초록 ▼

Disclosed is a production process and apparatus of high-purity air and various air material gases for semiconductor production factories that, together with enabling the production of high-purity air, also enables the production high-purity nitrogen simultaneous to the production of oxygen-rich air

Disclosed is a production process and apparatus of high-purity air and various air material gases for semiconductor production factories that, together with enabling the production of high-purity air, also enables the production high-purity nitrogen simultaneous to the production of oxygen-rich air as the finished product. This is accomplished by compressing feed air to a pressure of 3 to 10 kg/cm2G, introducing this compressed air into a catalyst tower (8) to convert the carbon monoxide, hydrocarbons and hydrogen contained in the feed air into carbon dioxide and water, and introducing the purified air into an adsorption tower (12a) or (12b) after cooling the heated air following catalytic reaction to remove carbon dioxide, water and other minute amounts of impurities by adsorption. A portion of the resulting purified air is removed as product high-purity air, while the remainder is introduced into a main heat exchanger (18) where it is cooled to substantially the liquefaction temperature. After cooling, the air is introduced into a single rectification tower (19) followed by liquefaction rectification. High-purity nitrogen is then removed from the top of said single rectification tower which is then obtained as product high-purity nitrogen after going through the main heat exchanger (18). On the other hand, oxygen-rich liquefied air is drawn out from the bottom of the single rectification tower (19). This oxygen-rich liquefied air is then introduced into a condenser-evaporator. (24) where it is vaporized and then drawn out. This drawn out air is then introduced into the main heat exchanger (18) where it is heated to an intermediate temperature and then removed. This oxygen-rich air is then introduced into an expansion turbine (35) where it is expanded and lowered in temperature. After generation of cold, the cold is recovered followed by obtaining of the product gas in the form of purified oxygen-rich air.

대표청구항 ▼

A process for producing gases for semiconductor production factories comprising: introducing feed air compressed to a pressure of 3-10 kg/cm2G into a catalyst tower to convert carbon monoxide, hydrocarbons and hydrogen in said feed air into carbon dioxide and water by catalytic reaction; cooling the

A process for producing gases for semiconductor production factories comprising: introducing feed air compressed to a pressure of 3-10 kg/cm2G into a catalyst tower to convert carbon monoxide, hydrocarbons and hydrogen in said feed air into carbon dioxide and water by catalytic reaction; cooling the heated air following said catalytic reaction to 5°to 10°C.; introducing the cooled air into an adsorption tower packed with alumina gel or silica gel near the inlet and zeolite thereon in a filling rate from 1:9 to 3:7 in terms of weight ratio and purifying the air by removing at least carbon dioxide and water by adsorption; obtaining a portion of the resulting purified air as product high-purity air; introducing the remainder of the purified air into a main heat exchanger and cooling the purified air to about a liquefaction temperature of the purified air by heat exchange with return gas; performing liquefied rectification by introducing the purified air after cooling into a single rectification tower having a top and a bottom; drawing out high-purity nitrogen from the top of said single rectification tower and obtaining product high-purity nitrogen gas after recovery of cold in the main heat exchanger, together with drawing out oxygen-rich liquefied air from the bottom of the single rectification tower; allowing the oxygen-rich liquefied air to expand and introducing the air to a condenser-evaporator of the single rectification tower; introducing the oxygen-rich liquefied air removed after gasification in said condenser-evaporator into the main heat exchanger and heating the air to an intermediate temperature; introducing the oxygen-rich air at said intermediate temperature into an expansion turbine so as to lower the temperature by expansion and generate cold; again introducing the expanded and cooled oxygen-rich air into the main heat exchanger to recover cold; and, obtaining the resulting oxygen-rich air as product.