✦ LIBER ✦

Kinetics of the catalytic oxidation ofp-phenetidine with chlorate and the role of the catalyst vanadium(V)

✍ Scribed by P. R. Bontschev; B. G. Jeliazkowa

Publisher: Springer
Year: 1967
Tongue: English
Weight: 398 KB
Volume: 55
Category: Article
ISSN: 0026-3672
DOI: 10.1007/bf01216489

No coin nor oath required. For personal study only.

📜 SIMILAR VOLUMES

Mechanism of the catalytic oxidation ofp

Mechanism of the catalytic oxidation ofp-phenetidine and some phenols with chlorate in the presence of vanadium (V) as catalyst

✍ P. R. Bontschev; B. G. Jeliazkowa 📂 Article 📅 1967 🏛 Springer 🌐 English ⚖ 420 KB

Kinetics of the Oxidation of Triethanola

Kinetics of the Oxidation of Triethanolammonium Ion with Vanadium (V)

✍ P. O. I. Virtanen; M. Puutio 📂 Article 📅 2010 🏛 Wiley (John Wiley & Sons) ⚖ 48 KB 👁 1 views

Kinetics of the catalytic oxidation of n

Kinetics of the catalytic oxidation of naphthalene over V2O5 using a spinning catalyst basket reactor

✍ G.L. Ross; P.H. Calderbank 📂 Article 📅 1971 🏛 Elsevier Science 🌐 English ⚖ 500 KB

The kinetics of the oxidation of naphthalene to phthalic anhydride were studied at high levels of conversion between 330 and 420°C using a commercial vanadium catalyst. Some departures from the simple redox model were observed.

Kinetics of the selective catalytic redu

Kinetics of the selective catalytic reduction of nitric oxide with ammonia on a platinum catalyst

✍ H. Meier; G. Gut 📂 Article 📅 1978 🏛 Elsevier Science 🌐 English ⚖ 814 KB

The Role of Bulk Oxide Ion in the Cataly

The Role of Bulk Oxide Ion in the Catalytic Oxidation Reaction over Metal Oxide Catalyst

✍ Yoshihiko Moro-oka; Wataru Ueda; Kang-Hee Lee 📂 Article 📅 2003 🏛 John Wiley and Sons ⚖ 52 KB 👁 2 views

Kinetics of the catalytic air oxidation

Kinetics of the catalytic air oxidation of o-xylene over a commercial V2O5-TiO2 catalyst

✍ J. Skrzypek; M. Grzesik; M. Galantowicz; J. Soliński 📂 Article 📅 1985 🏛 Elsevier Science 🌐 English ⚖ 836 KB

The gas-phase oxidation of o-xylene over a commercial V205-Ti02 catalyst was studied in tied bed non-isothermal reactor. The experiments were carried out at initial o-xylene concentrations which differed greatly from each other. The following reaction network was suggested.