1
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Mok J, Park M, Choi W, Kang KC, Lee S, Lee JD, Seo Y. Investigation of theoretical maximum water yield and efficiency-optimized temperature for cyclopentane hydrate-based desalination. WATER RESEARCH 2023; 246:120707. [PMID: 37827038 DOI: 10.1016/j.watres.2023.120707] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 06/23/2023] [Revised: 09/20/2023] [Accepted: 10/06/2023] [Indexed: 10/14/2023]
Abstract
Hydrate-based desalination (HBD) shows promise as a freshwater production technology for saline water. Liquid-phase hydrate formers, with their ability to facilitate hydrate formation at atmospheric pressure, have gained attention for their high energy efficiency in HBD. This study explored cyclopentane (CP) HBD by experimentally measuring the thermodynamic properties of CP hydrate in saline solutions and developing a theoretical framework to estimate the water yield of CP HBD under various operating conditions. The measured dissociation enthalpy of CP hydrate was found to be 12 % and 22 % lower compared to those of propane and R134a hydrates, respectively. The equilibrium dissociation temperatures of CP hydrate at different NaCl concentrations under atmospheric pressure were experimentally measured and then predicted using the Hu-Lee-Sum correlation. The theoretically achievable maximum salinity and water yield for CP HBD were calculated in the temperature range of 268-280 K and the initial salinity range of 0-8 wt.%. Additionally, the concept of HBD heat efficiency, representing the maximum amount of pure water producible per unit of heat, was introduced to identify an optimal operating condition for the HBD process. Efficiency-maximized temperatures, where the HBD heat efficiency reached its peaks, were determined for various initial salinities in the process, for example, 273.4 K for NaCl 3.5 wt.% solution. This novel approach provides invaluable guidance for determining the most energy-efficient operating conditions in the HBD process and establishes a solid foundation for further advancements in this field.
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Affiliation(s)
- Junghoon Mok
- Department of Civil, Urban, Earth, and Environmental Engineering, Ulsan National Institute of Science and Technology, Ulsan 44919, Republic of Korea; Department of Chemical and Biological Engineering, Colorado School of Mines, CO 80401, USA
| | - Minseo Park
- Graduate School of Carbon Neutrality, Ulsan National Institute of Science and Technology, Ulsan 44919, Republic of Korea
| | - Wonjung Choi
- Department of Chemical Engineering, Changwon National University, Gyeongsangnam-do 51140, Republic of Korea
| | - Kyung Chan Kang
- Offshore Plant Resources R&D Center, Korea Institute of Industrial Technology, Busan 46744, Republic of Korea
| | - Seungmin Lee
- Offshore Plant Resources R&D Center, Korea Institute of Industrial Technology, Busan 46744, Republic of Korea
| | - Ju Dong Lee
- Offshore Plant Resources R&D Center, Korea Institute of Industrial Technology, Busan 46744, Republic of Korea
| | - Yongwon Seo
- Department of Civil, Urban, Earth, and Environmental Engineering, Ulsan National Institute of Science and Technology, Ulsan 44919, Republic of Korea; Graduate School of Carbon Neutrality, Ulsan National Institute of Science and Technology, Ulsan 44919, Republic of Korea.
