Heat and Mass Transfer in an Adsorbed Natural Gas Storage System Filled with Monolithic Carbon Adsorbent during Circulating Gas Charging

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 he...

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Published inNanomaterials (Basel, Switzerland) Vol. 11; no. 12; p. 3274
Main Authors Strizhenov, Evgeny M, Chugaev, Sergey S, Men'shchikov, Ilya E, Shkolin, Andrey V, Zherdev, Anatoly A
Format Journal Article
LanguageEnglish
Published Switzerland MDPI AG 02.12.2021
MDPI
Subjects
Activated carbon
adsorbed natural gas
Adsorbents
Adsorption
Carbon
Charging
circulating charging
Efficiency
Energy efficiency
Energy storage
Flow rates
Flow velocity
Fluid dynamics
Fluid flow
Gas flow
Heat conductivity
Heat exchange
Heat exchangers
Heat transfer
Heat transfer coefficients
High temperature effects
Liquefied natural gas
Low temperature
Mass transfer
Mathematical models
methane storage
Methods
monolithic adsorbent
nanoporous carbon
Natural gas
Reynolds number
Storage capacity
Storage tanks
Thermal management
nanoporous carbon
adsorption
methane storage
monolithic adsorbent
circulating charging
adsorbed natural gas
heat and mass transfer
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Abstract 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 m /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.
AbstractList 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.
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 m 3 /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.
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 m /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.
Author Strizhenov, Evgeny M
Chugaev, Sergey S
Men'shchikov, Ilya E
Shkolin, Andrey V
Zherdev, Anatoly A
AuthorAffiliation 1 Research Institute of Power Engineering, Bauman Moscow State Technical University, ul. Baumanskaya 2-ya, 5, 105005 Moscow, Russia; chugaev@bmstu.ru (S.S.C.); i.menshchikov@gmail.com (I.E.M.); shkolin@bk.ru (A.V.S.); azherdev@bmstu.ru (A.A.Z.)
2 Frumkin Institute of Physical Chemistry and Electrochemistry, Russian Academy of Sciences, Leninskii Prospect, 31, bld. 4, 119071 Moscow, Russia
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– name: 2 Frumkin Institute of Physical Chemistry and Electrochemistry, Russian Academy of Sciences, Leninskii Prospect, 31, bld. 4, 119071 Moscow, Russia
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BackLink https://www.ncbi.nlm.nih.gov/pubmed/34947623$$D View this record in MEDLINE/PubMed
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Issue 12
Keywords nanoporous carbon
adsorption
methane storage
monolithic adsorbent
circulating charging
adsorbed natural gas
heat and mass transfer
Language English
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Snippet Adsorbed natural gas (ANG) technology is a promising alternative to traditional compressed (CNG) and liquefied (LNG) natural gas systems. Nevertheless, the...
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SubjectTerms Activated carbon
adsorbed natural gas
Adsorbents
Adsorption
Carbon
Charging
circulating charging
Efficiency
Energy efficiency
Energy storage
Flow rates
Flow velocity
Fluid dynamics
Fluid flow
Gas flow
Heat conductivity
Heat exchange
Heat exchangers
Heat transfer
Heat transfer coefficients
High temperature effects
Liquefied natural gas
Low temperature
Mass transfer
Mathematical models
methane storage
Methods
monolithic adsorbent
nanoporous carbon
Natural gas
Reynolds number
Storage capacity
Storage tanks
Thermal management
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Title Heat and Mass Transfer in an Adsorbed Natural Gas Storage System Filled with Monolithic Carbon Adsorbent during Circulating Gas Charging
URI https://www.ncbi.nlm.nih.gov/pubmed/34947623
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