Charge-Discharge Characteristics of an Adsorbed Natural Gas Storage System under Ambient Conditions

2014 ◽  
Vol 592-594 ◽  
pp. 1448-1455 ◽  
Author(s):  
Satyabrato Sahoo ◽  
Maddali Ramgopal

The performance of an adsorbed natural gas (ANG) storage system with natural convection heat transfer between the ANG bed and the ambient air is studied. Results are obtained for the bed without and with external fins on ambient air side. A one dimensional transient conduction model with suitable kinetic equation is formulated to simulate the performance of the bed filled with a homogeneous mixture of activated carbon and graphite. The model duly considers non-ideal behaviour of natural gas, variable specific heat of the adsorbed phase and heat of adsorption. Results are obtained for the case of constant pressure charging and constant flow discharging. The performance of the ANG bed is evaluated in terms of delivery capacity and discharge time. Results are obtained at an ambient temperature of 308 K and 35 bar for a charging time of 3.34 min. It is found that under this condition, the bed temperature increases by 70 and 45K and the storage capacity reduces by 75 and 60% without and with external fins, respectively. During discharge also, due to insufficient heat supply the bed temperature drops to very a low value thereby increasing the amount of adsorbate retained at the end of discharge process. This study clearly shows the need for improving the heat transfer rate from or to the ANG bed for higher delivery capacity.

2012 ◽  
Vol 19 ◽  
pp. 190-195 ◽  
Author(s):  
KAZI AFZALUR RAHMAN ◽  
WAI SOONG LOH ◽  
KIM CHOON NG ◽  
WONGEE CHUN

An adsorbed natural gas (ANG) storage system with internal thermal control, based on fin and tube type heat exchanger is investigated in this study. The adsorbent bed, which consists of Maxsorb III activated carbon packed in between copper fins and tubes, is demonstrated to study the storage capacity and thermal management of the ANG storage system. The cylinder is pressurized up to 35 bar and water is circulated through the tubes during charge process for quick removal of adsorption heat, thus to increase the storage capacity. Similarly, the adsorbent bed is heated up during discharge process to maximize the gas delivery. The current experimental arrangement presented shows higher storage capacity and better thermal management than the adsorbent bed without fin and tube arrangement.


2021 ◽  
Vol 2116 (1) ◽  
pp. 012085
Author(s):  
Evgeny Strizhenov ◽  
Sergey Chugaev ◽  
Ilya Men’shchikov ◽  
Andrey Shkolin ◽  
Igor Shelyakin

Abstract The study of the thermal state of the monolithic adsorbent layer and internal heat exchange processes during the circulating charging of an adsorbed natural gas storage system was carried out. The correlation between gas flow mode and the heat transfer coefficient between gas and adsorbent is determined under conditions of mass transfer.


2014 ◽  
Vol 53 (11) ◽  
pp. 4522-4523 ◽  
Author(s):  
Pradeepta K. Sahoo ◽  
Mathew John ◽  
Bharat L. Newalkar ◽  
N. V. Choudhary ◽  
K. G. Ayappa

Nanomaterials ◽  
2021 ◽  
Vol 11 (12) ◽  
pp. 3274
Author(s):  
Evgeny M. Strizhenov ◽  
Sergey S. Chugaev ◽  
Ilya E. Men’shchikov ◽  
Andrey V. Shkolin ◽  
Anatoly A. Zherdev

Adsorbed natural gas (ANG) technology is a promising alternative to traditional compressed (CNG) and liquefied (LNG) natural gas systems. Nevertheless, the energy efficiency and storage capacity of an ANG system strongly depends on the thermal management of its inner volume because of significant heat effects occurring during adsorption/desorption processes. In the present work, a prototype of a circulating charging system for an ANG storage tank filled with a monolithic nanoporous carbon adsorbent was studied experimentally under isobaric conditions (0.5–3.5 MPa) at a constant volumetric flow rate (8–18 m3/h) or flow mode (Reynolds number at the adsorber inlet from 100,000 to 220,000). The study of the thermal state of the monolithic adsorbent layer and internal heat exchange processes during the circulating charging of an adsorbed natural gas storage system was carried out. The correlation between the gas flow mode, the dynamic gas flow temperature, and the heat transfer coefficient between the gas and adsorbent was determined. A one-dimensional mathematical model of the circulating low-temperature charging process was developed, the results of which correspond to the experimental measurements.


2014 ◽  
Vol 31 (11) ◽  
pp. 1994-2002 ◽  
Author(s):  
Mahdi Khorashadizadeh ◽  
Mahdi Niknam Shahrak ◽  
Akbar Shahsavand

2011 ◽  
Vol 50 (23) ◽  
pp. 13000-13011 ◽  
Author(s):  
Pradeepta K. Sahoo ◽  
Mathew John ◽  
Bharat L. Newalkar ◽  
N. V. Choudhary ◽  
K. G. Ayappa

2016 ◽  
Vol 819 ◽  
pp. 107-110
Author(s):  
D.T. Ybyraiymkul ◽  
A. Kaltayev ◽  
Kim Choon Ng

Natural gas, from the environmental point of view, is the cleanest fuel after hydrogen. Widespread use of gaseous fuel is restricted by its storage problems in containers under high pressure (20-25 MPa) or liquefied gas at low temperatures (-163 °C). One of the most promising solutions to such problems (high pressure and low temperature) is to develop a vessel based on adsorption technology, designed for efficient storage of natural gas at relatively low pressures (3-3.5 MPa). Adsorbed natural gas (ANG) storage system provides reduction in compressor cost, tank manufacture cost and gas refueling cost (energy consumption of ANG is lower than that of compressed (CNG) and liquefied natural gas (LNG) storage systems) and improves environmental safety by transferring vehicles from gasoline to natural gas. This paper presents simulation results of charging of ANG vessel under the dynamic conditions where the heat effect is controlled by the fin and tube type heat exchanger.


2010 ◽  
Vol 24 (13) ◽  
pp. 1421-1424 ◽  
Author(s):  
WAI SOONG LOH ◽  
KAZI AFZALUR RAHMAN ◽  
KIM CHOON NG ◽  
BIDYUT BARAN SAHA ◽  
ANUTOSH CHAKRABORTY

This paper presents the adsorption isotherm experiment of Methane and Maxsorb III activated carbon that was conducted and analyzed at temperatures from 5 to 55 °C and pressures up to 2.2 MPa in a volumetric apparatus. It is a complementary to the previous efforts by ways of analyzing the importance between charging and discharging rate, temperature increase and reduce of the bed, the heat transfer process, and the cylinder cooling and heating requirements during the charging and discharging of adsorbed natural gas.


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