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2
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Ezure R, Arai Y, Nakano D, Komatsu H, Tajima H. Novel SF6 gas concentration method using hydrate-based gas uptake and sweating process. Sep Purif Technol 2023. [DOI: 10.1016/j.seppur.2022.122441] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
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3
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Wu G, Coulon F, Feng JC, Yang Z, Jiang Y, Zhang R. Machine learning models for fast selection of amino acids as green thermodynamic inhibitors for natural gas hydrate. J Mol Liq 2022. [DOI: 10.1016/j.molliq.2022.120952] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/03/2022]
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4
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Wang P, Wang J, Xu K, Lin Y, Shi Q, Li T, Fu Y, Zhang Z, Wu J. Mechanical Stability of Fluorinated-Methane Clathrate Hydrates. J Mol Liq 2022. [DOI: 10.1016/j.molliq.2022.119553] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/01/2022]
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5
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Zhang G, Li J, Liu G, Yang H, Huang H. Applicability research of thermodynamic models of gas hydrate phase equilibrium based on different equations of state. RSC Adv 2022; 12:15870-15884. [PMID: 35685713 PMCID: PMC9133728 DOI: 10.1039/d2ra00875k] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Abstract] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 02/10/2022] [Accepted: 04/27/2022] [Indexed: 11/21/2022] Open
Abstract
Choosing an appropriate equation of state and thermodynamic model is very important for predicting the phase equilibrium of a gas hydrate. This study is based on statistical thermodynamics, considering the changes in water activity caused by gas dissolution, and deriving and summarizing four thermodynamic models. Based on the 150 collected experimental data points, the accuracy of the four thermodynamic models in predicting the phase equilibrium of methane hydrate, ethane hydrate, and carbon dioxide hydrate were compared. In addition, the influence of five equations of state on each thermodynamic model's phase equilibrium prediction accuracy is compared. The analysis results show that in the temperature range of 273.40–290.15 K, the Chen–Guo model is better than other thermodynamic models in predicting the phase equilibrium of methane hydrate by using the Patel–Teja equation of state. However, in the temperature range of 290.15–303.48 K, the John–Holder model predicts that the phase equilibrium of methane hydrate will perform better. In the temperature range of 273.44–283.09 K, the John–Holder model uses the Peng–Robinson state to predict the phase equilibrium of carbon dioxide hydrate with the highest accuracy. In the temperature range of 273.68 K to 287.6 K, the Chen–Guo model is selected to predict the phase equilibrium of ethane hydrate with the highest accuracy. However, as the temperature increases, the predicted values of the vdW–P model and the Parrish–Prausnitz model deviate further from the experimental values. Based on the 150 collected experimental data points, the accuracy of the four thermodynamic models in predicting the phase equilibrium of the gas hydrate was compared.![]()
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Affiliation(s)
- Geng Zhang
- China University of Petroleum-Beijing Beijing 102249 China
| | - Jun Li
- China University of Petroleum-Beijing Beijing 102249 China .,China University of Petroleum-Beijing at Karamay Karamay 834000 China
| | - Gonghui Liu
- China University of Petroleum-Beijing Beijing 102249 China
| | - Hongwei Yang
- China University of Petroleum-Beijing Beijing 102249 China
| | - Honglin Huang
- China University of Petroleum-Beijing Beijing 102249 China
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6
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Nasir Q, Suleman H, Ud Din I, Elfadol YE. A multi-layer perceptron neural network model for predicting the hydrate equilibrium conditions in multi-component hydrocarbon systems. Neural Comput Appl 2022. [DOI: 10.1007/s00521-022-07284-4] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
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7
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Li C. Twin Support Vector Regression for Prediction of Natural Gas Hydrate Formation Conditions. Ind Eng Chem Res 2021. [DOI: 10.1021/acs.iecr.1c03534] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
- Changzhou Li
- School of Mathematics, Jilin University, Changchun 130012, China
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8
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Doubra P, Hassanalizadeh R, Naidoo P, Ramjugernath D. Thermodynamic measurement and modeling of hydrate dissociation for
CO
2
/refrigerant + sucrose/fructose/glucose solutions. AIChE J 2021. [DOI: 10.1002/aic.17379] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Affiliation(s)
- Parisa Doubra
- Thermodynamics Research Unit, School of Engineering University of KwaZulu‐Natal Durban South Africa
| | - Rasoul Hassanalizadeh
- Thermodynamics Research Unit, School of Engineering University of KwaZulu‐Natal Durban South Africa
| | - Paramespri Naidoo
- Thermodynamics Research Unit, School of Engineering University of KwaZulu‐Natal Durban South Africa
| | - Deresh Ramjugernath
- Thermodynamics Research Unit, School of Engineering University of KwaZulu‐Natal Durban South Africa
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9
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Molecular dynamics simulation of the formation of methane hydrates in the presence of KHIs. Chem Eng Sci 2021. [DOI: 10.1016/j.ces.2021.116508] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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10
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Mok J, Choi W, Seo Y. Evaluation of kinetic salt-enrichment behavior and separation performance of HFC-152a hydrate-based desalination using an experimental measurement and a thermodynamic correlation. WATER RESEARCH 2021; 193:116882. [PMID: 33550169 DOI: 10.1016/j.watres.2021.116882] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 09/18/2020] [Revised: 01/06/2021] [Accepted: 01/25/2021] [Indexed: 06/12/2023]
Abstract
Hydrate-based desalination (HBD), a type of freezing-based desalination, can concentrate salts of saline water and produce fresh water via hydrate crystal formation. In this study, the thermodynamic stability, crystallographic information, and kinetic growth behavior of HFC-152a hydrate were investigated to estimate the desalination efficiency of HBD. The phase equilibria revealed that the HFC-152a hydrate could be formed at a higher temperature in the presence of NaCl (0 wt%, 3.5 wt%, and 8.0 wt%) than the HFC-134a hydrate at 0.3 MPa. The hydration number of the HFC-152a hydrate (sI) was found to be 7.74 through the Rietveld refinement of the powder X-ray diffraction patterns, and it was also used to determine the dissociation enthalpy of the HFC-152a hydrate. The Hu-Lee-Sum correlation was employed to predict the equilibrium shift and hydrate depression temperature of both HFC-152a and HFC-134a hydrates in the presence of NaCl. Faster hydrate growth kinetics and higher hydrate conversion were observed for the HFC-152a hydrate in saline solutions despite the smaller initial driving force at 0.3 MPa and the subcooling temperature of 3 K. Additionally, to quantify the desalination efficiency of the HFC-152a HBD, the maximum achievable salinity and maximum water yield were examined using the HLS correlation. The salt-enrichment efficiency decreased with an increase in the initial salinity and increased with increasing the subcooling. The overall results indicate that HFC-152a is, potentially, a superior candidate for HBD. The novel approach examined in this study will be useful for assessing the desalination efficiency of the HBD process.
