the Altmetric Attention Score and how the score is calculated. Article Views are the COUNTER-compliant sum of full text article downloads since November 2008 (both PDF and HTML) across all institutions and individuals. A Roadmap for Production of Cement and Concrete with Low-CO2 Emissions. Journal of Natural Gas Science and Engineering. Solubility of CO2 in water from -1.5 to 100°C and from 0.1 to 100 MPa: Evaluation of literature data and thermodynamic modelling Journal of Petroleum Science and Engineering. Tianyuan Wang, Elise El Ahmar, Christophe Coquelet, Georgios M. Kontogeorgis. The liquid phase composition at the thermodynamic equilibrium is determined by an analytical method (ion chromatography) and a static synthetic method. Klok, Gijs J. van Heeringen, Karel J. Keesman, Albert J.H. Measurement and correlation of solubility of carbon dioxide in triglycerides. Floriane Lucile * † ‡, Pierre Cézac ‡, François Contamine ‡, Jean-Paul Serin ‡, Deborah Houssin †, and ; Philippe Arpentinier † ��|��5���`+���yWU{cʽ�j*�4��6�T�BB�K�_7�9��T�&�� ҅��=RE���U%�7�->���6% stream Humbul Suleman, Abulhalim Shah Maulud, Zakaria Man. Kinetic study of the nitric oxide oxidation between 288 and 323 K, under pressure, focus on the oxygen influence on the reaction rate constant. Juha-Pekka Pokki, Huy Quang Lê, Petri Uusi-Kyyny, Herbert Sixta. Improving the lipid recovery from wet oleaginous microorganisms using different pretreatment techniques. Temperature Dependence As with other gases, the solubility of carbon dioxide in water decreases as the temperature increases. %PDF-1.3 Measuring mutual solubility in the H 2 O–CO 2 system up to 200 bar and 100 °C by in situ Raman spectroscopy. Biologically enhanced hydrogen sulfide absorption from sour gas under haloalkaline conditions. Byeong Soo Shin, Won Gu Rho, Seong-Sik You, Jeong Won Kang, Chul Soo Lee. %��������� The CO A hybrid equation of state and Kent-Eisenberg model for accurate prediction of carbon dioxide separation by aqueous alkanolamines. -behavior of water / carbon dioxide mixtures. Niaz Neisani Samani, Sayed Mohammadreza Miforughy, Hossein Safari, Omid Mohammadzadeh, Mohammad Hossein Panahbar, Sohrab Zendehboudi. Sanehiro Muromachi, Atsushi Shijima, Hiroyuki Miyamoto, Ryo Ohmura. Measurement and modeling of CO2 solubility in binary aqueous DMSO and MDEA and their ternary mixtures at different temperatures and compositions. As the temperature of the oceans increases with increasing These metrics are regularly updated to reflect usage leading up to the last few days. Isobaric Vapor–Liquid Equilibrium of Furfural + γ-Valerolactone at 30 kPa and Isothermal Liquid–Liquid Equilibrium of Carbon Dioxide + γ-Valerolactone + Water at 298 K. Hamdi Messabeb, François Contamine, Pierre Cézac, Jean Paul Serin, and Eric C. Gaucher . Thermodynamic models to accurately describe the Find more information about Crossref citation counts. The Altmetric Attention Score is a quantitative measure of the attention that a research article has received online. New experimental solubility data for carbon dioxide in pure water and in aqueous solution containing sodium hydroxide in the temperature range (293.15 to 393.15) K and pressures up to 5 MPa are presented in this work. Your Mendeley pairing has expired. International Journal of Chemical Kinetics. ?�������K9@�fV��B Kۭn�� �E�����[JTx�pՋ�Pi��L�zu�Q�����B\�P��j-��:��YPH���TV�c����?�$�����^TT�r�:������Um���iH����-�����N!�b High-pressure fluid-phase equilibria: Trends, recent developments, and systems investigated (2009–2012). Ehsan Ranjbar, Seyyed M. Ghaderi, Hossein Nourozieh, Anjani Kumar, Ali Takbiri-Borujeni. 6{���0�7,�h�aO�*�2�7;��E�5A�'=j�^Gkq�H�ê`�2I�Z�ޒ+����y9ܓK��`�P�+v,g��x7�-ܒCnDQ�����؊_� 4�D�����6j�")�����_�D*{�|< �#*�;�Ԃ��?�"����D��*!��95���-{��w� �ш���_Ț�̾�����G,UE���C Fonseca, Ralf Dohrn. Chemical and Phase Equilibria in the Reaction between NO and O2 in the Presence of Water and CO2 at 298.15 K up to 3 MPa. Stephanie Peper, José M.S. 2 Experimental Study of the Liquid Vapour Equilibrium of the System Water‐CO Esther Neyrolles, José Lara Cruz, Georgio Bassil, François Contamine, Pierre Cezac, Philippe Arpentinier. CO2 dissolution in water at different pressure and temperature conditions is one of the most essential issues to CO2 geological sequestration in brine aquifers. Extreme Learning Machine-Based Model for Solubility Estimation of Hydrocarbon Gases in Electrolyte Solutions. Experimental Measurement of CO2 Solubility in Aqueous NaCl Solution at Temperature from 323.15 to 423.15 K and Pressure of up to 20 MPa. Georgio Bassil, Esther Neyrolles, François Contamine, Pierre Cezac. You have to login with your ACS ID befor you can login with your Mendeley account. Find more information about Crossref citation counts. ���~J\�Jj5��q��1i���6٠�͈� �l��3�,`�I��}�.