2008
DOI: 10.1016/j.applthermaleng.2007.12.015
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Attapulgite based LiCl composite adsorbents for cooling and air conditioning applications

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Cited by 60 publications
(7 citation statements)
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“…The total mass loss of ~15 wt.%, ~14 wt.%, and ~14 wt.% was observed in the TG curves during heating. The TG curve of M1A3 microspheres showed mass loss stages before 700°C obviously, which could be attributed to the evaporation of free water (RT‐135°C), loss of coordinated water (135‐470°C), constitution water (470‐700°C) of palygorskite and combustion of carbon and organic matters during the heating process (Figure A). As for the DTA curves, the endothermic peak presented at 540°C ranged from 400 to 600°C, was mainly due to the dehydration of −OH groups of the kaolinite phase surface and formation of metakaolin, as described by the following reaction Equation 3 .…”
Section: Resultsmentioning
confidence: 99%
“…The total mass loss of ~15 wt.%, ~14 wt.%, and ~14 wt.% was observed in the TG curves during heating. The TG curve of M1A3 microspheres showed mass loss stages before 700°C obviously, which could be attributed to the evaporation of free water (RT‐135°C), loss of coordinated water (135‐470°C), constitution water (470‐700°C) of palygorskite and combustion of carbon and organic matters during the heating process (Figure A). As for the DTA curves, the endothermic peak presented at 540°C ranged from 400 to 600°C, was mainly due to the dehydration of −OH groups of the kaolinite phase surface and formation of metakaolin, as described by the following reaction Equation 3 .…”
Section: Resultsmentioning
confidence: 99%
“…Other authors proposed other promising adsorbents such as attapulgite clay sorbents impregnated with inorganic salts [55,56], silicalite MCM-41 [57] or zeolite/active carbon compounds [58], that showed attractive sorption properties for utilization of low grade heat. Figure 1.7 shows the water adsorption isobar (p H 2 O ¼ 11 mbar) measured at CNR ITAE for different adsorbents by the thermo-gravimetric technique based on a Cahn microbalance.…”
Section: New Trendsmentioning
confidence: 99%
“…The adsorption-desorption performance for ammonia on the composite adsorbent was measured in the device shown Figure 2 [14] . The experimental equipment system was made up of adsorption column, ammonia cylinder, vacuum pump and thermostatic device.…”
Section: Investigating Adsorption-desorption and Refrigeration Permentioning
confidence: 99%