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Affiliation(s)
- Junghoon Mok
- Department of Urban and Environmental Engineering, Ulsan National Institute of Science and Technology, Ulsan 44919, Republic of Korea
| | - Wonjung Choi
- Department of Urban and Environmental Engineering, Ulsan National Institute of Science and Technology, Ulsan 44919, Republic of Korea
| | - Yongwon Seo
- Department of Urban and Environmental Engineering, Ulsan National Institute of Science and Technology, Ulsan 44919, Republic of Korea.
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11
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Kummamuru NB, Perreault P, Lenaerts S. A New Generalized Empirical Correlation for Predicting Methane Hydrate Equilibrium Conditions in Pure Water. Ind Eng Chem Res 2021. [DOI: 10.1021/acs.iecr.0c05833] [Citation(s) in RCA: 7] [Impact Index Per Article: 2.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Nithin B. Kummamuru
- Sustainable Energy Air & Water Technology (DuEL), Department of Bioscience Engineering, University of Antwerp, Groenenborgerlaan 171, Antwerpen 2020, Belgium
| | - Patrice Perreault
- Faculty of Science, Instituut voor Milieu & Duurzame Ontwikkeling (IMDO), University of Antwerp, Campus Groenenborger, Building V.612, Groenenborgerlaan 171, Antwerpen 2020, Belgium
- University of Antwerp, BlueApp, Middelheimlaan 1, Antwerpen 2020, Belgium
| | - Silvia Lenaerts
- Sustainable Energy Air & Water Technology (DuEL), Department of Bioscience Engineering, University of Antwerp, Groenenborgerlaan 171, Antwerpen 2020, Belgium
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12
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Bai J, Cheng C, Wei Y, Yan K, Li P, Fang S, Chang C. Thermodynamic investigation of hydrate-based CO 2 capture from simulated flue gas with new mixed promoters. INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING 2021. [DOI: 10.1515/ijcre-2020-0147] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
Abstract
Abstract
CO2 hydrate-based desalination (CHBD) has been developing for decades to meet the global demands of decreasing carbon dioxide (CO2) emissions. In this work, the CO2 was captured from the simulated flue gas which consists of 18.30 mol% carbon dioxide and 81.70 mol% nitrogen in the presence of tetra-n-butyl ammonium bromide (TBAB) + cyclopentane (CP) + glucoamylase. Then the phase equilibrium data of CO2 hydrate were measured by the method of isochoric pressure-search. Among the seven cases with same concentration of TBAB (0.29 mol%) and CP (5.00 vol%) and different glucoamylase proportions (ranging from 0.00 to 20.00 wt%), the optimum concentration of glucoamylase in the mixed promoters was 3.00 wt%. The phase equilibrium data was calculated by the modified van der Waals–Platteeuw (vdW–P) model with a modification of vapor pressure of water in the empty hydrate lattice. The Peng–Robinson equation of state was used to calculate the fugacity of gas. The maximum average absolute deviation was 4.09% between the calculated results and the experimental results. It revealed that the calculated results were in good agreement with the experimental results.
