Accueil || Parcours || Recherche || S'enregistrer || Mon Compte || Contacts || Aide || Langues
Amann, Jean-Marc (2007) Etude de procédés de captage du CO2 dans les centrales thermiques. Doctorat Génie des Procédés, CEP - Centre Energétique et Procédés, ENSMP p.188.
Plein texte disponible en tant que :
|
|
Résumé
La présente étude a pour objectif d’évaluer et de comparer entre eux divers procédés de captage du CO2 appliqués aux centrales thermiques alimentées en gaz naturel (NGCC) et au charbon pulvérisé (CP). Ces procédés consistent en un captage du CO2 des fumées en post-combustion par des solvants chimiques, une décarbonisation du gaz naturel avec captage du CO2 en pré-combustion par un solvant physique et l’oxy-combustion du combustible avec séparation frigorifique du CO2. Ces procédés ont été évalués à l’aide du logiciel de procédés Aspen PlusTM pour aider à choisir la meilleure option pour chaque type de centrale. Pour la post-combustion, une solution aqueuse basée sur un mélange d’amines (N-méthyldiéthanolamine (MDEA) et triéthylène tétramine (TETA)) a été évaluée. Des mesures d’absorption ont été réalisées entre 298 et 333 K dans un réacteur fermé type cellule de Lewis. La pression partielle du CO2 à l’équilibre, caractéristique de la solubilité du CO2 dans le solvant, a été déterminée jusqu’à 393 K. Les performances sont comparées vis à vis de solvants plus conventionnels tels que la MDEA et la monoéthanolamine (MEA). Pour l’oxy-combustion, un procédé de captage, basé sur une séparation des composants des fumées à faible température, a été développé et appliqué aux centrales NGCC et CP. L’étude a montré que la pureté du flux d’O2 avait une influence non négligeable sur la concentration en CO2 dans les fumées et donc sur les performances du procédé de séparation. La dernière option étudiée est le reformage du gaz naturel qui permet un captage du CO2 en amont du système de production de l’électricité. Plusieurs configurations ont été évaluées : reformage à l’air ou à l’oxygène, pression de reformage et dilution du gaz de synthèse. La comparaison de ces différents concepts suggère que, à court et moyen terme, l’absorption chimique soit le procédé le plus intéressant pour la centrale NGCC. Pour la centrale CP, l’oxy-combustion peut être une option très intéressante, au même titre que le captage en post-combustion par absorption chimique.
| Type d'EPrint: | Thèse (Doctorat) |
|---|---|
| Directeur de Mémoire: | Bouallou, Chakib |
| Date: | 13 Décembre 2007 |
| Jury de Mémoire: | Sacadura, Jean-François et Grevillot, Georges et Prévost, Michel et Kanniche, Mohamed et Nougier, Luc et Bouallou, Chakib |
| Ecole Doctorale: | ED 432 ECOLE DOCTORALE SCIENCES DES METIERS DE L'INGENIEUR |
| Discipline: | Génie des Procédés |
| Fonds: | ENSMP |
| Institution: | ENSMP |
| Laboratoire: | CEP - Centre Energétique et Procédés |
| Sujets: | 6. Chimie, physico-chimie et génie chimique |
| Mots-clés libres: | Combined cycle power plant, Fume collection, Solvent, Decarbonization, CO2 Capture, Natural gas reforming, Process modelling, Captage CO2, Centrale charbon, Post-combustion, Oxy-combustion, N-methyldiethanolamine, Triethylène tetramine, Simulation de procédés, Pre-combustion |
| Code ID: | 3445 |
| Déposé par : | Claudine Abauzit |
| Déposé le : | 16 Mai 2008 |
Références Bibliographiques
Aboudheir A., Tontiwachwuthikul P., Chakma A., Idem R., Kinetics of the reactive
absorption of carbon dioxide in high CO2-loaded, concentrated aqueous monoethanolamine
solutions, Chemical Engineering Science, 58, pp 5195-5210, 2003.
Abu-Zahra M.R.M., Schneiders L.H.J., Niederer J.P.M., Feron P.H.M., Versteeg G.F.,
CO2 capture from power plants – Part I. A parametric study of the technical performance based
on monoethanolamine, International Journal of Greenhouse Gas Control, 1, pp. 37-46, 2007a.
