« Volver Ficha del Documento

Proceedings of the 1986 International Congress on Renewable Energy Sources. Methanol catalytic synthesis from biomass gases : optimization of the process. International Congress on Renewable Energy Sources [18-23 Mayo 1986, Madrid].

1987

V.1
CIENA
1113

84-00-6673-1

From experimental results obtained with (CO + 2 H2) mixtures under 50 bar on metallic catalyst (Cu - Zn) (1)(2)(3) complete stoechiometric equations were established and also thermal balance of the reaction. Influence of internal and external diffusion was shown. The whole of this study has permitted to define and to realise a reactor with two catalytic successive beds which permit to study the following parameters. -influence of preheating synthesis gases upon carbon monoxide conversion, - evolution of temperature from differents points of catalytic bed; - evolution of several gases concentration out from the reactor. This reactor permits to us in a first step with (CO + 2 H2) mixtures to study the catalyst in adiabatic conditions and to follow desactivation of the catalyst during the time. In a second step to define for our catalyst, optimun conditions for synthesis catalytic reaction of methanol, principally concerning carbon monoxide conversion rate. INTRODUCTION. EXPERIMENTAL PLANT DESIGN AND OPERATION. STARTING OF SYNTHESIS REATION. INFLUENCE OF CARBON DIOXIDE CONCENTRATION IN SYNTHESIS GAS ON CONVERSION RATE. CONCLUSIONS. REFERENCES.

Presenta gráfs.

Ministerio de Ambiente y Energía. Secretaría de Planificación del Sub-Sector Energía - Centro de Información de Energía y Ambiente, CIENA

Grettel Ruiz Matarrita

Calle 25, Avenidas 8 y 10. San José, Costa Rica

(506)25476900 - 25476239

De lunes a viernes de 8 a.m. a 12m.


Dirección: Av. Mariscal Antonio José de Sucre N58-63 y Fernández Salvador Edif. Olade - San Carlos, Quito - Ecuador.

Web: www.olade.org

Teléfonos: (593 2) 259 8122 / 2598 280

Correo: realc@olade.org

ADMIN
Desarrollado por: Aikyu-Systems