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Journal articles on the topic 'Ethanolamines. Carbon dioxide. Mass transfer'

Author: Grafiati

Published: 4 June 2021

Last updated: 1 February 2022

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1

Gómez-Díaz, D., and J. M. Navaza. "Carbon dioxide mass transfer to non-linear alkanes." Canadian Journal of Chemical Engineering 86, no. 4 (August 2008): 719–24. http://dx.doi.org/10.1002/cjce.20035.

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2

Hu, Miao, Rainer Benning, Özgür Ertunc, Antonio Delgado, Vanusch Nercissian, and Andreas Berger. "Mass Transfer of Organic Substances in Supercritical Carbon Dioxide." Defect and Diffusion Forum 326-328 (April 2012): 360–65. http://dx.doi.org/10.4028/www.scientific.net/ddf.326-328.360.

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In this work special attention is paid on the direct visualization of the diffusion process of oil droplets in supercritical carbon dioxide as well as a better characterization of the process by quantitative evaluation of the diffusion coefficients obtained with a shearing interferometer. Experiments are also to be carried out under microgravity in to improve the experiment condition where the influence of gravity-driven convection that usually dominates the transport process is minimized.

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3

Gómez-Díaz, D., and J. M. Navaza. "Gas/liquid mass transfer in carbon dioxide–alkanes mixtures." Chemical Engineering Journal 114, no. 1-3 (November 2005): 131–37. http://dx.doi.org/10.1016/j.cej.2005.09.007.

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4

Hu, M., R. Benning, Ö. Ertunc, J. Neukam, T. Bielke, A. Delgado, V. Nercissian, and A. Berger. "Mass transfer of organic substances in supercritical carbon dioxide." Journal of Physics: Conference Series 327 (December 6, 2011): 012041. http://dx.doi.org/10.1088/1742-6596/327/1/012041.

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5

García-Abuín, Alicia, Diego Gómez-Díaz, and José M. Navaza. "Carbon Dioxide Mass Transfer in Gas–Liquid–Liquid System." Industrial & Engineering Chemistry Research 51, no. 15 (April 5, 2012): 5585–91. http://dx.doi.org/10.1021/ie202775n.

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6

Knaff, G., and E. U. Schlünder. "Mass transfer for dissolving solids in supercritical carbon dioxide." Chemical Engineering and Processing: Process Intensification 21, no. 3 (April 1987): 151–62. http://dx.doi.org/10.1016/0255-2701(87)87004-6.

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7

Bandyopadhyay, Debajyoti, Nirupam Chakraborti, and Ahindra Ghosh. "Heat and mass transfer limitations in gasification of carbon by carbon dioxide." Steel Research 62, no. 4 (April 1991): 143–51. http://dx.doi.org/10.1002/srin.199101264.

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8

Okuno, R., and Z. Xu. "Mass Transfer on Multiphase Transitions in Low-Temperature Carbon-Dioxide Floods." SPE Journal 19, no. 06 (April 10, 2014): 1005–23. http://dx.doi.org/10.2118/166345-pa.

