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Separacja wybranych kwaśnych składników mieszanin gazowych z wykorzystaniem zjawiska hydratacji

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Warianty tytułu
EN
Separating selected acid components of gas mixtures using the hydratation phenomenon
Języki publikacji
PL
Abstrakty
EN
Possibilities of gases" separation by hydrates" crystallization. Characteristics of acid gases" hydrates. Features essential for hydrates" structures. Carbohydrate effect. Separation of acid gases.
Rocznik
Tom
Strony
2--9
Opis fizyczny
Bibliogr. 46 poz.
Twórcy
autor
  • Polskie Górnictwo Naftowe i Gazownictwo S.A. w Warszawie, Oddział w Sanoku, Dział Eksploatacji Gazu Ziemnego, ul. Sienkiewicza 12, 38-500 Sanok
Bibliografia
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  • [2] Warowny W., Kwiecień K.: Suchy reforming gazu ziemnego, IX Krajowa Konferencja GAZTERM 2006, Międzyzdroje 22-24 maja 2006.
  • [3] Warowny W.: Hydraty, Gaz, Woda i Technika Sanitarna, 2001, 75 (3), 88-94.
  • [4] Sloan Jr, E. D.: Clathrate Hydrates of Natural Gases, Marcel Dekker, Inc., 1998.
  • [5] Carroll J.: Natural gas hydrates, A guide for engineers Gulf Professional Publishing, 2003.
  • [6] Warowny W., Lorenc M.: Hydraty w transporcie i magazynowaniu gazu ziemnego, artykuł wysłany do druku w Gaz, Woda i Technika Sanitarna, 2006.
  • [7] Warowny W.: Wprowadzenie do wiedzy o gazohydratach (raczej hydratach), Seminarium Wydziałowe, Politechnika Warszawska, Wydział BMiP (www.ich.pw.plock.pl- aktualności/rok akademicki 2003/2004)
  • [8] Lubaś J.: Doświadczalno-teoretyczne studium zjawisk powstawania i dysocjacji hydratów gazu ziemnego, Instytut Nafty i Gazu w Krakowie Oddział w Krośnie, 2002.
  • [9] I-Ming Chou i inni, Transformations in methane hydrates, PNAS USA, 2000, 97(25), 13484-13487.
  • [10] Warowny W., Lorenc M.: Zastosowanie hydratów w transporcie gazu ziemnego, IX Krakowa Konferencja GAZTERM, Międzyzdroje, 2006.
  • [11] Robson R.: New clathrate structure shows promise for H2 storage, Fuel Cell Today, (www.fuelcelltoday.com), 2004.
  • [12] Gudmundsson J. S., i inni: Hydrate concept for capturing associated gas, SPE 50598, 1998.
  • [13] Mork M., Gudmundsson J. S.: Hydrate formation rate in a continuous stirred tank reactor: experimental results and bubble-to-crystal model, Proceedings of the Fourth International Conference on Gas Hydrates, Yokohama, Japan, 2002 May, 19-23.
  • [14] Mork M.: Formation rate of natural gae hydrate - Reactor experiments and models, Praca doktorska, Norwegian University of Science and Technology, 2002.
  • [15] Carroll J. J.: Physical properties relevant to acid gas injection, Venezuelan Gas Processors Association (AVPG), XIV International Gas Convention, May 10-12, 2000.
  • [16] Boyle T. B., Carroll J. J.: Calculation of acid gas density in the vapor, liquid, and dense-phase regions, (www.gasliquids.com/papers.html), 2001
  • [17] Warowny W., Mather A. E.: A new approach to substance dependent tree-parameter cubic equation of state, Inżynieria Chemiczna i Procesowa, 1999, 21, 281-297..
  • [18] Carroll J. J.: Phase equilibria relevant to acid gas injection, Part l - Non-aqueous phase behaviour, (www.gasliquids.com/papers.html), 2002, 41, No. 6.
  • [19] Carroll J. J.: Phase equilibria relevant to acid gas injection, Part 2 - Aqueous phase behaviour, (www.gasliquids.com/papers.html), 2002, 41, No. 7.
  • [20] Sun C. Y., i inni: Hydrate formation conditions of sour natural gases, J. Chem. Eng., 2003, 48, 600-602.
  • [21] Carroll J. J.: An examination of the prediction of hydrate formation conditions in sour natural gas, GPA Europe, Spring Meeting, Dublin, Ireland, May 19-21, 2004.
  • [22] Řstergaard K. K., i inni: Hydrate phase equilibria of a near critical fluid: effect of inhibition and separation, AIChE Journal, 2001, 47, No. 7.
