The Infona portal uses cookies, i.e. strings of text saved by a browser on the user's device. The portal can access those files and use them to remember the user's data, such as their chosen settings (screen view, interface language, etc.), or their login data. By using the Infona portal the user accepts automatic saving and using this information for portal operation purposes. More information on the subject can be found in the Privacy Policy and Terms of Service. By closing this window the user confirms that they have read the information on cookie usage, and they accept the privacy policy and the way cookies are used by the portal. You can change the cookie settings in your browser.
The catalytic cracking of ginger oil in a fixed-bed tubular reactor with a weight hourly space velocity 1.0h −1 at temperatures ranging from 300°C to 450°C has been accomplished over zeolites MFI, BEA, and FAU having different SiO 2 /Al 2 O 3 ratios. Gasoline fraction yields have been observed along with liquid, gas, and coke yields. Trends in the various yields have...
The catalytic conversion of canola oil was performed at atmospheric pressure with a weight hourly space velocity of 1.0h −1 in a fixed-bed reactor at temperatures of 400°C and 450°C over MFI, BEA, and FAU, and with different SiO 2 /Al 2 O 3 ratios for BEA and FAU. Simulated distillation of the organic liquid product showed that MFI gave the highest gasoline range product...
Gallosilicates isostructural with MFI ([Ga]MFI) with different SiO 2 /Ga 2 O 3 molar ratios were prepared by hydrothermal synthesis and subsequent calcination and conversion to the proton form. Microbalance weight loss determinations both upon H 2 reduction of the calcined [Ga]MFIs and upon reduction of the same materials mechanically mixed with β-Ga 2 O ...
Set the date range to filter the displayed results. You can set a starting date, ending date or both. You can enter the dates manually or choose them from the calendar.