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Summary Mixtures of reservoir oil and carbon dioxide (CO2) can exhibit complex multiphase behavior at temperatures typically less than 120°F, in which a third CO2-rich liquid (L2) phase can coexist with the oleic (L1) and gaseous (V) phases. The three-phase behavior is bounded by two types of critical endpoints (CEPs) in composition space. The lower CEP (LCEP) is a tie line in which the two liquid phases merge in the presence of the V phase, and the upper CEP (UCEP) is a tie line in which the L2 and V phases merge in the presence of the L1 phase. Slimtube tests reported in the literature show that low-temperature oil displacement by CO2 can result in the high displacement efficiency of more than 90% when three phases are present during the displacement. The nearly piston-like displacements can be quantitatively reproduced in numerical simulations when the CEP behavior is properly considered. However, it is uncertain how multicontact miscibility (MCM) is developed through the interaction of flow and three-hydrocarbon-phase behavior. This research presents a detailed analysis of mass conservation on multiphase transitions between two and three phases for the limiting three-phase flow, where the L1 phase is completely displaced by the L2 phase on the LCEP. The analysis indicates that interphase mass transfer on multiphase transitions occurs in the most-efficient way for MCM development. Simple analytical conditions derived for MCM through three phases are applied to 1D fine-scale simulations of CO2 floods by use of four and more components. Results show that the MCM conditions are nearly satisfied when the effect of numerical dispersion is small. MCM is likely developed through three hydrocarbon phases on the LCEP in the cases studied. This is consistent with analytical solutions of water and gas injection presented in the literature, in which MCM is developed on a CEP for the aqueous, V, and L1 phases. For MCM cases in this research, the L2-V two phases are present upstream of the miscible front if the composition path does not go through the UCEP tie line. However, they also can be miscible on the non-L1 edge of the UCEP tie line if the MCM composition path goes through it. Three-phase flow gradually changes to two-phase flow with varying pressure in the presence of numerical dispersion. It is shown that interphase mass transfer on multiphase transitions becomes less efficient during the change until the three-phase region completely disappears.

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9

Gómez-Díaz, D., and JM Navaza. "Gas/liquid mass transfer processes in a carbon dioxide/alkane system." Journal of Chemical Technology & Biotechnology 80, no. 7 (2005): 812–18. http://dx.doi.org/10.1002/jctb.1251.

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10

Park, Sang-Wook, Byoung-Sik Choi, Sung-Su Kim, and Jae-Wook Lee. "Mass transfer of carbon dioxide in aqueous polyacrylamide solution with methyldiethanolamine." Korean Journal of Chemical Engineering 21, no. 6 (December 2004): 1205–11. http://dx.doi.org/10.1007/bf02719495.

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11

Gómez-Díaz, D., and J. M. Navaza. "Carbon Dioxide Mass Transfer into Solvents in a Zeolite Hybrid Device." Chemical Engineering & Technology 36, no. 11 (October 11, 2013): 1853–58. http://dx.doi.org/10.1002/ceat.201300172.

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12

López, Ana B., M. Dolores La Rubia, José M. Navaza, Rafael Pacheco, and Diego Gómez-Díaz. "Carbon Dioxide Absorption in Triethanolamine Aqueous Solutions: Hydrodynamics and Mass Transfer." Chemical Engineering & Technology 37, no. 3 (February 7, 2014): 419–26. http://dx.doi.org/10.1002/ceat.201300603.

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13

Ouboukhlik, Maria, Gilles Godard, Sawitree Saengkaew, Marie-Christine Fournier-Salaün, Lionel Estel, and Gérard Grehan. "Mass Transfer Evolution in a Reactive Spray during Carbon Dioxide Capture." Chemical Engineering & Technology 38, no. 7 (June 10, 2015): 1154–64. http://dx.doi.org/10.1002/ceat.201400651.

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14

Liu, Jinzhao, Shujuan Wang, Guojie Qi, Bo Zhao, and Changhe Chen. "Kinetics and mass transfer of carbon dioxide absorption into aqueous ammonia." Energy Procedia 4 (2011): 525–32. http://dx.doi.org/10.1016/j.egypro.2011.01.084.

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15

Ghaemi, Ahad. "Mass transfer and thermodynamic modeling of carbon dioxide absorption into MEA aqueous solution." Polish Journal of Chemical Technology 19, no. 3 (September 1, 2017): 75–82. http://dx.doi.org/10.1515/pjct-2017-0052.

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Abstract In this research, thermodynamic and absorption rate of carbon dioxide in monoethanolamine (MEA) solution was investigated. A correlation based on both liquid and a gas phase variable for carbon dioxide absorption rate was presented using the π-Buckingham theorem. The correlation was constructed based on dimensionless numbers, including carbon dioxide loading, carbon dioxide partial pressure, film parameter and the ratio of liquid phase film thickness and gas phase film thickness. The film parameter is used to apply the effect of chemical reactions on absorption rate. A thermodynamic model based on the extended-UNIQUAC equations for the activity coefficients coupled with the Virial equation of state for representing the non-ideality of the vapor phase was used to predict the CO2 solubility in the CO2-MEA-H2O system. The average absolute error of the results for the correlation was 6.4%, which indicates the accuracy of the proposed correlation.

