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An adsorbent for separating nitrogen from a mixed gas of oxygen and nitrogen is MSC wherein an oxygen and nitrogen separation ratio α and a ratio (t95/t50) of a time t50 required for adsorbing 50% of the oxygen equilibrium adsorption amount and a time t95 required for adsorbing 95% of the oxygen equ

An adsorbent for separating nitrogen from a mixed gas of oxygen and nitrogen is MSC wherein an oxygen and nitrogen separation ratio α and a ratio (t95/t50) of a time t50 required for adsorbing 50% of the oxygen equilibrium adsorption amount and a time t95 required for adsorbing 95% of the oxygen equilibrium adsorption amount satisfy the inequality(t95/t50)<0.4×(α?24)α?35.The amount of adsorbent used with respect to a predetermined amount of nitrogen generated can be reduced since a method is carried out which uses this adsorbent to produce nitrogen by separating nitrogen from the mixed gas of oxygen and nitrogen by means of a PSA method. By this method, it is possible to reduce the cost of the apparatus and reduce and miniaturize the scale of the apparatus, and the power consumption amount can be reduced.

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1. An adsorbent for separating nitrogen from a mixed gas of oxygen and nitrogen, the adsorbent being a MSC, wherein a oxygen and nitrogen separation ratio α (ratio of an oxygen adsorption rate constant K(O2) and nitrogen adsorption rate constant K(N2), K(O2)/K(N2)) is 35 or more, and an adsorption r

1. An adsorbent for separating nitrogen from a mixed gas of oxygen and nitrogen, the adsorbent being a MSC, wherein a oxygen and nitrogen separation ratio α (ratio of an oxygen adsorption rate constant K(O2) and nitrogen adsorption rate constant K(N2), K(O2)/K(N2)) is 35 or more, and an adsorption rate characteristic, expressed by a time t95 required for adsorbing 95% of an oxygen equilibrium adsorption amount and a time t50 required for adsorbing 50% of an oxygen equilibrium adsorption amount, satisfies the following inequality:(t95/t50)<0.4×(α?24)α?35. 2. An adsorbent for separating nitrogen from a mixed gas of oxygen and nitrogen according to claim 1, wherein the MSC is prepared by a pore adjustment process by means of chemical vapor deposition (CVD) of a thermally decomposable hydrocarbon at 600 to 770° C.3. An adsorbent for separating nitrogen according to claim 1, wherein the mixed gas of oxygen and nitrogen is air.4. A nitrogen production method carried out by a PSA method in which one cycle comprises a pressurization adsorption step of collecting nitrogen by pressurizing a mixed gas of oxygen and nitrogen and bringing it into contact with the adsorbent according to claim 1, and a depressurization desorption step of depressurizing the adsorbent which is in a pressurized state after the adsorption step and desorbing the adsorbed component, wherein a half cycle time is within a range of 45 to 240 seconds.5. The nitrogen production method according to claim 4, wherein the half cycle time is within a range of 60 to 180 seconds.6. An adsorbent for separating nitrogen from a mixed gas of oxygen and nitrogen, the adsorbent being a MSC, wherein an oxygen adsorption rate constant is 6.5×10?2 s?1 or more, an oxygen and nitrogen separation ratio α (ratio of an oxygen adsorption rate constant K(O2) and a nitrogen adsorption rate constant K(2), K(O2)/K(N2)) is 35 or more, and an adsorption rate characteristic, expressed by a time t95 required for adsorbing 95% of an oxygen equilibrium adsorption amount and a time t50 required or adsorbing 50% of an oxygen equilibrium adsorption amount, satisfies the following inequality:(t95/t50)<0.4×(α?24)α?35.