Method for producing carbon monoxide by reverse conversion with an adapted catalyst
OwnerRene Dupont, Pierre Gauthier +1inventors
InventorsRene Dupont, Pierre Gauthier, Pascal Marty
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OwnerRene Dupont, Pierre Gauthier +1inventors
InventorsRene Dupont, Pierre Gauthier, Pascal Marty
Estimating the term…
The invention concerns a method for producing carbon monoxide by reverse conversion, in gas phase, of carbonic acid gas and gaseous hydrogen while minimising the production of methane. The invention is characterised in that the reaction is carried out at a temperature between 300 and 520° C. and under pressure between 10 to 40 bars in the presence of an iron-free catalyst based on zinc oxide and chromium oxide. Said method is preferably carried out continuously and comprises preferably the following steps which consist in: a) preparing a gas mixture rich in carbon dioxide and in hydrogen having a temperature between 300 and 520° C.: b) reacting said gas mixture, forming carbon monoxide and water vapour, by passing said mixture through a catalytic bed based on zinc oxide and chromium oxide maintained under pressure between 10 and 40 bars; c) cooling the gas flux derived from the catalytic bed so as to cause condensation of all or part of the water vapour formed; d) separating the condensed water from said gas fluid; e) optionally, re-treating at least once the resulting gas stream. previously brought to a temperature between 300 and 520° C., by performing steps b) to d) above, so as to increase the proportion of carbon monoxide in the gas stream, each step b) being carried out in a different catalytic bed.
A process for the production of carbon monoxide by reverse conversion, in the gas phase, of gaseous carbon dioxide and gaseous hydrogen, while minimizing the production of methane, characterized in that the reaction is carried out at a temperature of 300 to 520° C. and at a pressure of 10 to 40 bar in the presence of a catalyst based on zinc oxide and chromium oxide and not containing iron.
The process as claimed in either of the preceding claims, characterized in that the weight ratio of zinc oxide to chromium oxide is between 1.5 and 4.5, preferably between 1.5 and 2.5.
The process as claimed in any one of the preceding claims, characterized in that it is carried out continuously and in that it comprises the step consisting in making a gas mixture rich in hydrogen and carbon dioxide pass at a temperature of 300 to 520° C. through a catalyst bed furnished with said catalyst.
The process as claimed in any one of the preceding claims, characterized in that the reaction is carried out at a pressure of 15 to 25 bar.
The process as claimed in any one of the preceding claims, characterized in that it furthermore includes the step consisting in separating the steam contained in the gas mixture, produced during the reaction, by condensation.
The process a claimed in any one of the preceding claims, characterized in that the steam formed is separated from the mixture progressively as it is formed.
Dependencies are inferred from the claim text.