Abstract: The invention concerns a method for combined production of hydrogen and carbon dioxide from a mixture of hydrocarbons wherein the residual PSA is treated to produce a carbon dioxide-enriched fluid, and wherein: the residual PSA is compressed to a pressure such that the partial pressure of the CO<SUB>2</SUB> contained ranges between about 15 and 40 bar; the residue is subjected to one or more condensation/separation steps with production of CO<SUB>2</SUB>-rich condensate(s) and a purge of noncondensable gas; the purge of noncondensable gas is preferably treated to produce a H<SUB>2</SUB>-rich permeate which is recycled to the PSA, and a residue which is recycled to syngas generation, Preferably, the condensate(s) are purified by cryogenic distillation to produce food grade CO<SUB>2</SUB>. The invention also concerns an installation for implementing the method.

Abstract: The invention relates to a method for simultaneously producing hydrogen and carbon monoxide consisting in generating a synthesis gas and in processing it by decarbonising and removing water and remaining carbon dioxide by passing said gas through a bed of adsorbents, in separating remaining components by forming at least one H<SUB>2</SUB>-rich flow, a CO flow containing at least one type of impurity selected from nitrogen and argon, a methane-rich purge gas flow and a flash gas flow. The inventive method also consists in regenerating the bed of adsorbents by passing a regeneration gas comprising at least one non-zero proportion of the formed H<SUB>2</SUB>flow and in recycling at least the purge and flash gases for feeding the synthesis gas generation stage.

Abstract: A method of limiting the bit rate going to a network service having a target bit rate, data packet traffic to the service coming from at least one contributor, and a bit rate being associated with the portion of the traffic coming from said contributor. The method includes sending the packet from the contributor to the service if the bit rate of the traffic of the contributor is below a threshold that is a function of the target bit rate and a current data packet traffic to said service, the bit rate of the traffic from the contributor being measured on the current data packet traffic.

Abstract: The invention relates to a method for utilizing a combustible gas product collected in the seal device of a compressor of the said combustible gas product, comprising the steps of: a) feeding the seal device of the said compressor with an inert gas flow, b) recovery at the outlet of the said seal device of a gas flow containing all or part of the inert gas flow of step a) and all or part of the gas flow of combustible product collected in the said compressor seal device, to supply a line connected to the outlet of the seal device, c) separation of the said gas flow (mixture of inert gas and the gas flow of combustible product) at the outlet of the said line into two gas flows, the first being intended to feed a fuel header connected to burners, and the second being sent to a flare to be burned (the lines conveying the gas flows of steps b) and c) constituting the leak circuit). The pressure in the seal device is maintained at a pressure above the gas pressure in the fuel header.

Abstract: A method of producing a synthesis gas which contains hydrogen and carbon dioxide. A hydrocarbon mioxture is pre-reformed to create a first mixture. The first mixture is then reformed in a catalytic ceramic membrane reactor (RCMC) with oxidizing an oxidizing mixture to form a raw synthesis gas. The oxidizing mixture contains oxygen, and the raw synthesis gas contains hydrogen, carbon monoxide, carbon dioxide, water, and an oxygen depleted mixture. Several of the process streams are also preheated. The oxidizing mixture is brought to a temperature between 871° C. and 1300° C. prior to the formation of the raw synthesis gas.

Abstract: 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.