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Affiliation(s)
- Jing Bai
- School of Mechanical and Power Engineering , Zhengzhou University , Zhengzhou 450001 , China
- Henan Key Laboratory of Green Manufacturing of Biobased Chemicals , Puyang 457000 , China
- Henan Outstanding Foreign Scientists’ Workroom , Zhengzhou 450001 , China
- Engineering Laboratory of Henan Province for Biorefinery Technology and Equipment , Zhengzhou 450001 , China
| | - Canwei Cheng
- School of Mechanical and Power Engineering , Zhengzhou University , Zhengzhou 450001 , China
- Henan Outstanding Foreign Scientists’ Workroom , Zhengzhou 450001 , China
| | - Yuanxia Wei
- School of Mechanical and Power Engineering , Zhengzhou University , Zhengzhou 450001 , China
- Henan Outstanding Foreign Scientists’ Workroom , Zhengzhou 450001 , China
| | - Kele Yan
- School of Mechanical and Power Engineering , Zhengzhou University , Zhengzhou 450001 , China
| | - Pan Li
- School of Mechanical and Power Engineering , Zhengzhou University , Zhengzhou 450001 , China
- Henan Key Laboratory of Green Manufacturing of Biobased Chemicals , Puyang 457000 , China
- Henan Outstanding Foreign Scientists’ Workroom , Zhengzhou 450001 , China
- Engineering Laboratory of Henan Province for Biorefinery Technology and Equipment , Zhengzhou 450001 , China
| | - Shuqi Fang
- School of Mechanical and Power Engineering , Zhengzhou University , Zhengzhou 450001 , China
- Henan Outstanding Foreign Scientists’ Workroom , Zhengzhou 450001 , China
- Engineering Laboratory of Henan Province for Biorefinery Technology and Equipment , Zhengzhou 450001 , China
| | - Chun Chang
- School of Mechanical and Power Engineering , Zhengzhou University , Zhengzhou 450001 , China
- Henan Key Laboratory of Green Manufacturing of Biobased Chemicals , Puyang 457000 , China
- Henan Outstanding Foreign Scientists’ Workroom , Zhengzhou 450001 , China
- Engineering Laboratory of Henan Province for Biorefinery Technology and Equipment , Zhengzhou 450001 , China
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13
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Promoting and Inhibitory Effects of Hydrophilic/Hydrophobic Modified Aluminum Oxide Nanoparticles on Carbon Dioxide Hydrate Formation. ENERGIES 2020. [DOI: 10.3390/en13205380] [Citation(s) in RCA: 5] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
Abstract
Hydrate-based CO2 capture from large emission sources is considered a promising process for greenhouse gas mitigation. The addition of nanoparticles may promote or inhibit the formation of hydrates. In this work, CO2 hydrate formation experiments were performed in a dual-cell high-pressure reactor. Non-modified, hydrophilic modified and hydrophobic modified aluminum oxide (Al2O3) nanoparticles at different concentrations were added to assess their promoting or inhibitory effects on CO2 hydrate formation. The equilibrium temperature and pressure, induction time, and total gas consumption during CO2 hydrate formation were measured. The results show that the presence of Al2O3 nanoparticles exerts little effect on the phase equilibrium of CO2 hydrates. Under the experimental conditions, the addition of all Al2O3 nanoparticles imposes an inhibitory effect on the final gas consumption except for the 0.01 wt% addition of hydrophilic modified Al2O3 nanoparticles. The induction time required for the nucleation of CO2 hydrates mainly ranges from 70 to 90 min in the presence of Al2O3 nanoparticles. Compared to the absence of nanoparticles, the addition of non-modified and hydrophilic modified Al2O3 nanoparticle reduces the induction time. However, the hydrophobic modified Al2O3 nanoparticles extend the induction time.
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14
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Experimental study and kinetic modeling of R410a hydrate formation in presence of SDS, tween 20, and graphene oxide nanosheets with application in cold storage. J Mol Liq 2020. [DOI: 10.1016/j.molliq.2020.112665] [Citation(s) in RCA: 19] [Impact Index Per Article: 4.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
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15
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Hassanpouryouzband A, Joonaki E, Vasheghani Farahani M, Takeya S, Ruppel C, Yang J, English NJ, Schicks JM, Edlmann K, Mehrabian H, Aman ZM, Tohidi B. Gas hydrates in sustainable chemistry. Chem Soc Rev 2020; 49:5225-5309. [DOI: 10.1039/c8cs00989a] [Citation(s) in RCA: 247] [Impact Index Per Article: 61.8] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/20/2023]
Abstract
This review includes the current state of the art understanding and advances in technical developments about various fields of gas hydrates, which are combined with expert perspectives and analyses.
