@article { ISI:000309370500003, title = {Carbon dioxide capture using amine functionalized silica gel}, journal = {Indian Journal of Chemistry Section A-Inorganic Bio-Inorganic Physical Theoretical \& Analytical Chemistry}, volume = {51}, number = {9-10, SI}, year = {2012}, month = {SEP}, pages = {1214-1222}, publisher = {NATL INST SCIENCE COMMUNICATION-NISCAIR}, address = {DR K S KRISHNAN MARG, PUSA CAMPUS, NEW DELHI 110 012, INDIA}, abstract = {

Commercially available silica gel is chemically modified for carbon dioxide capture. Calcinated silica gel of certain particle size functionalized with amine using two different methods, wet impregnation and grafting via silane chemistry has been employed as a porous media. The prepared material is characterized by Fourier transform infrared, scanning electron microscopy, energy dispersive analysis of X-rays, thermogravimetry and N-2 physisorption techniques. Gas uptake measurements have been carried out to ascertain the CO2 capture capacity of the amine functionalized material. The experiments have been carried out at moderate pressure and temperature range to ascertain its potential for easy scale up.

}, keywords = {Amine functionalized silica gel, Carbon dioxide capture, grafting, Poly(ethyleneimine), Silane chemistry, Wet impregnation}, issn = {0376-4710}, author = {Sakpal, Tushar and Kumar, Asheesh and Kamble, Sanjay and Kumar, Rajnish} } @article { ISI:000311935400073, title = {Influence of contact medium and surfactants on carbon dioxide clathrate hydrate kinetics}, journal = {Fuel}, volume = {105}, year = {2013}, month = {MAR}, pages = {664-671}, publisher = {ELSEVIER SCI LTD}, address = {THE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, OXON, ENGLAND}, abstract = {

Carbon dioxide (CO2) hydrate formation kinetic was investigated in a fixed bed crystallizer at constant pressure (3.55 MPa) and temperature (274 K). Porous media of three different silica gels were used, with a mesh size of 60-120, 100-200 and 230-400 having different surface area. The observed trends indicate that silica gel with larger surface area leads to higher gas consumption as well as reduces the induction time. The effect of pore diameter and particle size distribution has already been reported in a previous study [1]. In this study the effect of additives on hydrate formation kinetics were also investigated. The additives studied were nonionic surfactant Tween-80 (T-80), cationic dodecyltrimethylammonium chloride (DTACl) and anionic Sodium Dodecyl Sulphate (SDS). Out of the three surfactants used in this study, SDS was found to be most effective in enhancing the rate of hydrate formation as well as reducing the induction time. The current result shows significant improvement in water to hydrate conversion in silica gel media compared to quiescent water or surfactant-water system under similar conditions. (C) 2012 Elsevier Ltd. All rights reserved.

}, keywords = {Carbon dioxide capture, Clathrate hydrate, kinetics, Silica gel, Surfactants}, issn = {0016-2361}, doi = {10.1016/j.fuel.2012.10.031}, author = {Kumar, Asheesh and Sakpal, Tushar and Linga, Praveen and Kumar, Rajnish} } @article { ISI:000337337000035, title = {Impact of fly ash impurity on the hydrate-based gas separation process for carbon dioxide capture from a flue gas mixture}, journal = {Industrial \& Engineering Chemistry Research}, volume = {53}, number = {23}, year = {2014}, month = {JUN}, pages = {9849-9859}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

The hydrate-based gas separation (HBGS) process for gas mixtures of CO2 + N-2 (flue gas) and CO2 + H-2 (fuel gas) has proven to be very efficient and highly selective for CO2 capture. In addition to CO2 and N-2, flue gas from coal-based thermal power stations can contain impurities such as nitrogen oxides (NOx), sulfur oxides (SOx), and fly ash. In this work, the impact of fly ash on the HBGS process efficiency was investigated. Tetrahydrofuran (THF, 1 mol \%) was used as a thermodynamic promoter, and sodium dodecyl sulfate (SDS) and sodium dodecyl benzenesulfonate (SDBS) (anionic surfactants) were used as kinetic promoters. Whereas the use of THF in the HBGS process reduces the operating pressure significantly, both SDS and SDBS were found to enhance the rate of hydrate formation. It was observed that the hydrate equilibrium conditions did not change in the presence of fly ash. However, the presence of fly ash enhanced the separation efficiency of the HBGS process by reducing the induction time and increasing the kinetics of hydrate formation. Therefore, the presence of fly ash in a flue gas mixture is not detrimental to the HBGS process, which is a positive factor for the capture and geological sequestration of CO2 in the form of gas hydrates.

