[1] وافری، بهزاد ؛ کرمی، حمیدرضا ؛ کریمی، غلامرضا؛
مدلسازی فرایند ریفرمینگ گازطبیعی با بخار آب در راکتور غشایی پالادیم ـ نقره برای تولید هیدروژن خالص،
نشریه شیمی و مهندسی شیمی ایران، (3)
30: 25 تا 37 (1390).
[4] خواجه نوری، مسعود؛ رضایی، مهران؛ مشکانی، فرشته؛
بررسی تأثیر مواد فعال سطحی بر ساختار و فعالیت کاتالیست نیکل بر پایه منیزیم اکسید در فرایند ریفرمینگ خشک متان،
نشریه شیمی و مهندسی شیمی ایران، (1)
35: 71 تا 81 (1395).
[7] Gobina E.N., Oklany J.S., Houghes R.,
Elimination of Ammonia from Coal Gasification Streams by Using a Catalytic Membrane Reactor, Industrial & Engineering Chemistry Research,
34: 3777-3783 (1995).
[8] Temkin M., Pyzhev V.,
Kinetics of the Synthesis of Ammonia on Promoted Ion Catalysts,Acta Physicochim, 12: 327-356 (1940).
[9] Harrison R.H., Kobe K.A.,
Thermodynamics of Ammonia Synthesis and Oxidation, Chemical Engineering Progress,
49: 349-353 (1953).
[13] Rahimpour M.R., Jamshidnejad Z., Jokar S.M., Karimi G., Ghorbani A., Mohammadi A.H.,
A Comparative Study of Three Different Methods for Flare Gas Recovery of Asalooye Gas Refinery, Journal of Natural Gas Science and Engineering,
4: 17-28 (2012).
[15] Fazeli A., Fatemi S., Mahdavian M., Ghaee A.,
Mathematical Modeling of an Industrial Naphtha Reformer wif Three Adiabatic Reactors in Series,Iranian Journal of Chemistry and Chemical Engineering (IJCCE),
28: 97-102 (2009).
[16] Mohammadikhah R., Zahedi Abghari S., Ganji H., Ahmadi Marvast M.
, Improvement of Hydrodynamics Performance of Naphtha Catalytic Reforming Reactors Using CFD,Iranian Journal of Chemistry and Chemical Engineering (IJCCE),
33: 63-76 (2014).
[17]Eg and G Technical Services. Inc. ""
Fuel Cell Handbook", 2004.
[18]
Yakabe H., Ogiwara T., Hishinuma M., Yasuda me.
, 3-D model calculation for planar SOFC, Journal of Power Sources,
102: 144-154 (2001).
[20] Peters R., Dahl R., Kluttigen U., Palm C., Stolten D.,
Internal Reforming of Methane in Solid Oxide Fuel Cell Systems,Journal of Power Sources,
106: 238-244 (2002).
[23] Saadatjou1 N., Jafari A., Sahebdelfar S.,
Synthesis and Characterization of Ru/Al2O3 Nanocatalyst for Ammonia Synthesis, Iranian Journal of Chemistry & Chemical Engineering (IJCCE), 34: 1-9 (2015).
[25] Haberman B.A., Young J.B., Three-Dimensional Simulation of Chemically Reacting Gas Flows in the Porous Support Structure of an Integrated -Planar Solid Oxide Fuel Cell, menternational Journal of Heat and Mass Transfer, 47: 3617-3629 (2004).
[26] Smith J.M., Van Ness H.C., Abbot M.M., “Chemical Engineering Thermodynamics”, New York: McGrow Hill,Inc, (1996).
[27] Hajimolana S.A., Hussain M.A., Wan Daud M.WA., Soroush M., Shamiri A., Mathematical Modeling of Solid Oxide Fuel Cells: A Review, Renewable & Sustainable Energy Reviews, 15: 1893-1917 (2011).
[28] Patcharavorachot Y., Peangjuntuek W., Assabumrungrat S., Arpornwichanop A., Performance Evaluation of Combined Solid Oxide Fuel Cells wif Different Electrolytes,International Journal of Hydrogen Energy, 35: 4301-4310 (2010).
[29] Treybal R.E., “Mass-Transfer Operations”, New York: McGraW Hill Inc, (1980).
[30] Perry R.H., Green D.W., “Perry ’s Chemical Engineering Handbook”, 7th ed., New York, (1997).