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16

de Oliveira, Leonardo Hadlich, Joziane Gimenes Meneguin, Edson Antonio da Silva, Maria Angélica Simões Dornellas de Barros, Pedro Augusto Arroyo, Wilson Mantovani Grava, and Jailton Ferreira do Nascimento. "Linear Driving Force Model in Carbon Dioxide Capture by Adsorption." Applied Mechanics and Materials 830 (March 2016): 38–45. http://dx.doi.org/10.4028/www.scientific.net/amm.830.38.

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In this work, experimental data of CO2 capture by adsorption was determined gravimetrically, at 30 °C and pressures up to 40 bar, and in a fixed bed unit at 20 bar, using NaY as adsorbent. Langmuir, Sips and Tóth isotherm models were used to correlate the equilibrium data. Sips and Tóth models were best fitted allowing estimate the maximum CO2 adsorbed amount. The breakthrough curve was modeled using Linear Driving Force (LDF) and Thomas models. The LDF model represented better the CO2 breakthrough curve than Thomas model. The mass transfer resistance in NaY micropores can be assumed as the limiting step for CO2 adsorption in fixed bed, since the intraparticle mass transfer coefficient of LDF model was smaller than the experimental overall volumetric mass transfer coefficient, although external film resistance is not negligible.

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17

Ma’mun, S., Hallvard F. Svendsen, and I. M. Bendiyasa. "Amine-based carbon dioxide absorption: evaluation of kinetic and mass transfer parameters." Journal of Mechanical Engineering and Sciences 12, no. 4 (December 27, 2018): 4088–97. http://dx.doi.org/10.15282/jmes.12.4.2018.08.0354.

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Global emission of carbon dioxide (CO2), a major contributor to the climate change, has increased annually and it reached over 37 Gt in 2017. An effort to reduce the emission, therefore, needs to be conducted, e.g. post-combustion capture by use of amine-based absorption. The objective of this study is to evaluate the kinetic and mass transfer parameters in a CO2 absorption process using monoethanolamine (MEA), 2-(methylamino)ethanol (MMEA), and 2-(ethylamino)ethanol (EMEA) as absorbents. The experiments were conducted in a bubble reactor at atmospheric pressure and 40 °C with 10-vol% CO2 flowrate of 5 NL/men. The CO2 concentration leaving the reactor was measured by an IR CO2 analyzer. The results obtained from this experiment were the overall absorption rates consisting of both chemical reaction and mass transfer. Analysis result shows that the reaction between CO2 and amines takes place fast, therefore the mass transfer of CO2 from the gas into the liquid through the gas film would control the overall absorption rate.

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18

Özkal, S. G., M. E. Yener, and L. Bayındırlı. "Mass transfer modeling of apricot kernel oil extraction with supercritical carbon dioxide." Journal of Supercritical Fluids 35, no. 2 (September 2005): 119–27. http://dx.doi.org/10.1016/j.supflu.2004.12.011.

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19

Kögel, Andrea, Nicolaus Dahman, and Hanns Ederer. "Mass transfer coefficients from pendant water drop measurements in compressed carbon dioxide." Journal of Supercritical Fluids 29, no. 3 (May 2004): 237–49. http://dx.doi.org/10.1016/s0896-8446(03)00071-8.

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20

Kudra, T., and M. Poirier. "Gaseous Carbon Dioxide as the Heat and Mass Transfer Medium in Drying." Drying Technology 25, no. 2 (February 2007): 327–34. http://dx.doi.org/10.1080/07373930601119912.

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21

Matsumoto, Hiroyo, Akira Kakimoto, and Shuichi Sato. "Mass Transfer Characteristics of Oxygen and Carbon Dioxide in an Artificial Gill." KAGAKU KOGAKU RONBUNSHU 17, no. 6 (1991): 1201–8. http://dx.doi.org/10.1252/kakoronbunshu.17.1201.