}, issn = {0888-5885}, doi = {10.1021/ie5001955}, author = {Kumar, Asheesh and Sakpal, Tushar and Linga, Praveen and Kumar, Rajnish} } @article { ISI:000355645000021, title = {Carbon dioxide sequestration: influence of porous media on hydrate formation kinetics}, journal = {ACS Sustainable Chemistry \& Engineering}, volume = {3}, number = {6}, year = {2015}, month = {JUN}, pages = {1205-1214}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

In the present study, CO, sequestration by hydrate formation in porous sediments has been discussed. Two siliceous materials with high porosities, pumice and fire hardened red clay (FHRC), have been used as packing materials in a fixed bed setup to study hydrate formation kinetics. The results obtained using the aforementioned materials were compared with those obtained using silica sand and quartz. Carbon dioxide hydrate formation kinetics was studied at 3.0 MPa pressure and 274 K temperature. Two different types of experiments were conducted: (a) using a constant volume of water and (b) maintaining a constant bed height. These experiments were conducted using the different porous media individually as packing materials. It was observed that pumice as the porous medium showed better hydrate formation kinetics resulting in 46 mol \% water to hydrate conversion in 5 h. Moreover, kinetics was enhanced with decrease in the bed height of pumice; this suggests that at field scale adaptation of CO, sequestration in geological formations, mass transfer limitations would be significant. The effects of particle size on hydrate formation kinetics were also investigated. It was observed that hydrate formation kinetics was enhanced with decrease in the particle size fraction.

}, keywords = {Bed height, Gas hydrate, gas uptake, Geological sequestration, Particle size}, issn = {2168-0485}, doi = {10.1021/acssuschemeng.5b00171}, author = {Bhattacharjee, Gaurav and Kumar, Asheesh and Sakpal, Tushar and Kumar, Rajnish} } @article {43037, title = {Enhanced carbon dioxide hydrate formation kinetics in a fixed bed reactor filled with metallic packing}, journal = {Chemical Engineering Science}, volume = {122}, year = {2015}, month = {JAN}, pages = {78-85}, doi = {10.1016/j.ces.2014.09.019}, author = {Kumar, Asheesh and Sakpal, Tushar and Linga, Praveen and Kumar, Rajnish} } @article { ISI:000357869100005, title = {Influence of low-dosage hydrate inhibitors on methane clathrate hydrate formation and dissociation kinetics}, journal = {Energy Technology}, volume = {3}, number = {7, SI}, year = {2015}, month = {JUL}, pages = {717-725}, publisher = {WILEY-V C H VERLAG GMBH}, address = {BOSCHSTRASSE 12, D-69469 WEINHEIM, GERMANY}, abstract = {

This work investigates the effect of low-dosage hydrate inhibitors (LDHIs) on methane hydrate formation and dissociation. The hydrate inhibitors used in this study were the sodium salt of polyacrylic acid, a polysaccharide chitosan, and the linear sulfated polysaccharide i-carrageenan; the inhibiting behavior of these additives were compared with that of the commonly used hydrate inhibitor polyvinylpyrrolidone for methane hydrate formation. A LDHI concentration of 1wt\% was found to increase the induction time relative to that at a LDHI concentration of 0.1wt\%. Chitosan was found to be better than the others in reducing nucleation and the growth rate of the hydrate at a concentration of 1wt\%. At a lower concentration of 0.1wt\%, nucleation inhibition was minimal, however, growth inhibition was significant. The effect of these inhibitors on the decomposition rate of the hydrate was also studied, and the decomposition kinetics at a constant driving force in excess of three-phase equilibrium is reported.

