Assessment of commercial hydrate inhibitors using the 3‐in‐1 method
Abstract Phase equilibria, kinetics, and morphology studies of gas hydrates require separate pieces of equipment and experimentation times in the order of days. Recently, we designed a reactor that allows for tight control of the crystallization temperature. Coupled with a novel method, this reactor...
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crwiley:10.1002/cjce.23611 2024-03-17T08:58:56+00:00 Assessment of commercial hydrate inhibitors using the 3‐in‐1 method Ovalle, Sebastian Martinez, Camilo Bonilla, Luna Lara, Andres Beltran, Juan G. Canada Foundation for Innovation Natural Sciences and Engineering Research Council of Canada 2019 http://dx.doi.org/10.1002/cjce.23611 https://onlinelibrary.wiley.com/doi/pdf/10.1002/cjce.23611 https://onlinelibrary.wiley.com/doi/full-xml/10.1002/cjce.23611 en eng Wiley http://onlinelibrary.wiley.com/termsAndConditions#vor The Canadian Journal of Chemical Engineering volume 97, issue 11, page 2818-2826 ISSN 0008-4034 1939-019X General Chemical Engineering journal-article 2019 crwiley https://doi.org/10.1002/cjce.23611 2024-02-22T01:55:20Z Abstract Phase equilibria, kinetics, and morphology studies of gas hydrates require separate pieces of equipment and experimentation times in the order of days. Recently, we designed a reactor that allows for tight control of the crystallization temperature. Coupled with a novel method, this reactor can screen the crystal morphology, phase equilibria, and apparent kinetics of gas hydrates. Compared to traditional multi‐trial methods, the main advantage of this method is that only a single experiment, completed in the order of hours, is required to assess: (a) the change in hydrate growth velocity with respect to temperature, (b) the HLV equilibrium temperature at the experimental pressure, and (c) the change in crystal morphology with respect to driving force. Using this 3‐in‐1 method, methane hydrate growth and dissociation was studied in the presence of four commercial inhibitors. Phase equilibria, kinetics, and morphology were obtained for all hydrate systems with inhibitors. The standard uncertainty for the HLV equilibrium temperature was 0.05 K and for pressure 0.005 MPa. The apparent rates of growth were measured for all systems (standard uncertainty was 0.008 mm · s −1 ) and the difference between the inhibited systems and the pure system was very clear. Crystal habits varied considerably among inhibitors and radically with respect to the uninhibited system. Overall, we present an innovative technology to assess the morphology, kinetics, and thermodynamics of hydrate forming systems with a single apparatus. Furthermore, with little time investment, small sample sizes can be used to obtain replicates with minimum temperature and pressure uncertainties. Article in Journal/Newspaper Methane hydrate Wiley Online Library The Canadian Journal of Chemical Engineering 97 11 2818 2826 |
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Wiley Online Library |
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language |
English |
topic |
General Chemical Engineering |
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General Chemical Engineering Ovalle, Sebastian Martinez, Camilo Bonilla, Luna Lara, Andres Beltran, Juan G. Assessment of commercial hydrate inhibitors using the 3‐in‐1 method |
topic_facet |
General Chemical Engineering |
description |
Abstract Phase equilibria, kinetics, and morphology studies of gas hydrates require separate pieces of equipment and experimentation times in the order of days. Recently, we designed a reactor that allows for tight control of the crystallization temperature. Coupled with a novel method, this reactor can screen the crystal morphology, phase equilibria, and apparent kinetics of gas hydrates. Compared to traditional multi‐trial methods, the main advantage of this method is that only a single experiment, completed in the order of hours, is required to assess: (a) the change in hydrate growth velocity with respect to temperature, (b) the HLV equilibrium temperature at the experimental pressure, and (c) the change in crystal morphology with respect to driving force. Using this 3‐in‐1 method, methane hydrate growth and dissociation was studied in the presence of four commercial inhibitors. Phase equilibria, kinetics, and morphology were obtained for all hydrate systems with inhibitors. The standard uncertainty for the HLV equilibrium temperature was 0.05 K and for pressure 0.005 MPa. The apparent rates of growth were measured for all systems (standard uncertainty was 0.008 mm · s −1 ) and the difference between the inhibited systems and the pure system was very clear. Crystal habits varied considerably among inhibitors and radically with respect to the uninhibited system. Overall, we present an innovative technology to assess the morphology, kinetics, and thermodynamics of hydrate forming systems with a single apparatus. Furthermore, with little time investment, small sample sizes can be used to obtain replicates with minimum temperature and pressure uncertainties. |
author2 |
Canada Foundation for Innovation Natural Sciences and Engineering Research Council of Canada |
format |
Article in Journal/Newspaper |
author |
Ovalle, Sebastian Martinez, Camilo Bonilla, Luna Lara, Andres Beltran, Juan G. |
author_facet |
Ovalle, Sebastian Martinez, Camilo Bonilla, Luna Lara, Andres Beltran, Juan G. |
author_sort |
Ovalle, Sebastian |
title |
Assessment of commercial hydrate inhibitors using the 3‐in‐1 method |
title_short |
Assessment of commercial hydrate inhibitors using the 3‐in‐1 method |
title_full |
Assessment of commercial hydrate inhibitors using the 3‐in‐1 method |
title_fullStr |
Assessment of commercial hydrate inhibitors using the 3‐in‐1 method |
title_full_unstemmed |
Assessment of commercial hydrate inhibitors using the 3‐in‐1 method |
title_sort |
assessment of commercial hydrate inhibitors using the 3‐in‐1 method |
publisher |
Wiley |
publishDate |
2019 |
url |
http://dx.doi.org/10.1002/cjce.23611 https://onlinelibrary.wiley.com/doi/pdf/10.1002/cjce.23611 https://onlinelibrary.wiley.com/doi/full-xml/10.1002/cjce.23611 |
genre |
Methane hydrate |
genre_facet |
Methane hydrate |
op_source |
The Canadian Journal of Chemical Engineering volume 97, issue 11, page 2818-2826 ISSN 0008-4034 1939-019X |
op_rights |
http://onlinelibrary.wiley.com/termsAndConditions#vor |
op_doi |
https://doi.org/10.1002/cjce.23611 |
container_title |
The Canadian Journal of Chemical Engineering |
container_volume |
97 |
container_issue |
11 |
container_start_page |
2818 |
op_container_end_page |
2826 |
_version_ |
1793768850653708288 |