Abu-Zahra M.R.M., Niederer J.P.M., Feron P.H.M., Versteeg G.F., CO2 capture from
power plants – Part II. A parametric study of the economical performance based on monoethanolamine,
International Journal of Greenhouse Gas Control, 1, pp. 135-142, 2007b.
Al-Ghawas H.A., Hagewiesche D.P., Ruiz-Ibanez G., Sandall O.C., Physicochemical
properties important for carbon dioxide absorption in aqueous methyldiethanolamine, Journal of
Chemical and Engineering Data, 34(4), pp. 385-391, 1989.
Alie C.F., CO2 capture with MEA: Integrating the absorption process and steam cycle of an
existing coal-fired power plant, thesis, University of Waterloo, Ontario, Canada, 2004.
Allam R. J., Spilsbury C. G., A study of the extraction of CO2 from the flue gas of a 500 MW
pulverised coal fired boiler, Energy Conversion and Management, vol. 33, no 5-8, pp 373 - 378,
1992.
Al-Sahhaf T.A., Kidnay A.J., Dedy Sloan E., Liquid + vapor equilibria in the N2 + CO2 + CH4
system, Industrial and engineering chemistry Fundamentals, 22, pp. 372-380, 1983.
Andersson K., Johnsson F., Strömberg L., An 865 MWe lignite-fired power plant with CO2
capture – a technical feasibility study, VGB Conference “Power Plants in Competition –
Technology, Operation and Environment, Cologne, mars 2003.
Andersson K., Maksinen P., Chalmers – Process evaluation of CO2 free combustion in an
O2/CO2 power plant, Master thesis, 2002.
Aroonwilas A., Veawab A., Integration of CO2 capture unit using single- and blended-amines
into supercritical coal-fired power plants: Implications for emission and energy management,
International Journal of Greenhouse Gas Control, 1, pp. 143-150, 2007.
Aroua M.K., Haji-Sulaiman M.Z., Ramasamy K., Modelling of carbon dioxide absorption in
aqueous solutions of AMP and MDEA and their blends using Aspenplus, Separation and
Purification Technology, 29, pp. 153-162, 2002.
Arpentinier P., Cavani F., Trifirò F., The technology of Catalytic Oxidations, Chemical,
catalytic & engineering aspects, pp. 23 – 48, Editions TECHNIP, 2001.
AspenTech, Aspen Physical Property System - Physical Property Data 12.1, juin 2003b.
AspenTech, Aspen Physical Property System - Physical Property Methods and Models 12.1,
juin 2003a.
Austgen D. M., Rochelle G. T., Model of vapor-liquid equilibria for aqueous acid gasalkanolamine
systems. 2. Representation of hydrogen sulfide and carbon dioxide solubility in
aqueous MDEA and carbon dioxide solubility in aqueous mixtures of MDEA with MEA or
DEA, Industrial and Engineering Chemistry Research, vol. 30(3), pp. 543-555, 1991.
Babatunde A. O., Rochelle G. T., Alternative stripper configurations to minimize energy for
CO2 capture, 8th International Conference on Greenhouse Gas Control Technologies, Trondeim,
Norvège, 19-22 Juin, 2006.
Bailey D.W., Feron P.H.M., Post-combustion Decarbonisation Processes, Oil & Gas Science
and Technology – Rev. IFP, Vol. 60, n° 3, pp. 461-474, 2005.
Barth D., Tondre C., Delpuech J-J., Kinetics and mechanisms of the reactions of carbon
dioxide with alkanolamines: a discussion concerning the cases of MDEA and DEA, Chemical
Engineering Science, vol. 39, n° 12, pp. 1753-1757, 1984.
Blauwhoff P.M.M., Versteeg G.F., Van Swaaij P.M., A study on the reaction between CO2
and alkanolamines in aqueous solutions, Chemical Engineering Science, Vol. 39, No. 2, pp 207-
225, 1984.
Bohm M.C., Herzog H.J., Parsons J.E., Sekar R.C., Capture-ready coal plants-options,
technologies and economics, International Journal of Greenhouse Gas Control, 1, pp. 113-120,
2007.
Bolland O, Undrum H., A novel methodology for comparing CO2 capture options for natural
gas-fired combined cycle plants, Advances in Environmental Research, 7, pp. 901-911, 2003.
Bolland O., Mathieu P., Comparison of two CO2 removal options in combined cycle power
plants, Energy Conversion and Management, Vol. 39, No 16-18, pp 1653 - 1663, 1998.