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22

Han, Jingyi, Dag A. Eimer, and Morten C. Melaaen. "Liquid Phase Mass Transfer Coefficient of Carbon Dioxide Absorption by Water Droplet." Energy Procedia 37 (2013): 1728–35. http://dx.doi.org/10.1016/j.egypro.2013.06.048.

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23

Hu, M., R. Benning, Ö. Ertunç, A. Delgado, V. Nercissian, and M. Berger. "Study of mass transfer in supercritical carbon dioxide (SCCO2) using optical methods." Heat and Mass Transfer 53, no. 12 (June 7, 2017): 3409–20. http://dx.doi.org/10.1007/s00231-017-2075-7.

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24

Larson, R. J., M. A. Hansmann, and E. A. Bookland. "Carbon dioxide recovery in ready biodegradation tests: Mass transfer and kinetic considerations." Chemosphere 33, no. 6 (September 1996): 1195–210. http://dx.doi.org/10.1016/0045-6535(96)00253-6.

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25

Scholes, Colin A., and Shufeng Shen. "Mass transfer correlations for membrane gas-solvent contactors undergoing carbon dioxide desorption." Chinese Journal of Chemical Engineering 26, no. 11 (November 2018): 2337–43. http://dx.doi.org/10.1016/j.cjche.2018.05.005.

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26

Ferreira, Bruno S., Helena L. Fernandes, Alberto Reis, and Marília Mateus. "Microporous hollow fibres for carbon dioxide absorption: mass transfer model fitting and the supplying of carbon dioxide to microalgal cultures." Journal of Chemical Technology & Biotechnology 71, no. 1 (January 1998): 61–70. http://dx.doi.org/10.1002/(sici)1097-4660(199801)71:1<61::aid-jctb785>3.0.co;2-r.

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27

Liu, Hong Jing, Yang Pan, Hui Yao, and Ying Zhang. "Enhancement of Carbon Dioxide Mass Transfer Rate by (Ionic Liquid)-in-Water Emulsion." Advanced Materials Research 881-883 (January 2014): 113–17. http://dx.doi.org/10.4028/www.scientific.net/amr.881-883.113.

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Effects of dispersed ionic liquid (IL) on physical absorption of CO2in aqueous solution were investigated in the study. IL-in-water emulsion had been prepared, whose continuous phase was surfactant aqueous solution, and dispersed phase was an ionic liquid, 1-octyl-3 methyl imidazole hexafluoride phosphate. The morphololgy of dispersion had been observed by visual method. The CO2concentrations in the bulk of the absorption solvent were calculated. Results show that the enhancement of carbon dioxide mass transfer was realized by IL-in-water emulsion. The reason for the increase of CO2mass transfer rates by dispersed ionic liquid has been attributed to the increase of mass transfer driving force depending on shuttle effect.

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28

Bernard, P., and D. Barth. "Internal Mass Transfer Limitation During Enzymatic Esterification in Supercritical Carbon Dioxide and Hexane." Biocatalysis and Biotransformation 12, no. 4 (January 1995): 299–308. http://dx.doi.org/10.3109/10242429509003192.

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29

Merkel, Wolf, and Karlheinz Krauth. "Mass transfer of carbon dioxide in anaerobic reactors under dynamic substrate loading conditions." Water Research 33, no. 9 (June 1999): 2011–20. http://dx.doi.org/10.1016/s0043-1354(98)00434-5.

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30

Bishnoi, Sanjay, and Gary T. Rochelle. "Absorption of carbon dioxide into aqueous piperazine: reaction kinetics, mass transfer and solubility." Chemical Engineering Science 55, no. 22 (November 2000): 5531–43. http://dx.doi.org/10.1016/s0009-2509(00)00182-2.

