A. A. Askalany, B. B. Saha, M. S. Ahmed and I. M. Ismail, “Adsorption Cooling System Employing Granular Activate Carbon-R134a Pair for Renewable Energy Applications,” International Journal of Refrigeration, Vol. 36, No. 3, 2013, pp. 1037-1044. - References

Browse Menu >>

Browse Subjects >>

Computer Science & Communications

Earth & Environmental Sciences

Social Sciences & Humanities

Why Us? >>

- Open Access
- Peer-reviewed
- Rapid publication
- Lifetime hosting
- Free indexing service
- Free promotion service
- More citations
- Search engine friendly

Free SCIRP Newsletters>>

Add your e-mail address to receive free newsletters from SCIRP.

Contact Us >>

customer@scirp.org

+86 18163351462(WhatsApp)

1655362766

Paper Publishing WeChat

Book Publishing WeChat

(or Email:book@scirp.org)

Article citations
More>>

A. A. Askalany, B. B. Saha, M. S. Ahmed and I. M. Ismail, “Adsorption Cooling System Employing Granular Activate Carbon-R134a Pair for Renewable Energy Applications,” International Journal of Refrigeration, Vol. 36, No. 3, 2013, pp. 1037-1044.
http://dx.doi.org/10.1016/j.ijrefrig.2012.11.009

has been cited by the following article:

TITLE: Experimental Investigation of Granular Activated Carbon/R-134a Pair for Adsorption Cooling System Applications

AUTHORS: M. Attalla, S. Sadek

KEYWORDS: Adsorption; Activated Carbon; R-134a; Isosteric Heat

JOURNAL NAME: Journal of Power and Energy Engineering, Vol.2 No.2, February 15, 2014

ABSTRACT: The objective of this study is to investigate the adsorption characteristics of granular activated carbon GAC/R-134a pair in the temperature range of 20℃- 60℃and pressure up to 10 bars. The Dubinin-Astakhov adsorption equilibrium model is fit to experimental data with acceptable error limit. The pressure-temperature-concentration (P-T-X) diagram of the pair is also presented. The isosteric heat of adsorption of R-134a on activated carbon has been calculated using the Clausius-Clapeyron equation as a function of adsorption capacity. The maximum adsorption capacity was found to be 1.92 kgR134a/kg carbon at 20℃after 1200 s. The experimental results also show that the increase of heat transfer area improves the adsorption capacity per kg of adsorber, which leads to the design of a finned tubes heat exchanger adsorption unit.