Bozzuto C., Scheffknecht G., Fouilloux J.-P., Clean power generation technologies utilizing
solid fuels, World Energy Council, 18th Congress, octobre 2001.
Butwell K. F., Kubek D. J., Sigmund P. W., Alkanolamine treating – The chemistry,
engineering and operational aspects of the primary and secondary amines utilized in syngas
purification are explored, Hydrocarbon Processing, mars 1982.
Cadours R., Absorption-désorption de gaz acides par des solutions aqueuses d’amines, Thèse
de l’Ecole des Mines de Paris, 1998.
Cadours R., Bouallou C., Rigorous simulation of gas absorption into aqueous solutions,
Industrial and Engineering Chemistry Research, vol. 37, pp. 1063-1070, 1998.
Chang C-S, Rochelle G. T., Mass transfer enhanced by equilibrium reactions, Industrial and
Engineering Chemistry Fundamentals, 21, pp. 379-385, 1982.
Christensen T. S., Primdahl I. I., Improve syngas production using autothermal reforming,
Hydrocarbon Processing, mars 1994.
Claverie M., Clément D., Girard C., Benkhalifa F., Labrousse M., Mission d’évaluation
économique de la filière nucléaire - La prospective technologique des filières non nucléaires,
Commissariat général du plan, http://www.ladocumentationfrancaise.fr, juillet 2000.
Croiset E., Thambimuthu K. V., NOx and SO2 emissions from O2/CO2 recycle coal
combustion, Fuel, vol. 80, pp. 2117 -2121, 2001.
Cullinane J.T., Rochelle G.T., Carbon dioxide absorption with aqueous potassium carbonate
promoted by piperazine, Chemical Engineering Science, 59, pp. 3619-3630, 2004.
Cullinane J.T., Rochelle G.T., Thermodynamics of aqueous potassium carbonate, piperazine,
and carbon dioxide, Fluid Phase Equilibria, 227, pp. 197-213, 2005.
Dang H., Rochelle G.T., CO2 absorption rate and solubility in
monoethanolamine/piperazine/water, First National Conference on Carbon Sequestration,
Washington, DC, 14-17 mai, 2001.
Davison J., Performance and costs of power plants with capture and storage of CO2, Energy,
32, pp. 1163-1176, 2007.
de Molliens P., Calcul des réacteurs catalytiques - Conversion du CO par la vapeur d’eau,
Technique de l’Ingénieur, J4080, 1993.
Dechamps P., Pilavachi P.A., Research and Development Actions to Reduce CO2 Emissions
within the European Union, Oil & Gas Science and Technology – Rev. IFP, Vol. 59, n° 3, pp.
323-330, 2004.
Descamps C., Coquelet C., Bouallou C., Richon D., Solubility of hydrogen in methanol at
temperatures from 248.41 to 308.20 K, Thermochimica Acta, 430, pp. 1 – 7, 2005.
Descamps C., Etude de la capture du CO2 par absorption physique dans les systèmes de
production d’électricité bases sur la gazéification du charbon intégrée à un cycle combiné,
Thèse de l’Ecole des Mines de Paris, 2004.
Descamps C., Bouallou C., Kanniche M., Efficiency of an integrated gasification combined
cycle (IGCC) power plant including CO2 removal, Energy, doi:10.1016/j.energy.2007.07.013,
2007.
Dillon D. J., Pansesar, R. S., Wall R. A., Allam R. J. V. White, Gibbins J., Haines M. R.,
Oxy-combustion processes for CO2 capture from advanced supercritical PF and NGCC power
plant, 7th International Conference on Greenhouse Gas Control Technologies, Canada, 5-9
septembre 2004.
Duan L., Lin R., Deng S., Jin H., Cai R., A novel IGCC system with steam injected H2/O2
cycle with CO2 recovery, Energy Conversion and Management, 45, pp. 797-809, 2004.
Edwards T.J., Maurer G., Newman J., Prausnitz J.M., Vapor-liquid equilibria in
multicomponent aqueous solutions of volatile weak electrolytes, AIChE Journal, vol. 24, n° 6,
pp. 966-976, 1978.
Ertesvåg I. S., Kvamsdal H. M., Boland O., Exergy analysis of a gas-turbine combined cycle
power plant with precombustion CO2 capture, Energy 30, pp 5-39, 2005.