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31

Shirazian, S., and S. N. Ashrafizadeh. "Mass Transfer Simulation of Carbon Dioxide Absorption in a Hollow-Fiber Membrane Contactor." Separation Science and Technology 45, no. 4 (February 25, 2010): 515–24. http://dx.doi.org/10.1080/01496390903530081.

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32

Svanström, Magdalena, Olle Ramnäs, Maria E. Olsson, and Ulf Jarfelt. "Mass Transfer of Carbon Dioxide through the Polyethylene Casing of District Heating Pipes." Journal of Thermal Insulation and Building Envelopes 21, no. 2 (October 1997): 171–84. http://dx.doi.org/10.1177/109719639702100207.

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33

Sherman, Brent J., Arlinda F. Ciftja, and Gary T. Rochelle. "Thermodynamic and mass transfer modeling of carbon dioxide absorption into aqueous 2-piperidineethanol." Chemical Engineering Science 153 (October 2016): 295–307. http://dx.doi.org/10.1016/j.ces.2016.07.019.

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34

Luo, Xiao, Ardi Hartono, Saddam Hussain, and Hallvard F. Svendsen. "Mass transfer and kinetics of carbon dioxide absorption into loaded aqueous monoethanolamine solutions." Chemical Engineering Science 123 (February 2015): 57–69. http://dx.doi.org/10.1016/j.ces.2014.10.013.

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35

Park, Sang-Wook, Byoung-Sik Choi, Seong-Soo Kim, and Jae-Wook Lee. "Mass transfer of carbon dioxide in aqueous colloidal silica solution containing N-methyldiethanolamine." Korean Journal of Chemical Engineering 25, no. 4 (July 2008): 819–24. http://dx.doi.org/10.1007/s11814-008-0136-9.

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36

May Lin, Ting, Then Siew Ping, Agus Saptoro, and Panau Freddie. "Mass Transfer Coefficients and Correlation of Supercritical Carbon Dioxide Extraction of Sarawak Black Pepper." International Journal of Food Engineering 10, no. 1 (December 5, 2013): 1–15. http://dx.doi.org/10.1515/ijfe-2012-0219.

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Abstract Bioactive compound, namely piperine, was extracted from Sarawak black pepper using supercritical carbon dioxide extraction. Experiments were carried outin the range of 3,000–5,000 psi (20.7–34.4 MPa) pressures, 318–328 K temperatures, 0.4–1 mm mean particle sizes and5–10 ml/min carbon dioxide flow rates. Experimental data analysis shows that extraction yield ismainly influenced by pressure, particle size and coupled-interactions between these two variables. Extraction process was modeled accounting for intraparticle diffusion and external mass transfer. The kinetics parameters for the internal and external mass transfers were evaluated and estimated. Mass transfer correlation was also developed. From simulation results, good agreement between experimental and simulated data has been found.

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37

Lockemann, C. A., and E. U. Schlünder. "High-pressure mass-transfer coefficients in the liquid phase of the binary systems carbon dioxide-methyl myristate and carbon dioxide-methyl palmitate." Chemical Engineering and Processing: Process Intensification 35, no. 2 (March 1996): 121–29. http://dx.doi.org/10.1016/0255-2701(95)04118-4.

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38

Hafner, Sasha D., Sven G. Sommer, Valdemar Petersen, and Rikke Markfoged. "Effects of carbon dioxide hydration kinetics and evaporative convection on pH profile development during interfacial mass transfer of ammonia and carbon dioxide." Heat and Mass Transfer 53, no. 4 (September 2, 2016): 1335–42. http://dx.doi.org/10.1007/s00231-016-1910-6.

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39

Chong, G. H., S. Y. Spotar, and R. Yunus. "Numerical Modeling of Mass Transfer for Solvent-Carbon Dioxide System at Supercritical (Miscible) Conditions." Journal of Applied Sciences 9, no. 17 (August 15, 2009): 3055–61. http://dx.doi.org/10.3923/jas.2009.3055.3061.