}, keywords = {gas uptake, hydrates, inhibitors, kinetics, thermal stimulation}, issn = {2194-4288}, doi = {10.1002/ente.201500004}, author = {Kumar, Asheesh and Sakpal, Tushar and Kumar, Rajnish} } @article { ISI:000359067400013, title = {Methane hydrate formation in a test sediment of sand and clay at various levels of water saturation}, journal = {Canadian Journal of Chemistry}, volume = {93}, number = {8, 1, SI}, year = {2015}, month = {AUG}, pages = {874-881}, publisher = {CANADIAN SCIENCE PUBLISHING, NRC RESEARCH PRESS}, address = {65 AURIGA DR, SUITE 203, OTTAWA, ON K2E 7W6, CANADA}, abstract = {

Kinetics of methane hydrate formation with different ratios of silica sand and clay and different water saturations were studied. At suitable temperature and methane gas pressure, water in the void spaces of silica sand packing and intercalated area of clay were converted into hydrate. It was observed that the rate of hydrate formation increases with higher void space in the packing, and addition of clay in test sediment decreases water to hydrate conversion as well as rate of hydrate formation. Maximum water to hydrate conversion of 60.0\% was achieved in pure silica sand bed at 75\% water saturation. Presence of fine clay particles is expected to reduce the void spaces and thus may hinder effective mass transfer of hydrate forming gases in the bed. However, it is also possible that the bentonite clay used in this work may actually inhibit hydrate growth. Additional experiments in stirred tank reactor were carried out to understand the inhibiting effect of bentonite clay for hydrate formation.

}, keywords = {clay, formation kinetics, methane hydrate, Silica sand, water saturation}, issn = {0008-4042}, doi = {10.1139/cjc-2014-0537}, author = {Kumar, Asheesh and Sakpal, Tushar and Roy, Sudip and Kumar, Rajnish} } @article { ISI:000360026900051, title = {Role of metallic packing and kinetic promoter in designing a hydrate-based gas separation process}, journal = {Energy \& Fuels}, volume = {29}, number = {7}, year = {2015}, note = {2nd International Conference Biogas Science, Vienna, AUSTRIA, 2014}, month = {JUL}, pages = {4463-4471}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

In the present work, kinetics of the hydrate-based gas separation (HBGS) process has been studied employing an unstirred reactor configuration. Gas uptake measurements were carried out for studying hydrate formation kinetics and final water to hydrate conversion using fuel gas mixtures (mixture 1, 40.4\% CO2 + 59.6\% H-2; mixture 2, 40.9\% CO2 + 58.05\% H-2 + 1.05\% H2S). Silica sand and stainless-steel-structured packing (SSP) were used as contact media in the presence of an anionic surfactant sodium dodecyl sulfate (SDS) as a kinetic promoter. Experiments were conducted with three different concentrations of SDS in water to enhance hydrate formation kinetics. On the basis of induction time and rate of hydrate growth, 1 wt \% SDS was determined to be the best concentration for carbon dioxide capture at 7.0 MPa and 273.65 K from the CO2 + H-2 gas mixture. In comparison to silica sand packing, use of SSP was found to improve the final water to hydrate conversion (71.0 +/- 4.1\%). The addition of H2S impurity in the fuel gas mixture was also found to enhance the rate of hydrate formation in the presence of SDS at 7.8 MPa and 274.5 K. On the basis of the experimental results and our previous studies on separation efficiency, a continuous HBGS process is proposed to separate CO2 and produce CO2- and H2S-free H-2 stream from a fuel gas mixture.

}, issn = {0887-0624}, doi = {10.1021/acs.energyfuels.5b00664}, author = {Kumar, Asheesh and Kumar, Rajnish} } @article { ISI:000366878100001, title = {Role of surfactants in promoting gas hydrate formation}, journal = {Industrial \& Engineering Chemistry Research}, volume = {54}, number = {49}, year = {2015}, month = {DEC}, pages = {12217-12232}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

Gas hydrates have been proposed as a potential technology for a number of applications, such as separation of gas mixtures, CO2 capture, transportation, and sequestration, methane storage and transport, and seawater desalination. Most of these applications will benefit from reduced induction time of hydrate nucleation, enhanced hydrate growth rate, and maximum water-to-hydrate conversion. The addition of surfactants to the gas-water system serves this purpose in a very effective manner. This review focuses on different surfactants that were utilized for gas hydrate formation studies; insights have been provided on the possible mechanisms of action through which these surfactants affect hydrate formation kinetics. A thorough analysis of the existing literature on surfactants suggests that enhanced rate of hydrate nucleation and growth kinetics may not be directly linked to micelle formation. Conversely, reduced surface tension in the presence of surfactants not only enhances the mass transfer but also changes the morphology of hydrate formation, which in turn enhances gas-water interactions for faster hydrate growth rate.