Farina G.L., Bressan L., Optimisation of the Degree of Integration of IGCC Design, Power-
Gen Europe, 1998.
Hagewiesche D.P., Ashour S.S., Al-Ghawas H.A., Sandall O.C., Absorption of carbon
dioxide into aqueous blends of monoethanolamine and N-methyldiethanolamine, Chemical
Engineering Science, Vol. 50, n° 7, pp. 1071-1079, 1995.
Hermsdorf C., Kather A., Klostermann M., Mieske K., Oxyfuel process for hard coal with
CO2 capture, Fouth Nordic Minisympsosium on Carbon Dioxide Capture and Storage, Helsinki,
8-9 septembre, 2005.
Horng S.-Y., Li M.-H., Kinetics of absorption of carbon dioxide into aqueous solutions of
monoethanolamine + triethanolamine, Industrial and Engineering Chemistry Research, vol. 41,
pp. 257-266, 2002.
Jensen M., Musich M., Ruby J., Steadman E., Harju J., Carbon separation and capture,
Plains CO2 reduction (PCOR) Partnership, EERC-UND, juin 2005.
Jordal K., Anheden M., Yan J., Strömberg L., Oxyfuel combustion for coal-fired power
generation with CO2 capture – opportunities and challenges, 7th International Conference on
Greenhouse Gas Control Technologies, Canada, 5-9 septembre 2004.
Jou F-Y, Mather A., Otto F., Solubility of H2S and CO2 in aqueous methyldiethanolamine
solutions, Industrial and Engineering Chemistry Process Design and Development, 21, pp. 539-
544, 1982.
Jou F-Y, Mather A., Otto F., The solubility of CO2 in a 30 mass percent monoethanolamine
solution, The Canadian Journal of Chemical Engineering, vol. 73, pp. 140-147, Février 1995.
Jou F-Y, Otto F., Mather A., Vapor-Liquid Equilibrium of carbon dioxide in aqueous
mixtures of monoethanolamine and methyldiethanolamine, Industrial and Engineering
Chemistry Research, vol. 33, pp. 2002-2005, 1994.
Kanniche M., Bouallou C., CO2 capture study in advanced integrated gasification combined
cycle, Applied Thermal Engineering, vol. 27, pp. 2693-2702, 2007.
Klaeylé M., Nandjee F., Technologie de gazéification intégrée à un cycle combiné, Technique
de l’Ingénieur, B8920, avril 1997.
Knapp H., Döring R., Oellrich L., Plöcker U., Prausnitz J. M., Vapor-liquid equilibria for
mixtures of low boiling substances, Demecha chemistry data series, vol. 6, 1982.
Ko J-J, Li M-H, Kinetics of absorption of carbon dioxide into solutions of Nmethyldiethanolamine
+ water, Chemical Engineering Science, 55, pp. 4139-4147, 2000.
Kohl A., Nielsen R., Gas purification, Gulf Publishing Company, Houston, 1997.
Kvamsdal H., Jordal K., Bolland O., A quantitative comparison of gas turbine cycles with
CO2 capture, Energy, Vol. 32, pp. 10-24, 2007.
Kvamsdal H., Maurstad O., Jordal K., Bolland O., Benchmarking of gas-turbine cycles with
CO2 capture, 7th International Conference on Greenhouse Gas Control Technologies, Canada,
5-9 septembre 2004.
Laursen T., Andersen S. I., High-pressure vapor-liquid equilibrium for nitrogen + methanol,
Journal of Chemical and Engineering Data, 47; pp. 1173-1174, 2002.
Li Y.-G., Mather A. E., Correlation and prediction of the solubility of carbon dioxide in a
mixed alkanolamine solution, Industrial and Engineering Chemistry Research, 33, pp. 2006-
2015, 1994.
Liao C.-H., Li M.-H., Kinetics of absorption of carbon dioxide into aqueous solutions of
monoethanolamine + N-methyldiethanolamine, Chemical Engineering Science, 57, pp. 4569-
4582, 2002.
Liljedahl G. N., Marion J., Nsakala N., Bozzuto C., Palkes M., Vogel D., Gupta J.C., Guha
M., Johnson H., Plasynski S., Technical and economic feasibility of CO2 capture on an
existing US coal-fired power plant, 2001 International Joint Power Generation Conference, 4-7
juin, New Orleans, 2001.
