling cycle volume, i.e air conditioning system, while M1-9906-ethanol and M2-0003-ethanol pairs are more preferable to low-temperature refrigeration system, i.e ice-making and chilling system. Adsorption refrigeration volume of M1-9906-water pairs is 2.0~2.5 times that of 13X-water. Regenerated at temperature of 60~120℃, adsorption refrigeration volume of M4-0132-water pairs is 441~924kJ?kg?1, while regenerated at 40~100℃, said cooling volume of M1-0001-alcohol pairs is 315~909kJ?kg?1, which is 2.2~5.9 times that of activated carbon-ethanol pairs.

选取13X分子筛、凹凸棒土和氯化锶等为主要吸附材料,制备了一系列有着优良吸附性能的复合吸附剂(M4-0132、M1-9906、M1-0001和M2-0003)。测定了水、乙醇在自制复合吸附剂上的吸附等温线。根据吸附等温线拟合参数对水、乙醇与自制复合吸附剂组成的吸附工质对的特征吸附功计算表明:复合吸附剂-水吸附工质对的特征吸附功约为13X分子筛-水的12%~29%;复合吸附剂-乙醇吸附工质对的特征吸附功约为活性炭-乙醇的10%~20%。采用吸附制冷体系(液体-气体-吸附剂)的稳态平衡方程,对水和乙醇与复合吸附剂组成的吸附工质对适合的制冷场合分析表明:M4-0132-水和M1-0001-水工质对可用于大循环量的制冷体系,例如空调系统的场合;M1-9906-乙醇和M2-0003-乙醇工质对可用于低温制冷体系,例如制冰和冷冻系统的场合。M1-9906-水工质对的吸附制冷量是13X-水的2.0~2.5倍;在60~120℃再生条件下,M4-0132-水工质对的吸附制冷量为441~924kJ?kg?1。40~100℃再生条件下,M1-0001-乙醇工质对的吸附制冷量315~909kJ?kg?1,是活性炭-乙醇的2.2~5....

选取13X分子筛、凹凸棒土和氯化锶等为主要吸附材料,制备了一系列有着优良吸附性能的复合吸附剂(M4-0132、M1-9906、M1-0001和M2-0003)。测定了水、乙醇在自制复合吸附剂上的吸附等温线。根据吸附等温线拟合参数对水、乙醇与自制复合吸附剂组成的吸附工质对的特征吸附功计算表明:复合吸附剂-水吸附工质对的特征吸附功约为13X分子筛-水的12%~29%;复合吸附剂-乙醇吸附工质对的特征吸附功约为活性炭-乙醇的10%~20%。采用吸附制冷体系(液体-气体-吸附剂)的稳态平衡方程,对水和乙醇与复合吸附剂组成的吸附工质对适合的制冷场合分析表明:M4-0132-水和M1-0001-水工质对可用于大循环量的制冷体系,例如空调系统的场合;M1-9906-乙醇和M2-0003-乙醇工质对可用于低温制冷体系,例如制冰和冷冻系统的场合。M1-9906-水工质对的吸附制冷量是13X-水的2.0~2.5倍;在60~120℃再生条件下,M4-0132-水工质对的吸附制冷量为441~924kJ?kg?1。40~100℃再生条件下,M1-0001-乙醇工质对的吸附制冷量315~909kJ?kg?1,是活性炭-乙醇的2.2~5.9倍。

 
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