An analysis of the ignition of premixed gases by a hot spherical surface with catalytic reforming reaction*

By Fu W.-B.   Hou L.-Y.   Zhong B.-J.   Ma F.-H.   Qin C.   Li C.-L.  

Fuel, Vol. 82, Iss. 5, 2003-03 ,pp. : 539-544

Elsevier

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Experimental and numerical study on the combustion characteristics of partially premixed charge compression ignition engine with dual fuel *

By Lee C.S.   Lee K.H.   Kim D.S.  

Fuel, Vol. 82, Iss. 5, 2003-03 ,pp. : 553-560

Elsevier

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An experimental study of biomass ignition *

By Grotkjaer T.   Dam-Johansen K.   Jensen A.D.   Glarborg P.  

Fuel, Vol. 82, Iss. 7, 2003-05 ,pp. : 825-833

Elsevier

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Estimation of concentration and temperature profiles for methane-steam reforming reaction in a porous catalyst

By Levent M.   Budak G.   Karabulut A.  

Fuel Processing Technology, Vol. 55, Iss. 3, 1998-06 ,pp. : 251-263

Elsevier

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Methanol steam reforming in supported Pd membrane reactor The supported Pd membrane is promising for the production of high-purity hydrogen from catalytic steam reforming of methanol. At the 35 o C reaction temperature, the catalyst activity and stability are promoted by increasing the alumina content. Here a compact doublejacketed reactor has generated high-purity hydrogen directly from steam reforming of methanol, with no need for external purification and a much higher recovery yield.

By  

Fuel Cells Bulletin, Vol. 4, Iss. 37, 2001-10 ,pp. : 12-12

Elsevier

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