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40

Adeib, I. S., I. Norhuda, R. N. Roslina, and M. S. Ruzitah. "Mass Transfer and Solubility of Hibiscus cannabinus L. Seed Oil in Supercritical Carbon Dioxide." Journal of Applied Sciences 10, no. 12 (June 1, 2010): 1140–45. http://dx.doi.org/10.3923/jas.2010.1140.1145.

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41

Determan, Matthew D., Dhruv C. Hoysall, and Srinivas Garimella. "Heat- and Mass-Transfer Kinetics of Carbon Dioxide Capture Using Sorbent-Loaded Hollow Fibers." Industrial & Engineering Chemistry Research 51, no. 1 (December 5, 2011): 495–502. http://dx.doi.org/10.1021/ie201380r.

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42

Shamu, Andrew, Henk Miedema, Sybrand J. Metz, Zandrie Borneman, and Kitty Nijmeijer. "Mass transfer studies on the dehydration of supercritical carbon dioxide using dense polymeric membranes." Separation and Purification Technology 209 (January 2019): 229–37. http://dx.doi.org/10.1016/j.seppur.2018.07.042.

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43

Turri, Fabio, and Jurandir Itizo Yanagihara. "Computer-Assisted Numerical Analysis for Oxygen and Carbon Dioxide Mass Transfer in Blood Oxygenators." Artificial Organs 35, no. 6 (April 1, 2011): 579–92. http://dx.doi.org/10.1111/j.1525-1594.2010.01150.x.

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44

Zhang, Liang-Liang, Jie-Xin Wang, Zhi-Ping Liu, Ying Lu, Guang-Wen Chu, Wen-Chuan Wang, and Jian-Feng Chen. "Efficient capture of carbon dioxide with novel mass-transfer intensification device using ionic liquids." AIChE Journal 59, no. 8 (March 14, 2013): 2957–65. http://dx.doi.org/10.1002/aic.14072.

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45

Luo, BenYi, and YiGang Lu. "The ultrasonic-enhanced factor of mass-transfer coefficient in the supercritical carbon dioxide extraction." Science in China Series G: Physics, Mechanics and Astronomy 51, no. 10 (September 14, 2008): 1496–504. http://dx.doi.org/10.1007/s11433-008-0143-1.

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46

Aoki, Jiro, Kosuke Hayashi, Shigeo Hosokawa, and Akio Tomiyama. "Effects of Surfactants on Mass Transfer from Single Carbon Dioxide Bubbles in Vertical Pipes." Chemical Engineering & Technology 38, no. 11 (August 28, 2015): 1955–64. http://dx.doi.org/10.1002/ceat.201500063.

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47

Aoki, Jiro, Yohei Hori, Kosuke Hayashi, Shigeo Hosokawa, and Akio Tomiyama. "Mass transfer from single carbon dioxide bubbles in alcohol aqueous solutions in vertical pipes." International Journal of Heat and Mass Transfer 108 (May 2017): 1991–2001. http://dx.doi.org/10.1016/j.ijheatmasstransfer.2017.01.058.

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48

Hori, Yohei, Kosuke Hayashi, Shigeo Hosokawa, and Akio Tomiyama. "Mass transfer from single carbon-dioxide bubbles in electrolyte aqueous solutions in vertical pipes." International Journal of Heat and Mass Transfer 115 (December 2017): 663–71. http://dx.doi.org/10.1016/j.ijheatmasstransfer.2017.07.087.

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49

Zıraman, Duygu Uysal, Özkan Murat Doğan, and Bekir Zühtü Uysal. "Mass transfer enhancement factor for chemical absorption of carbon dioxide into sodium metaborate solution." Korean Journal of Chemical Engineering 35, no. 9 (August 3, 2018): 1800–1806. http://dx.doi.org/10.1007/s11814-018-0100-2.

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50

Malekshahian, Maryam, Alex De Visscher, and Josephine M. Hill. "A non-equimolar mass transfer model for carbon dioxide gasification studies by thermogravimetric analysis." Fuel Processing Technology 124 (August 2014): 1–10. http://dx.doi.org/10.1016/j.fuproc.2014.02.009.

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