}, issn = {0888-5885}, doi = {10.1021/acs.iecr.5b03476}, author = {Kumar, Asheesh and Bhattacharjee, Gaurav and Kulkarni, B. D. and Kumar, Rajnish} } @article { ISI:000377466600023, title = {Crystallization kinetics for carbon dioxide gas hydrate in fixed bed and stirred tank reactor}, journal = {Korean Journal of Chemical Engineering}, volume = {33}, number = {6}, year = {2016}, month = {JUN}, pages = {1922-1930}, publisher = {KOREAN INSTITUTE CHEMICAL ENGINEERS}, address = {F.5, 119, ANAM-RO, SEONGBUK-GU, SEOUL 136-075, SOUTH KOREA}, abstract = {

The phase change from germ nuclei to growth nuclei and subsequent volume transformation in a crystallization process was modeled by Avrami equations. The phase change during the hydrate formation was fitted with the classical Avrami model by utilizing gas uptake data. The idea is to understand the difference in growth behavior of hydrate crystals when in small pores compared to a stirred tank reactor which does not pose any physical restrictions to hydrate growth. The parameters n and k of the Avrami equation were determined explicitly for CO2 hydrate formation.

}, keywords = {Avrami Equation, CO2 Capture \& Sequestration, Fixed Bed, Gas hydrates, kinetics}, issn = {0256-1115}, doi = {10.1007/s11814-016-0040-7}, author = {Kumar, Asheesh and Khatri, Dishant and Lee, Ju Dong and Kumar, Rajnish} } @article {43437, title = {Effect of additives on formation and decomposition kinetics of methane clathrate hydrates: application in energy storage and transportation}, journal = {Canadian Journal of Chemical Engineering}, volume = {94}, year = {2016}, month = {NOV}, pages = {2160-2167}, abstract = {Methane gas storage and transportation via clathrate hydrates is proposed to be a potential solution for large-scale energy storage. In this work, we study the formation and decomposition kinetics of methane hydrates (MH) in a laboratory-scale unstirred crystallizer. The present investigation demonstrates comparative studies of hydrate formation and dissociation kinetics in the presence of tetrahydrofuran (55.6 and 27.8mmol/mol, 5.56 and 2.78mol\% THF) and sodium dodecyl sulphate (1mg/g, 0.1wt\% SDS). Moreover, the storage capacity and hydrate formation kinetics in both the systems are discussed. In a recent work, enhanced methane hydrate growth in the presence of THF at close to atmospheric conditions was demonstrated. The emphasis of the current work is to study the stability of hydrates to understand dissociation kinetics by measuring the rate of hydrate decomposition at different temperatures. Hydrate stability measurements were performed at -8, -3, 2, 10, and 20 degrees C to study the decomposition rates of MH and self-preservation in presence of the two additives THF and SDS.}, doi = {10.1002/cjce.22583}, author = {Kumar, Asheesh and Kushwaha, Omkar Singh and Rangsunvigit, Pramoch and Linga, Praveen and Kumar, Rajnish} } @article { ISI:000367235100139, title = {Effect of different fixed bed media on the performance of sodium dodecyl sulfate for hydrate based CO2 capture}, journal = {Materials \& Design}, volume = {90}, year = {2016}, month = {JAN}, pages = {1186-1191}, publisher = {ELSEVIER SCI LTD}, address = {THE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, OXON, ENGLAND}, abstract = {

Sodium Dodecyl Sulfate (SDS) is used as a kinetic promoter in gas hydrate formation. In this work, the performance of SDS for carbon dioxide gas hydrate formation in two different fixed bed media: silica sand and zeolite (5A and 13X) has been evaluated. The concentration of SDS was fixed at 0.5 wt\%. The experiments were carried out in batch mode with the initial pressure fixed at 3.0 MPa, and the temperature kept constant at 274.65 K. The results showed that hydrate of carbon dioxide with fixed bed of silica sand was significantly promoted by the addition of SDS as compared to the other fixed bed medium used in this study: zeolite 13X. (c) 2015 Elsevier Ltd. All rights reserved.

