Abstract
Experimental studies are carried out to characterize an indigenous, coconut shell based, activated carbon suitable for storage of natural gas. Properties such as BET surface area, micropore volume, average pore diameter and pore size distribution are obtained by using suitable instruments and techniques. An experimental setup is developed to estimate the equilibrium methane adsorption capacity and adsorption/desorption kinetics. The experimental isothermal uptake data is used to fit four different isotherm models. Using the constants obtained for the D–A isotherm model the variation of heat of adsorption and adsorbed phase specific heat with equilibrium pressure and temperature are obtained. Similarly Henry’s Law coefficients, important at low pressure and low uptake regime are also obtained. Finally using the kinetic data and a linear driving force model, constants in the kinetic equation are obtained. Results show that the indigenous material used in this study offers reasonably high natural gas storage capacity and fast kinetics and is suitable for adsorbed natural gas (ANG) applications. It is expected that this study will be useful in the design and development of ANG systems based on this indigenous material.
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References
Wang X and Economides M J 2012 Purposefully built underground natural gas storage. J. Natural Gas Sci. Eng. 9: 130–137
Biloe S, Goetz V and Mauran S 2001a Dynamic discharge and performance of a new adsorbent for natural gas storage. AIChE J. 47(12): 2819–2830
Biloe S, Goetz V and Mauran S 2001b Characterization of adsorbent composite blocks for methane. Carbon 39(11): 1653–1662
Chang K J and Talu O 1996 Behaviour and performance of adsorptive natural gas storage cylinders during discharge. Appl. Therm. Eng. 16(5): 359–374
Cook T L, Komodromos C, Quinn D F and Ragan S 1999 Adsorbent storage for natural gas vehicles. In: Burchell T D (ed) Carbon material for advanced technologies. USA: Pergamon, pp. 269–302
Mota J P B 2008 Adsorbed natural gas technology. Recent advances in adsorption processes for environmental protection and security. Netherlands: Springer, pp. 177–192
Wegrzyn J and Gurevich M 1996 Adsorbent storage of natural gas. Appl. Energy 55(2): 71–83
Choi B U, Choi D K, Lee Y W and Lee B K 2003 Adsorption equilibria of methane, ethane, ethylene, nitrogen and hydrogen onto activated carbon. J. Chem. Eng. Data 48(3): 603–607
Frere M G and De Weireld G F 2002 High-pressure and high-temperature excess adsorption isotherm of N2, CH4, and C3H8 on activated carbon. J. Chem. Eng. Data 47(4): 823–829
Himeno S, Komatsu T and Fujita S 2005 High-pressure adsorption equilibria of methane and carbon dioxide on several activated carbons. J. Chem. Eng. Data 50(2): 369–376
Loh W S, Rahman K A, Chakraborty A, Saha B B, Choo Y S, Khoo B C and Ng K C 2010 Improved isotherm data for adsorption of methane on activated carbons. J. Chem. Eng. Data 55(8): 2840–2847
Otowa T, Tanibata R and Itoh M 1993 production and adsorption characteristics of MAXSORB: High surface area active carbon, gas separation and purification. 7 (4): 241–245
Sahoo P K, John M, Newalkar B L, Choudhary N V and Ayappa K G 2011 Filling characteristics for an activated carbon based adsorbed natural gas storage system, Ind. Eng. Chem. Res. 50(23): 13000–13011
MacDonald J A F and Quinn D F 1998 Carbon adsorbents for natural gas storage. Fuel 77(1): 61–64
Saha BB, EI-Sharkawy I, Habib K, Srinivasan K and Dutta P 2007 Evaluation of adsorption parameters and heats of adsorption through desorption measurement. J. Chem. Eng. Data 52(6): 2419–2424
Seaton N A, Walton J P R B and Quirke 1989 A new analysis method for the determination of the pore size distribution of porous carbon from nitrogen adsorption measurements. Carbon 27(6): 853–861
Wang X, French J, Kandadai S and Chua H T 2010 Adsorption measurements of methane on activated carbon in the temperature range (281–343) K and pressure to 1.2 MPa, J. Chem. Eng. Data 55(8): 2700–2706
Ozawa S, Kusumi S and Ogino Y 1976 Physical adsorption of gases at high pressure. J. Colloid Interface Sci. 56(1): 83–91
Glueckauf E and Coates JI 1947 The influence of incomplete equilibrium on front boundary of chromatograms and effectiveness of separation. J. Chem. Soc. 1315–1321
Chihara K and Suzuki M 1983 Simulation of nonisothermal pressure swing adsorption. J. Chem. Eng. Jpn 16(1): 53–61
Gemmingen U V 1993 Pressure swing adsorption process-design and simulations. In: Suzuki M (ed) Proceedings of the fourth international conference on fundamentals of adsorption, Kyoto, Kodansha, Japan, pp. 703–712
Hartzog D G and Sircar S 1995 Sensitivity of PSA process performance to input variables. Adsorption 1(2): 133–151
Raghavan N S, Hassan M M and Ruthven D M 1986 Numerical simulation of PSA system using a pore diffusion model. Chem. Eng. Sci. 41(11): 2787–2793
Vasiliev L L, Kanonchik L E, Mishkinis D A and Rabetsky M I 2000 Adosorbed natural gas storage and transportation vessels. Int. J. Therm. Sci. 39(9): 1047–1055
Rahman K A, Chakraborty A, Saha B B and Ng K C 2012 On thermodynamics of methane + carbonaceous material adsorption. Int. J. Heat Mass Transfer 55(4): 565–573
Acknowledgement
The authors sincerely thank ICC Indo German Carbons Limited, Kerala, for supplying the above-mentioned activated carbon sample along with some of its material properties.
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Appendices
Nomenclature
- a :
-
instantaneous uptake (kg/kg)
- a eq :
-
equilibrium uptake (kg/kg)
- C p,g :
-
specific heat of the gaseous phase (kJ/kg)
- C p,a :
-
specific heat of the adsorbed phase (kJ/kg)
- E :
-
characteristic energy (J/mol)
- E a :
-
energy of activation (J/mol)
- K so :
-
pre-exponent constant (s−1)
- K H :
-
Henry’s constant (MPa−1)
- M :
-
molecular weight (kg/kmol)
- m s :
-
mass of the adsorbent (kg)
- P :
-
Pressure (Pa)
- R :
-
gas constant (kJ/(kg K))
- R u :
-
universal gas constant (kJ/(kmol K))
- T :
-
temperature (K)
- V :
-
volume (m3)
- v :
-
specific volume (m3/kg)
- W :
-
volumetric adsorbate uptake (m3/kg)
- W o :
-
the limiting volumetric adsorbate uptake (m3/kg)
- Z :
-
compressibility factor
Greek symbols
- \( \tau \) :
-
time (s)
- \( \Delta H_{ads} \) :
-
isosteric heat of adsorption (kJ/kg)
- \( \alpha \) :
-
thermal expansion coefficient (K−1)
- \( \rho \) :
-
density (kg/m3)
Subscripts
- a:
-
adsorbed
- b:
-
boiling
- cr:
-
critical
- He:
-
Helium
- Me:
-
Methane
- exp:
-
experimental
- pre:
-
predicted
- rea:
-
reactor
- sat:
-
saturation
- st:
-
storage
- t:
-
total
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Sahoo, S., Ramgopal, M. Experimental studies on an indigenous coconut shell based activated carbon suitable for natural gas storage. Sādhanā 41, 459–468 (2016). https://doi.org/10.1007/s12046-016-0483-x
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DOI: https://doi.org/10.1007/s12046-016-0483-x