Littel R.J., van Swaaij W.P.M., Versteeg G.F., Kinetics of carbon dioxide with tertiary
amines in aqueous solution, AIChe Journal, Vol. 36, No. 11, pp. 1633-1640, novembre 1990.
Lozza G., Chiesa P., Natural gas decarbonization to reduce CO2 emission from combined
cycles - Part I: Partial oxidation, Journal of engineering for gas turbines and power, vol. 124,
no.1, pp. 82 – 88, 2002a.
Lozza G., Chiesa P., Natural gas decarbonization to reduce CO2 emission from combined
cycles - Part II: Steam-methane reforming, Journal of engineering for gas turbines and power,
vol. 124, no. 1, pp. 89-95, 2002b.
Ma’mun S., Svendsen H.F., Hoff K.A., Juliussen O., Selection of new absorbents for carbon
dioxide capture, Energy Conversion and Management, 48, pp. 251-258, 2007.
Mandal B.P., Bandyopadhyay S.S., Absorption of carbon dioxide into aqueous blends of 2-
amino-2-methyl-1-propanol and monoethanolamine, Chemical Engineering Science, 61, pp.
5440-5447, 2006.
Mandal B.P., Gupa M., Biswas A.K., Bandyopadhyay S.S., Removal of carbon dioxide by
absorption in aqueous MDEA/MEA and AMP/MEA solutions, Chemical Engineering Science,
56, pp. 6217-6224, 2001.
Marion J., Bozzuto C., Nsakala N., Liljedahl G., Greenhouse gas emissions control by oxygen
firing in circulating fluidized bed boilers: Phase 1 – A preliminary systems evaluation,
ALSTOM POWER INC., Rapport no. PPL-03-CT-09, 15 mai, 2003.
Matta R.K., Mercer G.D., Tuthill R.S., Power systems for the 21st century – “H” gas turbine
combined-cycles, GE Power Systems, GER-3935B, 2000.
Mazaud J.-P., Production des gaz de synthèse, Technique de l’Ingénieur, J5480, 1996.
Monteil J.-M., Centrale à cycle combiné, Technique de l’Ingénieur, BE 8 905, 2003.
Muirbrook N. K., Prausnitz J. M., Multicomponent Vapour-Liquid Equilibriums at High
Pressures. I. Experimental Study of the Nitrogen-Oxygen-Carbon Dioxide System at 0ºC,
AIChE. Journal., 11, pp. 1092-1097, 1965.
Naqvi R., Bolland O., Multi-stage chemical looping combustion (CLC) for combined cycles
with CO2 capture, International Journal of Greenhouse Gas Control, 1, pp. 19-30, 2007.
Nsakala N., Lijedahl G. N., Marion J., Levasseur A. A., Turek D., Chamberland R.,
MacWhinnie R., Morin J.-X., Cohen K., Oxygen-fired circulating fluidized bed boilers for
greenhouse gas emissions control and other applications, Third annual conference on carbon
capture and sequestration, Alexandria, VA, USA, 3-6 mai, 2004.
Pani F., Gaunand A., Cadours R., Bouallou C., Richon D., Kinetics of Absorption of CO2 in
Concentrated Aqueous Methyldiethanolamine Solutions in the Range 296 K – 343 K, Journal of
Chemical and Engineering Data, 42 (2); 353, 1997.
Ramachandran N., Aboudheir A., Idem R., Tontiwachwuthikul P., Kinetics of the
absorption of CO2 in mixed aqueous loaded solutions of monoethanolamine and
methyldiethanolamine, Industrial and Engineering Chemistry Research, 45, pp. 2608-2616,
2006.
Rinker E.B., Ashour S.S., Sandall O.C., Kinetics and Modelling of Carbon Dioxide
Absorption into Aqueous Solutions of N-Methyldiethanolamine, Chemical Engineering
Science, Vol. 50, No. 5, pp. 755-768, 1995.
Roizard C., Wild G., Charpentier J.-C., Absorption avec réaction chimique, Techniques de
l’ingénieur - J 1 079, juin 1997.
Sakwattanapong R., Aroonwilas A., Veawab A., Behavior of reboiler heat duty for CO2
capture plants using regenerable single and blended alkanolamines, Industrial and Engineering
Chemistry Research, 44, pp. 4465-4473, 2005.