}, keywords = {Carbon dioxide, Fixed bed media, Hydrate formation, Kinetic promoter, Silica sand, Zeolite 5A and 13X}, issn = {0261-3069}, doi = {10.1016/j.matdes.2015.06.049}, author = {Arora, Amit and Kumar, Asheesh and Bhattacharjee, Gaurav and Kumar, Pushpendra and Balomajumder, Chandrajit} } @article {45648, title = {Effect of the amino acid L-histidine on methane hydrate growth kinetics}, journal = {Journal of Natural Gas Science and Engineering}, volume = {35}, year = {2016}, month = {SEP}, pages = {1453-1462}, type = {Article}, abstract = {

In the present study, the effect of a polar amino acid, L-histidine on methane hydrate growth kinetics has been investigated. Methane hydrate formation experiments were carried out in a stirred tank reactor setup at pressure and temperature conditions of 274.15 K and 5.0 MPa respectively. Two different concentrations (0.1 and 1 wt \%) of L-histidine were studied. Hydrate growth through molecular dynamic (MD) simulation was also studied; pressure and temperature conditions for the simulations were set at 10.0 MPa and 270.0 K, while the concentration of L-histidine was kept fixed at 0.94 wt \%. Hydrate formation runs using MD simulation were carried out with optimal concentration of methane in water. The presence of L-histidine in the system was found to significantly enhance methane hydrate growth kinetics as compared to pure water for both experimental and MD simulation runs. Final gas consumption with 1 wt \% L-histidine was found to be comparable to that with 1 wt \% SDS, the most commonly used additive for hydrate promotion studies. L-histidine is a benign additive which offers considerable enhancement in methane hydrate formation kinetics and can be utilized for various hydrate based technologies such as methane storage and transport. (C) 2016 Elsevier B.V. All rights reserved.

}, keywords = {Amino acid, Crystal growth, Gas hydrate, kinetics, Molecular dynamic simulation}, issn = {1875-5100}, doi = {10.1016/j.jngse.2016.05.052}, author = {Bhattacharjee, Gaurav and Choudhary, Nilesh and Kumar, Asheesh and Chakrabarty, Suman and Kumar, Rajnish} } @article {43401, title = {Experimental investigation to elucidate why tetrahydrofuran rapidly promotes methane hydrate formation kinetics: applicable to energy storage}, journal = {Journal of Physical Chemistry C}, volume = {120}, year = {2016}, month = {DEC}, pages = {29062-29068}, abstract = {Methane storage as SNG (solidified natural gas) in the form of clathrate hydrates is an emerging, economically feasible and environmentally benign technology for large scale storage. Mixed tetrahydrofuran (THF)-methane (CH4) hydrates offer a paradigm shift to milder storage conditions and faster hydrate formation kinetics, providing a promising scenario to scale up the SNG technology. In this work, we synthesize mixed THF-CH4 hydrates in a high pressure microdifferential scanning calorimeter (HP mu-DSC) to elucidate the two-step hydrate formation mechanism of mixed THF-CH4 hydrate identifying the synergism between THF and CH4. Heat flow change during hydrate formation and dissociation of mixed THF-CH4 hydrates formed in the presence of 5.56 mol \% THF (stoichiometric composition) were monitored. The two step-mechanism of mixed THF-CH4 hydrate formation was further confirmed by the pressure-temperature profile and visual observations with a sample volume scale -up of about 350 times that of mu-DSC experiments.}, doi = {10.1021/acs.jpcc.6b11995}, author = {Kumar, Asheesh and Daraboina, Nagu and Kumar, Rajnish and Linga, Praveen} } @article { ISI:000380735100016, title = {Impact of H2S impurity on carbon dioxide hydrate formation kinetics in fixed bed arrangements}, journal = {Industrial \& Engineering Chemistry Research}, volume = {55}, number = {29}, year = {2016}, note = {13th International Conference on Carbon Dioxide Utilization (ICCDU), Singapore, SINGAPORE, JUL 05-09, 2015}, month = {JUL}, pages = {7964-7972}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

