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Modelowanie kinetyki reakcji w badaniach metodą TPR katalizatorów tlenkowych

Surman J., Kustrowski P., Chmielarz L., Dziembaj R.

Przemysł Chemiczny

2003

T. 82, nr 8-9

783-785

Oxidative dehydrogenation of n-butane over transition metal containing hydrotalcite derived catalysts.

Kuśtrowski P., Chmielarz L., Węgrzyn A., Surman J., Dziembaj R.

Prace Naukowe Instytutu Chemii i Technologii Nafty i Węgla Politechniki Wrocławskiej. Konferencje

2002

Vol. 10, nr 57

247-252

Mg-Al layered double hydroxides containing carbonates and nitrates in theinterlayer gallery were used as parent materials for anion exchange. NO-3 and CO2-3 anions were exchanged with oxoanions containing vanadium, chromium, molybdenum and tungsten. Ion-exchange in basic solution led to introduction of V2O 4-7, CrO2-4, MoO2-4 and WO2-4 anions, while V10O286-, Cr2O2-7, Mo7O6-24 and W7O6-24 forms were intercalated in acidic solution. The intercalation was confirmed by X-ray diffraction and FTIR spectroscopy. Oxidative dehydrogenation of n-butane was carried out over hydrotalcite-derived catalysts. The catalysts obtained by thermal decompn. of V2O4-7-contg. Hydrotalcites appeared to be the most active ones in a prodn. of 1,3-butadiene. However, the highest yield of butenes was achieved over Mg-Al-Cr oxides catalyst in the low temp. range (Ł550C).

Influence of preparation method of hematite catalyst precursors on their catalytic activity in dehydrogenation of ethylbenzene to styrene

Kuśtrowski P., Surman J., Chmielarz L., Dziembaj R.

Polish Journal of Chemical Technology

2000

Vol. 2, nr 2

27-30

A series of iron oxide based catalysts modified by introduction of chromium Cr, cerium Ce and potassium (KOH or K2CO3) promoters were prepared by coprecipitation method. KOH or K2C03were used as precipitating agents. Calcined catalyst precursors were characterised by XRD (structure) and low temperature Ar-sorption (specific surface area). Activity and selectivity of modified iron oxides were tested in dehydrogenation of ethylbenzene to styrene in fixed-bed microreactor system. Catalytic activity was influenced not only by introduced promoter (Cr, Ce, K) but also by kind of precipitating agent (KOH, K2CO3). The highest styrene yield was observed for iron oxide catalyst modified with cerium and potassium. All studied catalysts showed high selectivity towards styrene (>94%).