Soave G., Feliu J.A., Saving energy in distillation towers by feed splitting, Applied Thermal
Engineering, 22, pp. 889-896, 2002.
Somait F.A., Kidnay A.J., Liquid-vapor equilibriums at 270.00 K for systems containing
nitrogen, methane, and carbon dioxide, Journal of chemical engineering data, 23(4), pp. 301-
305, 1978.
Tan C-S, Chen J-E, Absorption of carbon dioxide with piperazine and its mixtures in a rotating
packed bed, Separation and Purification Technology, 49, pp. 174-180, 2006.
Tarun C.B., Croiset E., Douglas P.L., Gupta M., Chowdhury M.H.M., Techno-economic
study of CO2 capture from natural gas based hydrogen plants, International Journal of
Greenhouse Gas Control, 1, pp. 55-61, 2007.
Thambimuthu K., Davison J., Overview of CO2 capture, 7th International Conference on
Greenhouse Gas Control Technologies, Canada, 5-9 septembre 2004.
Versteeg G.F., van Swaaij W.P.M., Solubility and Diffusivity of Acid Gases (CO2, N2O) in
Aqueous Alkanolamine Solutions, Journal of Chemical and Engineering Data, 32(29), 1988.
Versteeg, G. F., Van Dijck L. A. J., Van Swaaij W. P. M., On the kinetics between CO2 and
alkanolamines both in aqueous and non-aqueous solutions. An overview, Chemical Engineering
Communications, vol. 144, pp. 113-158, 1996.
Vinel D.-J., Modélisation d’une colonne d’absorption de gaz acides par des solutions aqueuses
d’alcanolamines, Thèse de l’Ecole des Mines de Paris, 2003.
Viswanathan R., Romanosky R., Rao U., Purgert R., Johnson H., Boiler Materials for USC
Plant, 17th Annual Conference on Fossil Energy Materials, Pittsburgh, 22-24 avril, 2003.
Wang Y.W., Xu S., Otto F.D., Mather A.E., Solubility of N2O in alkanolamines and in mixed
solvents, The Chemical Engineering Journal, 48, pp 31-40, 1992.
Weber W., Zeck S., Knapp H., Gas solubilities in liquid solvents at high pressures: apparatus
and results for binary and ternary systems of N2, CO2, and CH3OH, Fluid phase equilibria, 18,
pp. 253-278, 1984.
Wilkinson M. B., Boden J. C., Panesar R S., Allam R. J., A study of the capture of carbon
dioxide from a large refinery power station boiler conversion to oxyfuel operation, 5th
International Conference on Greenhouse Gas Control Technologies, Cairns, Australia, 13-16
août, 2000.
Wilkinson M. B., Boden J. C., Panesar R S., Allam R. J., CO2 capture via oxyfuel firing:
optimisation of a retrofit design concept for a refinery power station boiler, First National
Conference on Carbon Sequestration, Washington DC, 15-17 mai, 2001.
Xu G-W., Zhang C-F., Qin S-J., Gao W-H., Liu H-B., Gas-liquid equilibrium in a CO2-
MDEA-H2O system ant the effect of piperazine on it, Industrial & Engineering Chemistry
Research, 74, pp. 1473-1477, 1998.
Yokoyama T., Japanese R&D on large-scale CO2 capture, Conference on Separations
Technology VI: New Perspectives on Very Large-Scale Operations, Kingfisher Resort, Fraser
Island, Queensland, Australia, 2-8 octobre, 2004.
Yorizane M., Yoshimura S., Masuoka H., Miyano Y., Kakimoto Y., New procedure for
vapour-liquid equilibria. Nitrogen + Carbon Dioxide, Methane + Freon 22, and Methane +
Freon 12, Journal of chemical engineering data, 30, pp. 174-176, 1985.
Zeck S., Knapp H., Vapor-liquid and vapor-liquid-liquid phase equilibria for binary and
ternary systems of nitrogen, ethane and methanol: experiment and data reduction, Fluid Phase
Equilibria, 25, pp. 303-322, 1986.
Zenner G. H., Dana L. I., Liquid-Vapour Equilibrium Compositions of Carbon Dioxide-
Oxygen-Nitrogen Mixtures. Chemical Engineering Progress Symposium Series, 59(44), pp. 36-
41, 1963.
Administrateurs de l'archive uniquement : éditer cet enregistrement