𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Dehydrogenation of hydroxymatairesinol to oxomatairesinol over carbon nanofibre-supported palladium catalysts

✍ Scribed by Heidi Markus; Arie J. Plomp; Thomas Sandberg; Ville Nieminen; Johannes H. Bitter; Dmitry Yu. Murzin


Publisher
Elsevier Science
Year
2007
Tongue
English
Weight
516 KB
Volume
274
Category
Article
ISSN
1381-1169

No coin nor oath required. For personal study only.


πŸ“œ SIMILAR VOLUMES


Oxidative carbonylation of phenol to dip
✍ Ho Young Song; Eun Duck Park; Jae Sung Lee πŸ“‚ Article πŸ“… 2000 πŸ› Elsevier Science 🌐 English βš– 113 KB

Oxidative carbonylation of phenol to form diphenyl carbonate DPC was investigated in the multi-step electron transfer system containing homogeneous or heterogeneous palladium as the main component. Carbon-supported Pd catalyst showed a Ε½ . better DPC yield than the best homogeneous system with Pd OA

Dehydrogenation of ethylbenzene with car
✍ Do-Young Hong; Vladislav P. Vislovskiy; Young Kyu Hwang; Sung Hwa Jhung; Jong-Sa πŸ“‚ Article πŸ“… 2008 πŸ› Elsevier Science 🌐 English βš– 468 KB

Alumina-supported V 0.43 Sb 0.57 oxide (VSb/Al) and MgO-modified alumina-supported V 0.43 Sb 0.57 oxide catalysts (VSb/Mg n Al with Mg/Al atomic ratio, n = 0.1, 0.3 or 0.5) have been tested for the dehydrogenation of ethylbenzene with carbon dioxide as an oxidant. Their catalytic behaviors were inte

Asymmetric synthesis of (S)-alkylamines
✍ S GΓΆbΓΆlΓΆs; E Tfirst; J.L Margitfalvi; K.S Hayes πŸ“‚ Article πŸ“… 1999 πŸ› Elsevier Science 🌐 English βš– 517 KB

and benzyl-esters of L-alanine introduced either by incipient wetness impregnation or by equilibrated impregnation onto the catalyst surface. In the first step of the transamination the Schiff base was formed from the ketone and aralkylamine which was then hydrogenated to secondary amine in the seco

Carbon dioxide reforming of methane to s
✍ Z.L. Zhang; X.E. Verykios πŸ“‚ Article πŸ“… 1994 πŸ› Elsevier Science 🌐 English βš– 451 KB

Carbon dioxide reforming of methane to synthesis gas has been investigated over supported Ni catalysts in the temperature range of 5004350Β°C. Addition of CaO ( 10 mol%) promoter to the Nil y-A1203 resulted in an increase of reaction rate and an improvement of catalyst stability, which may be related