Abstract: The invention relates to a cyclical method for producing a nitrogen fraction, the purity of which is greater than or equal to 95 mol %, and a hydrocarbon-enriched fraction from a filler containing nitrogen and a hydrocarbon, said method using a specific class of porous hybrid solids as an adsorbent in a pressure-swing adsorption (PSA) process. The invention also relates to equipment for implementing said method.

Abstract: The invention relates to a cyclical method for producing a nitrogen fraction, the purity of which is greater than or equal to 95 mol %, and a hydrocarbon-enriched fraction from a filler containing nitrogen and a hydrocarbon, said method using a specific class of porous hybrid solids as an adsorbent in a pressure-swing adsorption (PSA) process. The invention also relates to equipment for implementing said method.

Abstract: The invention is drawn to a cyclic pressure swing adsorption (PSA) process to recover an off-gas stream at high pressure with low energy consumption. Each cycle of said process comprises a blowdown phase consisting in lowering the pressure in an adsorbent bed from Phigh to Plow, wherein said blowdown phase is divided into several partial blowdown phases, wherein the gas streams discharged during the partial blowdown phases are introduced into respective discharge tanks.

Abstract: The present invention discloses a device, which uses membranes, capable of separating olefins from paraffins. The device (1) considers an ultramicroporous ceramic membrane module, zeolite or silicate based, containing a fixed carrier of copper I or silver ions (#-complexant ions) inserted by ion exchange, or as a monolayer of CuCl, AgNO3, Cu or Ag+ (2). Olefins have higher diffusivity and affinity to the membrane than the remaining species, therefore the bicomponent permeation selectivity becomes reinforced when compared to the ideal permeation selectivity. The purification of olefins by removal of dienes and/or alkynes, is accomplished with a zeolite membrane functionalized with Ag+ and having a specific catalyst in the permeate side (4), e.g. palladium nanoparticulated, for catalyzing the hydrogenation of the permeating dienes and alkynes to the corresponding olefins, thus increasing the selectivity and the driving force of the separation.