2004
DOI: 10.1016/j.ijrefrig.2003.10.004
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Mass recovery adsorption refrigeration cycle—improving cooling capacity

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Cited by 120 publications
(32 citation statements)
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“…In 1929, Hulse and Miller described an adsorption system using in the United States for the air conditioning system of railway carriages [2], in which Silica gel-sulphur dioxide was chosen as the adsorbent/adsorbate pair. In recent times, the adsorption pairs mostly used include ammonia-carbon [3,4], ammonia-salts [5,6], methanol-carbon [7,8], water-silica gel [9,10] and water-zeolite [11,12]. The sub-atmospheric refrigerants (water and methanol) have excellent thermodynamic properties but their specific cooling power (kW of cooling per kg of adsorbent) can be limited by low mass transfer rates resulting from pressure drops, internal diffusion etc.…”
Section: Introductionmentioning
confidence: 99%
“…In 1929, Hulse and Miller described an adsorption system using in the United States for the air conditioning system of railway carriages [2], in which Silica gel-sulphur dioxide was chosen as the adsorbent/adsorbate pair. In recent times, the adsorption pairs mostly used include ammonia-carbon [3,4], ammonia-salts [5,6], methanol-carbon [7,8], water-silica gel [9,10] and water-zeolite [11,12]. The sub-atmospheric refrigerants (water and methanol) have excellent thermodynamic properties but their specific cooling power (kW of cooling per kg of adsorbent) can be limited by low mass transfer rates resulting from pressure drops, internal diffusion etc.…”
Section: Introductionmentioning
confidence: 99%
“…The mass recovery cycle may greatly improve the system performance, compared with the conventional cycle powered by low temperature heat [7]. The process involves changing the pressure in adsorbent beds.…”
Section: Mass Recovery Cyclementioning
confidence: 99%
“…These studies have revealed the importance of heat and mass recovery that increases the coefficient of performance (COP), by developing appropriate models which compare favourably with experiments. Within this context, Akahira et al (2004) proposed a clever new strategy for mass recovery in conventional two-bed adsorption chillers. During the mass recovery process, hot water is supplied to the desorber while the adsorber is continuously supplied with cooling water; the additional heating and cooling accelerates the desorption/adsorption process, enhancing mass circulation and providing better cooling output.…”
Section: Introductionmentioning
confidence: 99%