%{�E�lQ�� Experimental measurements of carbon dioxide solubility in aqueous tetra-n-butylammonium bromide solutions. Please note: If you switch to a different device, you may be asked to login again with only your ACS ID. Narjes Nabipour, Sultan Noman Qasem, Ely Salwana, Alireza Baghban. Under Pressure at 298 K. Rieks de Rink, Johannes B.M. ‐NO Pilot project at Hazira, India, for capture of carbon dioxide and its biofixation using microalgae. ��n`Z=0���V꫶��.��U�õ�G:OEW���ӻ3�w��he�������j��UW6�~9[���~�?���+L�q�|��Sբs����o�}=�������b���� �,[�z�����h�:}D�lU�Yp�I���F��0�&H��A2�� Fundamentals of Gas Diffusion Electrodes and Electrolysers for Carbon Dioxide Utilisation: Challenges and Opportunities. Fluid Phase Equilibria 2003 , 208 (1-2) , 265-290. Get article recommendations from ACS based on references in your Mendeley library. Maria Gunnarsson, Diana Bernin, Åsa Östlund, Merima Hasani. Please reconnect. A�$#�_���Bk�oH�/�v��0T�ׄ�[��pP�u�%r��,�O��2&�Şe���GNHR� Effective Mass Transfer Area Measurement Using a CO2–NaOH System: Impact of Different Sources of Kinetics Models and Physical Properties. Monteiro, Hallvard F. Svendsen, Hanna Knuutila. Solubility of CO2 in water from −1.5 to 100 °C and from 0.1 to 100 MPa: evaluation of literature data and thermodynamic modelling. Solubility of pure gases like. VLE Modeling of Aqueous Solutions of Unloaded and Loaded Hydroxides of Lithium, Sodium and Potassium. �DoOE� ��ҢH��ERD/���Q/��tiKLER�Z)ߎ�H�Ђ \(���D�c=�%��d�y��њeV�PQ!JtV�\?CZ�b�_ -T�>n@�*�hb�]�д5��� x�Z�r��}�h?���X�cLIQ9���҃��C�P������>=��d"�j@�v�s��g���ls��p�m�®��G����;gOw'���-/�}�l�j&?��ɍ�qi�y��]�X����6��r����o�.�z{ԟڃ������W÷�ӳ=��ݾYz�������.��!��fo�@Sa����?���l��w6�{�.���I_��M��0ׯ��kdkl3�e��eU9/��b��,���ռCM#ˮ"e�l��;?�(��x��{���d���H���A������BN��/1�*9s��@G�^y�mV�Sg��eX�!���>�Yup��]P�]�XDP�Q�R e� %A��=#[�HT���ĵ+����B�t��d�x��yVU�5�ac�0�|�=�X�g����0t�*h�}����d��x�]����ʣ��x�"Z%��X:Q8�ZahA 2 the concentration of protons and bicarbonate ion in water. << /Length 5 0 R /Filter /FlateDecode >> 2 An electrolyte segmental wilson-nonrandom excess Gibbs energy model and measurement of carbon dioxide solubility into sulfolane +water and N-methyldiethanolamine+sulfolane+water systems. Buisman. International Journal of Greenhouse Gas Control. Improvement of the PR-CPA equation of state for modelling of acid gases solubilities in aqueous alkanolamine solutions. x Solubility prediction of carbon dioxide in water by an iterative equation of state/excess Gibbs energy model. Valderio de Oliveira Cavalcanti Filho, Antonin Chapoy, Rod Burgass. Md Shamim Howlader, William Todd French, Hossein Toghiani, Ben Hartenbower, Larry Pearson, Janice DuBien, Neeraj Rai. Shahla Gondal, Muhammad Usman, Juliana G.M.S. Ailo Aasen, Morten Hammer, Geir Skaugen, Jana P. Jakobsen, Øivind Wilhelmsen. Jannie S. J. van Deventer, Claire E. White, Rupert J. Myers. The CO2 + water system is used to validate the experimental apparatus; therefore data obtained are compared with literature data. Find more information on the Altmetric Attention Score and how the score is calculated. PVTxy https://doi.org/10.1016/j.fluid.2020.112845, https://doi.org/10.1016/j.jngse.2020.103654, https://doi.org/10.1016/j.measurement.2020.107999, https://doi.org/10.1007/s12649-020-01180-5, https://doi.org/10.1002/9781119593324.ch3, https://doi.org/10.1016/j.jhazmat.2019.121104, https://doi.org/10.1016/j.molliq.2019.111786, https://doi.org/10.1016/j.fluid.2018.10.007, https://doi.org/10.1016/j.fuel.2018.11.150, https://doi.org/10.1016/j.petrol.2018.09.091, https://doi.org/10.1016/j.biortech.2018.07.092, https://doi.org/10.1016/j.fluid.2018.04.019, https://doi.org/10.1007/s10765-018-2364-5, https://doi.org/10.1007/s10570-017-1288-8, https://doi.org/10.1016/j.fluid.2017.02.006, https://doi.org/10.1016/j.jct.2016.09.035, https://doi.org/10.1080/01496395.2016.1217241, https://doi.org/10.1007/s11356-016-6479-6, https://doi.org/10.1088/1755-1315/36/1/012003, https://doi.org/10.1016/j.ijggc.2016.01.034, https://doi.org/10.1016/j.egypro.2016.01.029, https://doi.org/10.1016/j.jct.2015.01.008, https://doi.org/10.1016/j.fluid.2013.07.029. 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