Process for separating nitrogen gas

Claim 2

A process for separating nitrogen gas from a pressurized gas mixture predominantly composed of nitrogen gas and oxygen gas in a nitrogen gas separation apparatus of a pressure swing adsorption system, having at least first and second adsorbers filled with a carbon molecular sieve and a product nitrogen gas holder, the process comprising the steps of: adsorbing oxygen gas selectively in the first adsorber, from a pressurized gaseous mixture with a carbon molecular sieve, while withdrawing nitrogen gas; regenerating a carbon molecular sieve in the second adsorber, by releasing the adsorbed oxygen; carrying out a transfer of the gas under pressure remaining in the first adsorber in which the adsorption step is complete, to the second adsorber in which the regeneration step is complete simultaneously through a piping connecting a raw material gas inlet of the first adsorber to a raw material gas inlet of the second adsorber or/and through a piping connecting a product nitrogen outlet of the first adsorber to a product nitrogen outlet of the second adsorber; and selectively starting an adsorption of oxygen gas in the second adsorber in which the gas transfer step is complete and regenerating the carbon molecular sieve in the first adsorber in which the gas transfer step is complete by releasing the adsorbed oxygen simultaneously, such that said steps of the first adsorber and the second adsorber are alternatively and successively repeated; wherein: said gas transfer step comprises the further step of outwardly discharging part of the gas being transferred from the piping connecting the raw material gas inlet of the first adsorber and the raw material gas inlet of the second adsorber, and as required, from the piping connecting the product nitrogen gas outlet of said first and second adsorbers.

Claim 3

A process for separating nitrogen according to claim 1, wherein the amount of liters of the gas discharged, Q (0° C., 1 atm), is in the following range: Q=0.02 (a×b) to 0.3 (a×b) where a=capacity in liters of each of the first and second adsorbers; and b=pressure in kg/cm 2 G in the adsorber of said first and second adsorbers which has completed said adsorption step.

Claim 4

A process for separating nitrogen according to claim 1, wherein a ratio between an amount of gas transferred through the connection of the feed gas inlet side and that through the connection on the product nitrogen outlet side is in a range of 0.05 to 1.0 and said gas transfer step is stopped when a ratio between an internal pressure of the adsorber of said first and second adsorbers which has completed regeneration and that of the adsorber of said first and second adsorbers just before a starting of said gas transfer step becomes 20 to 47%.

Claim 5

A process for separating nitrogen gas from a pressurized gas mixture predominantly composed of nitrogen gas and oxygen gas in a nitrogen gas separation apparatus of a pressure swing adsorption system, having at least first and second adsorbers filled with a carbon molecular sieve and a product nitrogen gas holder, the process comprising the steps of: adsorbing oxygen gas selectively in the first adsorber, from a pressurized gaseous mixture with a carbon molecular sieve, while withdrawing nitrogen gas; regenerating a carbon molecular sieve in the second adsorber, by releasing the adsorbed oxygen; carrying out a transfer of the gas under pressure remaining in the first adsorber in which the adsorption step is complete, to the second adsorber in which the regeneration step is complete simultaneously through a piping connecting a raw material gas inlet of the first adsorber to a raw material gas inlet of the second adsorber or/and through a piping connecting a product nitrogen outlet of the first adsorber to a product nitrogen outlet of the second adsorber; and selectively starting an adsorption of oxygen gas in the second adsorber in which the gas transfer step is complete and regenerating the carbon molecular sieve in the first adsorber in which the gas transfer step is complete by releasing the adsorbed oxygen simultaneously, such that said steps of the first adsorber and the second adsorber are alternatively and successively repeated; wherein: said gas transfer step comprises the first step of outwardly discharging part of the gas being transferred from the piping connecting the raw material gas inlets of the first and second adsorbers, and as required, from the piping connecting the product nitrogen gas outlets of the first and second adsorbers; said process comprising the further step of flowing back product nitrogen gas from said nitrogen gas holder to an adsorber of said first and second adsorbers which has completed regeneration and starting the adsorption step of the adsorber of the first and second adsorbers which has completed regeneration when its internal pressure has reached at least 70% of a maximum pressure of the adsorber to be attainable during the adsorption step.

Claim 6

A process for separating nitrogen gas from a pressurized gas mixture predominantly composed of nitrogen gas and oxygen gas in a nitrogen gas separation apparatus of a pressure swing adsorption system, having at least first and second adsorbers filled with a carbon molecular sieve and a product nitrogen gas holder, the process comprising the steps of: adsorbing oxygen gas selectively in the first adsorber, from a pressurized gaseous mixture with a carbon molecular sieve, while withdrawing nitrogen gas; regenerating a carbon molecular sieve in the second adsorber, by releasing the adsorbed oxygen; carrying out a transfer of the gas under pressure remaining in the first adsorber in which the adsorption step is complete, to the second adsorber in which the regeneration step is complete simultaneously through a piping connecting a raw material gas inlet of the first adsorber to a raw material gas inlet of the second adsorber or/and through a piping connecting a product nitrogen outlet of the first adsorber to a product nitrogen outlet of the second adsorber; and selectively starting an adsorption of oxygen gas in the second adsorber in which the gas transfer step is complete and regenerating the carbon molecular sieve in the first adsorber in which the gas transfer step is complete by releasing the adsorbed oxygen simultaneously, such that said steps of the first adsorber and the second adsorber are alternatively and successively repeated; wherein: said gas transfer step comprises the first step of outwardly discharging part of the gas being transferred from the piping connecting the raw material gas inlets of the first and second adsorbers, and as required, from the piping connecting the product nitrogen gas outlets of the first and second adsorbers; said process comprising the further step of flowing back product nitrogen gas from said nitrogen gas holder to an adsorber of said first and second adsorbers which has completed regeneration and starting the adsorption step of the adsorber of the first and second adsorbers which has completed regeneration when its internal pressure has reached at least 70% of a maximum pressure of the adsorber to be attainable during the adsorption step.