Search Results - "Soerijanto, H."

Steam reforming of methanol over copper-containing catalysts: Influence of support material on microkinetics by Frank, B., Jentoft, F.C., Soerijanto, H., Kröhnert, J., Schlögl, R., Schomäcker, R.

“…Steam reforming of methanol (SRM) was investigated over copper-containing catalysts supported on four different oxides and mixed oxides: Cu/ZnO/Al 2O 3, Cu/ZrO…”
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CO formation/selectivity for steam reforming of methanol with a commercial CuO/ZnO/Al2O3 catalyst by PURNAMA, H, RESSLER, T, JENTOFT, R. E, SOERIJANTO, H, SCHLÖGL, R, SCHOMÄCKER, R

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Steam reforming of methanol over Cu/ZrO2/CeO2 catalysts: a kinetic study by MASTALIR, A, FRANK, B, SZIZYBALSKI, A, SOERIJANTO, H, DESHPANDE, A, NIEDERBERGER, M, SCHOMÄCKER, R, SCHLÖGL, R, RESSLER, T

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The impact of nitrogen mobility on the activity of zirconium oxynitride catalysts for ammonia decomposition by Soerijanto, H., Rödel, C., Wild, U., Lerch, M., Schomäcker, R., Schlögl, R., Ressler, T.

“…A zirconium oxynitride catalyst was used for the decomposition of ammonia to hydrogen and nitrogen. The onset of catalytic activity at ∼550 °C coincided with…”
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Steam reforming of methanol over Cu/ZrO/CeO catalysts: a kinetic study by MASTALIR, A, FRANK, B, SZIZYBALSKI, A, SOERIJANTO, H, DESHPANDE, A, NIEDERBERGER, M, SCHOMACKER, R, SCHLOGL, R, RESSLER, T

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Katalysatoren für die Erzeugung von Wasserstoff aus Methanol und Ammoniak by Schomäcker, R., Frank, B., Soerijanto, H., Lerch, M., Schlögl, R.

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Steam reforming of methanol over Cu/ZrO 2/CeO 2 catalysts: a kinetic study by Mastalir, A., Frank, B., Szizybalski, A., Soerijanto, H., Deshpande, A., Niederberger, M., Schomäcker, R., Schlögl, R., Ressler, T.

“…Steam reforming of methanol (SRM) was investigated over Cu/ZrO 2/CeO 2 (CZC) catalysts prepared via a novel synthetic method based on coprecipitation and…”
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Zirconium oxynitride catalysts for ammonia decomposition by Soerijanto, H., Rödel, C., Wild, U., Lerch, M., Schomäcker, R., Schlögl, R., Ressler, T.

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CO formation/selectivity for steam reforming of methanol with a commercial CuO/ZnO/Al 2O 3 catalyst by Purnama, H, Ressler, T, Jentoft, R.E, Soerijanto, H, Schlögl, R, Schomäcker, R

“…A study of CO formation for steam reforming of methanol on a commercial CuO/ZnO/Al 2O 3 catalyst has been performed in the temperature range 230–300 °C and at…”
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Katalysatoren für die Erzeugung von Wasserstoff aus Methanol und Ammoniak by Schomäcker, R., Frank, B., Soerijanto, H., Lerch, M., Schlögl, R.

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