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Method and apparatus for treating a gas by adsorption. A gas is compressed and then treated by being circulated in an adsorber. A regenerating fluid is indirectly heated by the gas coming from the compressor. In a second regeneration phase, the regenerating fluid is sent directly to the adsorber, wh

Method and apparatus for treating a gas by adsorption. A gas is compressed and then treated by being circulated in an adsorber. A regenerating fluid is indirectly heated by the gas coming from the compressor. In a second regeneration phase, the regenerating fluid is sent directly to the adsorber, while the treated gas is refrigerated by an auxiliary refrigerator.

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What is claimed is: 1. A process for treating a gas by adsorption in an adsorber, comprising: a) compressing a gas to be treated; b) making the gas to be treated from step (a) flow through an adsorber in adsorption phase; c) making a stream of regeneration fluid flow through the adsorber in a regen

What is claimed is: 1. A process for treating a gas by adsorption in an adsorber, comprising: a) compressing a gas to be treated; b) making the gas to be treated from step (a) flow through an adsorber in adsorption phase; c) making a stream of regeneration fluid flow through the adsorber in a regeneration phase; c1) during a first part of the adsorber regeneration phase, indirect heat exchange between the gas to be treated from step (a) and a regeneration fluid stream is established in a heat exchanger so as to cool the gas to be treated from step (a) and intended for step (b) and to heat the regeneration fluid intended for step (c), and c2) during a second part of the adsorber regeneration phase, the regeneration fluid is made to flow through the adsorber without making it undergo the heat exchange of step (c1); and d) performing auxiliary refrigeration of the gas to be treated during said step (c2); and heating the regeneration fluid coming from step (c1) by means of an auxiliary heat injection before this regeneration fluid is made to pass through the adsorber. 2. The process as claimed in claim 1, wherein said auxiliary refrigeration step (d) further comprises refrigerating the gas to be treated by an auxiliary cold source. 3. The process as claimed in claim 1, wherein said auxiliary refrigeration step (d) further comprises refrigerating the gas to be treated by at least one part of the stream of regeneration fluid that has passed through the adsorber. 4. The process as claimed in claim 1, wherein said auxiliary refrigeration is carried out in the heat exchanger. 5. The process as claimed in claim 1, wherein said indirect heat exchange is carried out outside the heat exchanger. 6. The process as claimed in claim 5, wherein a flow of the gas to be treated and of the regeneration fluid is maintained in the heat exchanger during said auxiliary refrigeration step (d). 7. The process as claimed in claim 1, further comprising cooling the gas to be treated from step (c1), before this gas to be treated is made to pass through the adsorber. 8. The process as claimed in claim 1, wherein the gas to be treated is atmospheric air, in that the function of step (b) is to strip water and carbon dioxide from the air to be treated coming from step (a), in that said process further comprises separating the air from step (b) by distillation in order to produce at least one of its constituents and also a waste gas, and in that the waste gas forms said regeneration fluid. 9. An apparatus for treating a gas by adsorption, comprising: a compressor for compressing a gas to be treated, the delivery side of the compressor is designed to be connected to the inlet of at least one adsorber during an adsorption phase of the latter; a means for making a regeneration fluid flow through the adsorber during a regeneration phase of the latter; and a means for heating the regeneration fluid entering the adsorber in regeneration mode, wherein: a) the heating means comprises a heat exchanger designed to bring the regeneration fluid into indirect heat exchange with the gas coming from the compressor; b) the apparatus further comprises: 1) a branch-off means for sending the regeneration fluid into the adsorber in regeneration mode without passing through the heat exchanger and; 2) an auxiliary refrigerating means for refrigerating the gas to be treated when said branch-off means are activated; and c) the heating means further comprises an auxiliary heat source designed to carry out additional heating on the regeneration fluid. 10. The apparatus as claimed in claim 9, wherein the auxiliary refrigeration means comprise an auxiliary cold source for at least the cold part of the heat exchanger. 11. The apparatus as claimed in claim 9, wherein the auxiliary refrigerating means comprise a branch-off from a circuit for gas to be treated, that branch-off being mounted across the terminals of the heat exchanger and provided with an auxiliary cold source. 12. The apparatus as claimed in claim 9, wherein the auxiliary refrigerating means comprise a return line for returning the regeneration fluid to the heat exchanger after said fluid has passed through the adsorber in regeneration mode. 13. The apparatus as claimed in claim 9, wherein the auxiliary heat source is designed to provide additional heat for at least the hot part of the heat exchanger. 14. The apparatus as claimed in claim 9, further comprising an additional cooling means for cooling the gas to be treated, these means being placed between the heat exchanger and the adsorber. 15. The apparatus as claimed in claim 9, wherein an assembly starting from the compressor to the adsorber is placed upstream of an air separation installation for producing at least one of the constituents of air by distillation, in that the adsorber is intended to strip water and carbon dioxide from the air to be treated, and in that the regeneration fluid is formed from a waste gas produced by this separation installation.