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Affiliation(s)
- Aliakbar Hassanpouryouzband
- Hydrates, Flow Assurance & Phase Equilibria Research Group
- Institute of GeoEnergy Engineering
- School of Energy
- Geoscience, Infrastructure and Society
- Heriot-Watt University
| | - Edris Joonaki
- Hydrates, Flow Assurance & Phase Equilibria Research Group
- Institute of GeoEnergy Engineering
- School of Energy
- Geoscience, Infrastructure and Society
- Heriot-Watt University
| | - Mehrdad Vasheghani Farahani
- Hydrates, Flow Assurance & Phase Equilibria Research Group
- Institute of GeoEnergy Engineering
- School of Energy
- Geoscience, Infrastructure and Society
- Heriot-Watt University
| | - Satoshi Takeya
- National Institute of Advanced Industrial Science and Technology (AIST)
- Tsukuba 305-8565
- Japan
| | | | - Jinhai Yang
- Hydrates, Flow Assurance & Phase Equilibria Research Group
- Institute of GeoEnergy Engineering
- School of Energy
- Geoscience, Infrastructure and Society
- Heriot-Watt University
| | - Niall J. English
- School of Chemical and Bioprocess Engineering
- University College Dublin
- Dublin 4
- Ireland
| | | | - Katriona Edlmann
- School of Geosciences
- University of Edinburgh
- Grant Institute
- Edinburgh
- UK
| | - Hadi Mehrabian
- Department of Chemical Engineering
- Massachusetts Institute of Technology
- Cambridge
- USA
| | - Zachary M. Aman
- Fluid Science & Resources
- School of Engineering
- University of Western Australia
- Perth
- Australia
| | - Bahman Tohidi
- Hydrates, Flow Assurance & Phase Equilibria Research Group
- Institute of GeoEnergy Engineering
- School of Energy
- Geoscience, Infrastructure and Society
- Heriot-Watt University
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16
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Pourranjbar M, Pahlavanzadeh H, Mohammadi AH. Experimental Measurements and Thermodynamic Modeling of Hydrate Dissociation Conditions for Methane + TBAB + NaCl, MgCl 2, or NaCl-MgCl 2 + Water Systems. Ind Eng Chem Res 2019. [DOI: 10.1021/acs.iecr.9b04844] [Citation(s) in RCA: 17] [Impact Index Per Article: 3.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
Affiliation(s)
| | | | - Amir H. Mohammadi
- Discipline of Chemical Engineering, School of Engineering, University of KwaZulu-Natal, Howard College Campus, King George V, Avenue, Durban 4041, South Africa
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17
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18
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Woo Y, Jeong JH, Lee JW, Park J, Cha M, Kim D, Yoo K, Yoon JH. Thermodynamic stability and formation kinetics of CHClF2 hydrates in the presence of NiCl2. Chem Eng Sci 2019. [DOI: 10.1016/j.ces.2018.09.002] [Citation(s) in RCA: 5] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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19
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Li Z, Liao K, Qin H, Chen J, Ren L, Li F, Zhang X, Liu B, Chen G. The gas‐adsorption mechanism of kinetic hydrate inhibitors. AIChE J 2019. [DOI: 10.1002/aic.16681] [Citation(s) in RCA: 11] [Impact Index Per Article: 2.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/09/2022]
Affiliation(s)
- Zhi Li
- State Key Laboratory of Heavy Oil ProcessingChina University of Petroleum Beijing China
- Shandong Provincial Key Laboratory of Molecular engineering, School of Chemistry and Pharmaceutical EngineeringQiLu University of Technology (Shandong Academy of Sciences) Jinan China
| | - Kai Liao
- MOE Key Laboratory of Petroleum EngineeringChina University of Petroleum Beijing China
| | - Hui‐Bo Qin
- State Key Laboratory of Heavy Oil ProcessingChina University of Petroleum Beijing China
| | - Junli Chen
- State Key Laboratory of Heavy Oil ProcessingChina University of Petroleum Beijing China
| | - Liangliang Ren
- State Key Laboratory of Heavy Oil ProcessingChina University of Petroleum Beijing China
| | - Fengguang Li
- Shandong Provincial Key Laboratory of Molecular engineering, School of Chemistry and Pharmaceutical EngineeringQiLu University of Technology (Shandong Academy of Sciences) Jinan China
