# US 5,346,536 A · Process for separating nitrogen gas

> Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt

- Number: US 5,346,536 A
- Document ID: US5346536A
- Status: Granted
- Kind: A
- Application number: 08/032,023
- Filed: 1993-03-16
- Granted: 1994-09-13
- Earliest claimed: 1992-03-17
- Assignees: Kuraray Chemical Co., Ltd.
- Inventors: Isao Kaneshige; Tsuneo Genba; Takeshi Tamaru; Tetsuhiko Matsuura
- Web page: https://patentgrep.com/patent/US5346536A

## CPC

- C01B 21/045: {by adsorption in solids}
- B01D 53/047: Pressure swing adsorption
- B01D 53/0476: {Vacuum pressure swing adsorption}
- B01D 53/053: with storage or buffer vessel
- B01D 2253/116: Molecular sieves other than zeolites
- B01D 2253/25: Coated, impregnated or composite adsorbents
- B01D 2256/10: Nitrogen
- B01D 2257/104: Oxygen
- B01D 2259/4006: Less than four
- B01D 2259/402: using two beds
- C01B: NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; {METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C}
- B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28)

## Abstract

A process for separating nitrogen which comprises, with a nitrogen gas separation apparatus of a pressure-swing adsorption type, a gas transfer step between an adsorber having completed an adsorption step with another adsorber having completed a regeneration step. The gas transfer step further comprising discharging part of the gas being transferred out of the system. This process provides, with compact equipment, high-purity product nitrogen with a purity of at least 99.99%, which has been considered difficult to obtain with conventional pressure-swing adsorption apparatuses.

## Claims

### Claim 1

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 2 (depends on 1)

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

### Claim 3 (depends on 1)

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 4

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.