초록 ▼

The apparatus comprises four cylindrical absorbent beds of small particle size (16×40 mesh) molecular sieve, two with zeolite and two with carbon molecular sieve. The units are integrated with each carbon bed in series with one of the zeolite beds, with valving at the inlets to the zeolite beds and

The apparatus comprises four cylindrical absorbent beds of small particle size (16×40 mesh) molecular sieve, two with zeolite and two with carbon molecular sieve. The units are integrated with each carbon bed in series with one of the zeolite beds, with valving at the inlets to the zeolite beds and at the outlets from the carbon beds. The oxygen purity of the gas is increased by selectively adsorbing and exhausting the nitrogen component in the zeolite beds and the argon component in the carbon beds. In a two step cycle, during step 1 of the cycle one pair of beds (one zeolite and one carbon) receives high pressure air as feed gas which pressurizes the beds and establishes a product oxygen flow. Simultaneously, the high pressure gas in the other pair of beds is vented to a lower pressure usually the ambient surroundings, and this depressurization serves to desorb the nitrogen and argon previously adsorbed during the high pressure phase of the cycle. In step 2 of the cycle the adsorbent beds exchange roles. This constant cycling results in a continuous product stream of very high purity oxygen (up to 99.1%). The separation is conducted at a temperature of 297°K. The secondary purifier does not require a regenerative purge flow for the carbon beds for efficient operation, which minimizes the feed gas consumption.

대표청구항 ▼

A process for producing oxygen with a low proportion of argon from a feed gas which is compressed air, using first and second beds containing 16X40 mesh carbon molecular sieve, and third and fourth beds containing 16X40 mesh zeolite molecular sieve, operating by alternately cycling said beds through

A process for producing oxygen with a low proportion of argon from a feed gas which is compressed air, using first and second beds containing 16X40 mesh carbon molecular sieve, and third and fourth beds containing 16X40 mesh zeolite molecular sieve, operating by alternately cycling said beds through steps of adsorption and desorption, each cycle having first and second half cycles, comprising: in each first half-cycle of operation passing said feed gas under pressure through the third and first beds in series to pressurize the beds and provide a flow of product gas at an outlet port to preferentially absorb nitrogen in the third bed and argon in the first bed and concentrate oxygen, while simultaneously the second and fourth beds are depressurized and the nitrogen and argon absorbed during the previous cycle are desorbed and exhausted; and in each second half-cycle of operation passing said feed gas under pressure through the fourth and second beds in series to pressurize the beds and provide a flow of product gas at the outlet port to preferentially adsorb nitrogen in the fourth bed and argon in the second bed and concentrate oxygen, while simultaneously the first and third beds are depressurized and the nitrogen and argon adsorbed during the previous cycle are desorbed and exhausted; whereby by repeating these steps of adsorption and desorption, a continuous stream of oxygen is produced having a purity substantially greater than that of the feed gas (up to 99.1%).