In the present work, a combination of silica sand and metallic sheets as a fixed bed media was used for carbon dioxide hydrate formation studies. Two metallic sheets, aluminum and brass, were incorporated into the fixed bed of silica sand to enhance heat transfer properties of the bed. The results obtained from this arrangement of metal sheets were compared with those obtained with a pure silica sand system. Both brass and aluminum systems were found to be good candidates to enhance gas hydrate formation kinetics compared to simply a sand system. Production of fuel gas from coal often contains a toxic gas, hydrogen sulfide (H2S). For the first time, the effect of H2S on the formation kinetics of CO2 + H-2 + H2S hydrates has been studied. It was observed that the presence of H2S does not affect the hydrate formation kinetics and total gas uptake in the presence of H2S is either as good as CO2 + H-2 hydrate or better. However, H2S impurity in the fuel gas mixture shows a corrosive effect on silica sand media.

}, issn = {0888-5885}, doi = {10.1021/acs.iecr.5b04079}, author = {Kumar, Asheesh and Sakpal, Tushar and Bhattacharjee, Gaurav and Kumar, Anupam and Kumar, Rajnish} } @article {43738, title = {Effects of micellization on growth kinetics of methane hydrate}, journal = {Industrial \& Engineering Chemistry Research}, volume = {56}, year = {2017}, month = {APR}, pages = {3687-3698}, type = {Article}, abstract = {Surfactants are Specific functional materials, that form various types of self-assemblies and affect local water ordering alongside solution properties. Such surface active agents are used extensively in gas hydrate based applications as kinetic hydrate promoters. To understand the effect of surfactant micelles on hydrate formation kinetics, a novel surfactant system capable of producing micelles at hydrate forming temperature was developed. The presence of surfactant micelles in this new system (a combination of anionic surfactant SDS and zwitterionic surfactant CAPB) was determined through DLS measurements. Pure methane and a coal bed methane mixture were individually used to assess the efficacy of the surfactant mixture for hydrate formation. This study conclusively proves for the first time that the presence of surfactant micelles enhances hydrate formation kinetics. The findings reported here can contribute significantly toward improving the utility of surfactants in gas hydrate based technological applications such as gas separation and methane storage.}, doi = {10.1021/acs.iecr.7b00328}, author = {Bhattacharjee, Gaurav and Kushwaha, Omkar Singh and Kumar, Asheesh and Khan, Muzammil Yusuf and Patel, Jay Narayan and Kumar, Rajnish} } @article {47049, title = {Hydrate-based carbon capture process: assessment of various packed bed systems for boosted kinetics of hydrate formation}, journal = {Journal of Energy Resources Technology-Transactions of the ASME}, volume = {143}, year = {2021}, month = {MAR }, pages = {033005}, type = {Article}, abstract = {

The case for developing novel technologies for carbon dioxide (CO2) capture is fast gaining traction owing to increasing levels of anthropogenic CO2 being emitted into the atmosphere. Here, we have studied the hydrate-based carbon dioxide capture and separation process from a fundamental viewpoint by exploring the use of various packed bed media to enhance the kinetics of hydrate formation using pure CO2 as the hydrate former. We established the fixed bed reactor (FBR) configuration as a superior option over the commonly used stirred tank reactor (STR) setups typically used for hydrate formation studies by showing enhanced hydrate formation kinetics using the former. For the various packing material studied, we have observed silica gel with 100 nm pore size to return the best kinetic performance, corresponding to a water to hydrate conversion of 28 mol\% for 3 h of hydrate growth. The fundamental results obtained in the present study set up a solid foundation for follow-up works with a more applied perspective and should be of interest to researchers working in the carbon dioxide capture and storage and gas hydrate fields alike.

}, keywords = {air emissions from fossil fuel combustion, Carbon dioxide capture, combustion of waste, Fixed bed reactor, fuel combustion, Gas hydrate, hydrates, kinetics, Silica gel}, issn = {0195-0738}, doi = {10.1115/1.4048304}, author = {Arora, Amit and Kumar, Asheesh and Bhattacharjee, Gaurav and Balomajumder, Chandrajit and Kumar, Pushpendra} }