초록 ▼

The invention relates to a process for catalytic autothermal steam reforming of alcohols having two or more carbon atoms by directing a preheated educt or reactant mixture of the alcohols, oxygen and water or steam over a catalyst. The process is conducted in an adiabatic manner wherein the catalyst

The invention relates to a process for catalytic autothermal steam reforming of alcohols having two or more carbon atoms by directing a preheated educt or reactant mixture of the alcohols, oxygen and water or steam over a catalyst. The process is conducted in an adiabatic manner wherein the catalyst comprises at least one platinum group metal on an oxidic support selected from the group consisting of aluminum oxide, silicon dioxide, titanium dioxide or mixed oxides thereof and zeolites, and that the educt or reactant mixture contains additional hydrocarbons, which are reformed at the same time as the alcohols.

대표청구항 ▼

1. A process for catalytic autothermal steam reforming of alcohols having two or more carbon atoms comprising directing a preheated reactant mixture of the alcohols, oxygen and water or steam over a catalyst, in which the process is conducted in an adiabatic manner, wherein the catalyst comprises at

1. A process for catalytic autothermal steam reforming of alcohols having two or more carbon atoms comprising directing a preheated reactant mixture of the alcohols, oxygen and water or steam over a catalyst, in which the process is conducted in an adiabatic manner, wherein the catalyst comprises at least one platinum group metal on an oxidic support selected from the group consisting of aluminum oxide, silicon dioxide, titanium dioxide or mixed oxides thereof and zeolites, and wherein the reactant mixture contains additional hydrocarbons, which are reformed at the same time as the alcohols.2. The process according to claim 1, wherein the preheated reactant mixture comprises about 0.5 to about 10 wt. % hydrocarbons, based on the total weight of alcohols and hydrocarbons.3. The process according to claim 2, wherein the hydrocarbons are diesel fuels.4. The process according to claim 2, wherein the hydrocarbons are gasoline.5. The process according to claim 2, wherein the hydrocarbons also comprise aromatic hydrocarbons in addition to long-chain hydrocarbons.6. The process according to claim 1, wherein the alcohols mostly or completely consist of ethanol.7. The process according to claim 1, wherein the catalyst additionally comprises at least one oxide selected from the group consisting of boric oxide, bismuth oxide, gallium oxide, alkali metal oxides, alkaline earth metal oxides, oxides of subgroup elements and rare earth metal oxides in a concentration of up to about 40 wt. % based on the total weight of the catalyst composition.8. The process according to claim 1, wherein the catalyst comprises rhodium in a concentration of about 0.1 to about 2 wt.-%, based on total weight of the catalyst composition.9. The process according to claim 8, wherein the catalyst additionally comprises platinum and/or palladium in a ratio of rhodium to platinum and/or palladium of between about 20:1 to about 2:1.10. The process according to claim 8, wherein the aluminum oxide is used as support for rhodium and optionally platinum/palladium.11. The process according to claim 10, wherein the catalyst additionally comprises cerium oxide.12. The process according to claim 11, wherein the catalyst is coated on a carrier.13. The process according to claim 12, wherein the carrier is a monolithic honeycomb ceramic or metal carriers, open-cell ceramic or metallic foam bodies, metal sheets or irregularly shaped elements.14. The process according to claim 1, wherein the preheated reactant mixture is selected such that at the outlet of the catalyst the temperature is between about 600 and about 800° C.15. The process according to claim 13, wherein the reactant mixture has a steam to carbon ratio that is adjusted to between about 0.5 and about 4.