  • [23] Warowny W, i inni: Wyznaczanie punktu rosy wody w gazie ziemnym, Gaz, Woda i Technika Sanitarna, 2003, 77 (7-8), 236-243.
  • [24] Carroll J. J., Maddocks J.: Design considerations for acid gas injection, Laurance Reid Gas Conditioning Conference, Norman Oklahoma, (www.gasliquids. com/papers.html), 1999.
  • [25] Carroll J. J.: The water content of acid gas and sour gas from 100° to 220°F and pressures to 10,000 psia, Calgary, Alberta, Canada, (www.gasliquids.com/pa-pers.html), 2002.
  • [26] Grynia E., Carroll J. J.: Zatłaczanie gazu kwaśnego do złoża, (www.gasliqids.com/papers.html), 2004.
  • [27] Ng H.-J. I i inni: Impact of thermophysical properties research on acid gas injection process design, (www.gasliquids.com/papers.html), 1999.
  • [28] Rahimi N., Griffin P. J.: Potential for acid gas injection at Kharg Island, Calgary, Alberta, Canada, (www. gasliquids. com/papers. html), 2004.
  • [29] Maddocks J. R., Whiteside D.: Acid gas injection: an operator's perspective, Calgary, Alberta, Canada, (www.gasliquids.com/papers.html), 2004.
  • [30] Tanner M. R.: U. S. Patent No. 4,409,102, Process for removing contaminants from a stream of methane gas, Central Plants Inc. Culver City, Calif, 1983.
  • [31] Paulsen D. C. i inni: U. S. Patent No. 6,881,389 B2, Removal of H2S and CO2 from a hydrocarbon fluid stream, EDG, Inc., Metairie, LA (US), 2005.
  • [32] Wong S., Bioletti R.: Carbon Dioxide separation technologies, Carbon & Energy Management, Alberta Research Council, Edmonton, Alberta, T6N 1E4, Canada, (www.aidis.org.br), 2002.
  • [33] Carroll J. J.: Problem is the result of industry's move to use higher pressures, Calgary, Alberta, Canada, (www.gasliquids.com/papers.html), 2003.
  • [34] Shiojiri K.: A new process for the separation of condensable greenhouse gases by the formation of clathrate hydrates, VISION, The bimonthly e-journal of the World Student Community for Sustainable Development, (www.wscsd.org/ejo-urnal/), 2004.
  • [35] Elliot D. G. i inni: U. S. Patent No. 5,660,603, Process for separating selected components from multi-component natural gas streams, International Process Services, Inc. Huston, Tex., 1997.
  • [36] Lee H. i inni: U. S. Patent No. 6,602,326 B2, Method for separation of gas constituents employing hydrate promoter, Korea Advanced Institute of Science and Technology (KR), 2003.
  • [37] Hnatow M. A., Happel J.: U. S. Pat. No. 5,434,330, Process and apparatus for separation of constituents of gases using gas hydrates, 1995.
  • [38] Spencer D. F.: U. S. Pat. No. 5,700,311, Methods of selectively separating CO2 from a multicomponent gaseous stream, 1997.
  • [39] Quinn R. i inni: Hydrogen sulfide separation from gas streams using salt hydrate chemical absorbents and immobilized liquid membranes, Separation Science and Technology, 2002, 37 (3), 627-638.
  • [40] Kamata Y. i inni: Hydrogen sulfide separation using tetra-n-butyl ammonium bromide semi-clathrate (TBAB) hydrate, Energy & Fuels, 2005, 19, 1717-1722.
  • [41] Vorotyntsev V. M. i inni: Separation of gas mixtures by the gas hydrate crystallization method, Theoretical Foundations of Chemical Engineering, 2001, 35, No. 2, 119-123.
  • [42] Vorotyntsev V. M. i inni: Separation of gas mixtures by continuous gas hydrate crystallization, Theoretical Foundations of Chemical Engineering, 2001, 35, No. 5, 513-515.
  • [43] Tajima H. i inni: Energy consumption estimation for greenhouse gas separation processes by clathrate hydrate formation, Energy 2004, 29, 1713-1729.
  • [44] Warowny W., Demusiak G.: Gaz ziemny w technologiach ogniw paliwowych, Wiadomości Chemiczne, w serii Biblioteka, Ogniwa paliwowe - nowe kierunki rozwoju (ed. H. Drulis i inni), 219-235 (2005).
  • [45] Hefner III R. A.: The age of energy gases, International Journal of Hydrogen Energy, 2002, 27, 1-9.
  • [46] International Energy Agency, World Energy Outlook 2004, www.igu.org/data--base/
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPP1-0068-0024
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