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The method of nitrogen production in cryogenic air separation equipment

The method of nitrogen production in cryogenic air separation equipment
Mar 04, 2024
Author: DEAR AST

Nitrogen is the main component of air, accounting for about 78% of the air. With the progress of science and technology and economic development, the application scope of nitrogen is expanding day by day and has penetrated into many industrial sectors and daily life fields.

There are several main methods for producing nitrogen gas. One of them is cryogenic air separation for nitrogen production, which is a traditional nitrogen production method with a history of nearly several decades. It uses air as the raw material, undergoes compression, purification, and then uses heat exchange to liquefy the air into liquid air. Liquid air is mainly a mixture of liquid oxygen and liquid nitrogen. By utilizing the different boiling points of liquid oxygen and liquid nitrogen (at 1 atmospheric pressure, the former has a boiling point of -183 ℃, while the latter has a boiling point of -196 ℃), they are separated through distillation of liquid air to obtain nitrogen gas. The characteristics of deep cold air separation nitrogen production equipment are high gas production, high product nitrogen purity, and can be stored in liquid nitrogen storage tanks, making it suitable for large-scale industrial nitrogen production.

Due to the irreplaceable competitive advantage of low-temperature separation method in large-scale molding of oxygen and nitrogen liquid products, especially high-purity products, and the fact that only low-temperature separation method has the ability to simultaneously produce rare gas products such as argon, low-temperature separation method occupies a very important position in the industrial application of air separation.

DEAR Air Separation has the technology and experience of cryogenic nitrogen production. Capable of meeting customer nitrogen production needs.

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When the amount of treated air increases, the rising steam in the distillation column will increase, and the amount of liquid to be condensed in the main cooler will increase accordingly, so it has no effect on the reflux ratio in the column. The purity of oxygen and nitrogen remained unchanged in a certain range with the increase of gas volume, and the output increased proportionally with the increase of gas volume. However, with the increase of the amount of condensate in the main cooler, the heat load of the main cooler increases. When the heat transfer area is insufficient, the temperature difference of the main cooler will inevitably expand, and the pressure of the lower column will increase accordingly. At the same time, with the increase of gas velocity in the column, the amount of downflow liquid increases, and the liquid layer on the tray thickens, which increases the resistance of the tray and the pressure of the upper and lower columns. This will adversely affect the sepa
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