Applied thermal engineering2022,Vol.2109.DOI:10.1016/j.applthermaleng.2022.118355

Dehumidification behavior of an aluminophosphate zeolite coated crossflow heat exchanger driven with direct hot water heating and evaporative cooling

Sunhor, Seng Osaka, Yugo Tsujiguchi, Takuya Kodama, Akio Saputra, Dendi Adi
Applied thermal engineering2022,Vol.2109.DOI:10.1016/j.applthermaleng.2022.118355

Dehumidification behavior of an aluminophosphate zeolite coated crossflow heat exchanger driven with direct hot water heating and evaporative cooling

Sunhor, Seng 1Osaka, Yugo 1Tsujiguchi, Takuya 1Kodama, Akio 1Saputra, Dendi Adi1
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作者信息

  • 1. Kanazawa Univ
  • 折叠

Abstract

In this study, a crossflow-type heat exchanger coated with aluminophosphate zeolite was tested for desiccant dehumidification with direct-supplied hot water and evaporative cooling using remaining hot water. This evaporative cooling process could accelerate dehumidification by removing the heat of adsorption. Therefore, the influences of the cooling air velocity, regeneration hot water temperature, and adsorption/regeneration cycle time were experimentally investigated. The result showed that the minimum humidity of the adsorption outlet air decreased with an increase in the cooling air velocity and adsorption/desorption time, indicating that the complete regeneration of coated adsorbents is required to significantly decrease humidity. However, the maximum time-averaged amount of dehumidification appeared at an appropriate cycle time, which avoided adsorption saturation during the adsorption period. Further, in any case, increasing the cooling air velocity had a positive impact on both the momentary observed minimum humidity and time-averaged amount of dehumidification.& nbsp;At all cooling air velocity, the temperature of the hot water contributed to the increase in the time-averaged amount of dehumidification. However, when the hot water temperature was 55 ?, the cooling effect of evap-orative was not observed, even when the cooling air velocity reached 1.5 m/s. Considering that the actual temperature of the coated adsorbent was expected to be much lower than that of the supplied hot water, the hot water temperature should have been >=& nbsp;65 ?.

Key words

Desiccant dehumidification/Thermal swing adsorption/Coated adsorbent/Crossflow heat exchanger/Evaporative cooling/Direct hot water heating/AIR-CONDITIONING SYSTEM/SOLID DESICCANT/SILICA-GEL/PERFORMANCE/VAPOR/ENERGY

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出版年

2022
Applied thermal engineering

Applied thermal engineering

EISCI
ISSN:1359-4311
被引量8
参考文献量29
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