| | - Xianren Zhang
- State Key Laboratory of Organic‐Inorganic CompositesBeijing University of Chemical Technology Beijing China
| | - Bei Liu
- State Key Laboratory of Heavy Oil ProcessingChina University of Petroleum Beijing China
| | - Guangjin Chen
- State Key Laboratory of Heavy Oil ProcessingChina University of Petroleum Beijing China
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20
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Effect of ultrasonic waves on dissociation kinetics of tetrafluoroethane (CH 2 FCF 3 ) hydrate. J IND ENG CHEM 2016. [DOI: 10.1016/j.jiec.2016.07.021] [Citation(s) in RCA: 11] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/20/2022]
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21
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Relationship between the interfacial tension and inhibition performance of hydrate inhibitors. Chem Eng Sci 2016. [DOI: 10.1016/j.ces.2016.04.002] [Citation(s) in RCA: 38] [Impact Index Per Article: 4.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/20/2022]
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22
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Thermodynamic modeling of phase equilibria of semi-clathrate hydrates of CO2, CH4, or N2+tetra-n-butylammonium bromide aqueous solution. Chem Eng Sci 2012. [DOI: 10.1016/j.ces.2012.07.006] [Citation(s) in RCA: 71] [Impact Index Per Article: 5.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
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23
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Eslamimanesh A, Babaee S, Mohammadi AH, Javanmardi J, Richon D. Experimental Data Assessment Test for Composition of Vapor Phase in Equilibrium with Gas Hydrate and Liquid Water for Carbon Dioxide + Methane or Nitrogen + Water System. Ind Eng Chem Res 2012. [DOI: 10.1021/ie202465r] [Citation(s) in RCA: 14] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Ali Eslamimanesh
- MINES ParisTech, CEP/TEP - Centre
Énergétique et Procédés, 35 Rue Saint
Honoré, 77305 Fontainebleau, France
| | - Saeedeh Babaee
- Department of Chemical Engineering, Shiraz University of Technology, 71555-313, Shiraz,
Iran
| | - Amir H. Mohammadi
- MINES ParisTech, CEP/TEP - Centre
Énergétique et Procédés, 35 Rue Saint
Honoré, 77305 Fontainebleau, France
- Thermodynamics Research
Unit,
School of Chemical Engineering, University of KwaZulu-Natal, Howard College Campus, King George V Avenue, Durban 4041, South
Africa
| | - Jafar Javanmardi
- Department of Chemical Engineering, Shiraz University of Technology, 71555-313, Shiraz,
Iran
| | - Dominique Richon
- MINES ParisTech, CEP/TEP - Centre
Énergétique et Procédés, 35 Rue Saint
Honoré, 77305 Fontainebleau, France
- Thermodynamics Research
Unit,
School of Chemical Engineering, University of KwaZulu-Natal, Howard College Campus, King George V Avenue, Durban 4041, South
Africa
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24
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Mohammadi AH, Eslamimanesh A, Richon D, Gharagheizi F, Yazdizadeh M, Javanmardi J, Hashemi H, Zarifi M, Babaee S. Gas Hydrate Phase Equilibrium in Porous Media: Mathematical Modeling and Correlation. Ind Eng Chem Res 2011. [DOI: 10.1021/ie201904r] [Citation(s) in RCA: 35] [Impact Index Per Article: 2.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 02/01/2023]
Affiliation(s)
- Amir H. Mohammadi
- MINES ParisTech, CEP/TEP—Centre Énergétique et Procédés, 35 Rue Saint Honoré, 77305 Fontainebleau, France
- Thermodynamics Research Unit, School of Chemical Engineering, University of KwaZulu-Natal, Howard College Campus, King George V Avenue, Durban 4041, South Africa
| | - Ali Eslamimanesh
- MINES ParisTech, CEP/TEP—Centre Énergétique et Procédés, 35 Rue Saint Honoré, 77305 Fontainebleau, France
| | - Dominique Richon
- MINES ParisTech, CEP/TEP—Centre Énergétique et Procédés, 35 Rue Saint Honoré, 77305 Fontainebleau, France
- Thermodynamics Research Unit, School of Chemical Engineering, University of KwaZulu-Natal, Howard College Campus, King George V Avenue, Durban 4041, South Africa
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