Characterization of adsorbent composite blocks for methane storage

Biloé, S.; Goetz, V.; Mauran, Sylvain

doi:10.1016/s0008-6223(00)00288-8

Cited by 73 publications

(32 citation statements)

References 21 publications

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“…The performance of ANG storage is affected by the nature of the microporous solid (Biloe et al, 2002;Lozano-Castelló et al, 2002a;Lozano-Castelló et al, 2002b), the adsorbent size (MacDonald & Quinn, 1998;Biloe et al, 2001a), the scale of the ANG storage tank (Chang & Talu, 1996;Biloe et al, 2001b), the natural gas composition (Seki & Sumie, 2001;Pupier et al, 2005), and the inlet flowrate (Sahoo et al, 2011;Alhamid et al, 2015). During the filling process of natural gas into a storage tank, the gas undergoes several process stages, each of which has a mass transfer resistance that decreases the storage capacity.…”

Section: Introductionmentioning

confidence: 99%

Simulation of a Metal Organic Framework-based Adsorbed Natural Gas Storage Tank

Muharam¹,

Kusrini²,

Saubryani³

et al. 2018

IJTech

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An adsorbed natural gas storage tank was simulated in this work, with the objective being to predict the filling time, the filling capacity and the storage efficiency. A high-capacity HKUST-1 type metal-organic framework was used as adsorbent. The time-dependent phenomenological model of the adsorbed natural gas storage tank was developed considering mass, momentum and energy transfers. The cylindrical tank was 1.09 m in length with a radius of 0.15 m, and was equipped with an inlet hole for gas inflow. The simulation results show that the temperature increase in the tank due to adsorption heat is very significant. This affects the adsorption ability of the bed inside the tank, so the storage efficiency is consequently low. For the inlet gas flowrate of 50 L/min, the storage efficiency is 38% and increases to only 47% at 5 L/min. Corresponding filling capacities for the two flowrates are not very different, i.e. 89 V(STP)/V and 109 V(STP)/V. However, the difference in the filling times is extremely significant, which are 16 min at 50 L/min and 255 min at 5 L/min.

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Section: Introductionmentioning

confidence: 99%

Simulation of a Metal Organic Framework-based Adsorbed Natural Gas Storage Tank

Muharam¹,

Kusrini²,

Saubryani³

et al. 2018

IJTech

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“…There are several aspects that influence the performance of ANG storage (Pupier et al, 2005), namely the nature of the microporous solid (Biloe et al, 2002;Lozano-Castelló et al, 2002a;Lozano-Castello et al, 2002b;Matranga et al, 1992), the packing adsorbent scale (Biloe et al, 2001a;Burchell & Rogers, 2001;MacDonald & Quinn, 1998), the scale of ANG vessel (Biloe et al, 2001b;Chang & Talu, 1996) and the influence of the composition of natural gas during successive cycles of charge and discharge (Dvorak & Hodrien, 2001;Mota, 1999;Pupier et al, 2005;Seki & Sumie, 2001). …”

Section: Introductionmentioning

confidence: 99%

Effect of Methane Gas Flow Rate on Adsorption Capacity and Temperature Distribution of Activated

Alhamid¹,

Nasruddin²,

Senoadi³

et al. 2015

IJTech

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Adsorbed Natural Gas (ANG) is one of the gas storage methods which specialize in low pressure. This method is more competitive compared to Compressed Natural Gas (CNG). ANG is based on an adsorption process that involves adsorbate and adsorbent. This research is conducted to observe the effects of gas flow-rate on adsorption capacity and the temperature distribution of adsorbent. The adsorbent is a commercially activated carbon, and methane gas is the adsorbate. Methane flow rates are 1 standard liter per minute (SLPM) and 20 SLPM. Temperature in the pressure vessel is maintained at 25°C and the pressure at 3.5 MPa. The result shows that the adsorption capacity of activated carbon is higher at a lower gas flow rate. While a higher gas flow rate causes a higher temperature difference in the adsorption and in desorption process.

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“…In the literature, a lot of research work has been, and is being, carried out mainly on two classes of adsorbing microporous materials: zeolites and activated carbons [2,[5][6][7][8][9].Moreover, novel adsorbents, such as metal organic frameworks (MOFs), have been explored for the adsorption of methane [10,11]. Eddaoudi et al established a strategy based on reticulating metal ions and organic linkers into networks [12].…”

Section: Introductionmentioning

confidence: 99%

Methane Adsorption in a Series of IRMOFs Studied by PHSC and Sanchez–Lacombe Equations of State

Tahmooresi

Sabzi

2015

J Inorg Organomet Polym

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In this study, the methane adsorption on several kinds of isoreticular metal organic frameworks (IRMOF) has been modeled by applying perturbed hard sphere chain (PHSC) and Sanchez-Lacombe (SL) equation of state. PHSC and SL equation of state have three characteristic parameters calculated using group contribution method. In this study, the methane adsorption on absorbents, namely, IRMOF-6, IRMOF-8, IRMOF-10, IRMOF-14 has been obtained at temperature 298 K and various pressures up to 10 MPa. Finally, results have been compared with the simulated adsorption data points to show the precision of PHSC and SL equation of state in predicting the methane sorption trend.

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Characterization of adsorbent composite blocks for methane storage

Cited by 73 publications

References 21 publications

Simulation of a Metal Organic Framework-based Adsorbed Natural Gas Storage Tank

Simulation of a Metal Organic Framework-based Adsorbed Natural Gas Storage Tank

Effect of Methane Gas Flow Rate on Adsorption Capacity and Temperature Distribution of Activated

Methane Adsorption in a Series of IRMOFs Studied by PHSC and Sanchez–Lacombe Equations of State

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