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US4617040A Expired / Lapsed US ⏱️ 0.0 years remaining

Highly pure nitrogen gas producing apparatus

Assignee: Air Water Inc
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Filing: 1984-03-07
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Granted: 1986-10-14
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Expires: 2004-03-07
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Abstract

Abstract A producing apparatus of highly pure nitrogen gas which is used in electronic industry for manufacturing silicon semi-conductors. Conventional nitrogen gas producing apparatus of low temperature separation method and of PSA method are subjected to troubles frequently, the cost of the obtained product nitrogen gas is high, yet the purity is not very high. By the apparatus of this invention, the liquefied nitrogen storage means (23) is connected to rectifying column (15) through the inlet channel (24), the ultra low temperature compressed air supplied into the rectifying column (15) through the air compression means (9), removing means (12) and heat exchangers (13) (14) is cooled further by the evaporating heat of the liquefied nitrogen, the nitrogen is taken out in gas form by utilizing the difference in boiling point, and oxygen is left as liquid. The obtained nitrogen gas is combined with the gassified liquid nitrogen from the liquefied nitrogen storage means (23) and made into product nitrogen gas. Highly pure nitrogen gas can be produced at a low cost and with almost no trouble of the apparatus.

Inventors

  • 👤 Akira Yoshino

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 14:52
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/02; F25J3/04; F25J3/04763; F25J3/04769; F25J3/04812; F25J3/04824; F25J3/04151; F25J3/04187; F25J3/04193; F25J3/042; F25J3/04248; F25J3/04254; F25J3/0426; F25J3/044; F25J3/04624; F25J3/04636; F25J2200/00; F25J2200/50; F25J2200/74; F25J2205/00; F25J2205/60; F25J2210/00; F25J2210/42; F25J2215/00; F25J2215/42; F25J2215/44; F25J2250/00; F25J2250/10; F25J2290/00; F25J2290/62; Y; Y10; Y10S; Y10S62/00; Y10S62/912; Y10S62/913

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 265 words
In an apparatus comprising means designed for producing highly pure nitrogen gas from the rectification of air, for precluding the need for a subsequent high-temperature catalytic step and for precluding the need of purging large quantities of cooling nitrogen, the combination which comprises means effective to compress the air taken from the outside, a means to remove the carbon dioxide gas and water in the compressed air by the said air compression means, a means to store liquefied nitrogen supplied from the outside, a heat exchanger connected to cool down the compressed air passed through said removing means to ultra low temperature, a rectifying column connected to turn a part of the compressed air cooled by the heat exchanger to ultra low temperature into liquid and to keep only nitrogen in gas form, said rectifying column having evaporating means for converting said liquid nitrogen to gaseous nitrogen, a lead channel connected lead consistently the liquefied nitrogen in said liquefied nitrogen storage means into said evaporating means as a source of cooling for compressed air liquefication in place of cold generated from a gas expander, a means to control the feed rate of said liquefied nitrogen in order to maintain constant rectifying conditions in said rectifying column which is provided to said lead channel, and an outlet channel connected to combine and remove both of the gasified said liquid nitrogen after use as the cooling source and also the gasified nitrogen from the outside source, pass them through said heat exchanger and heat them by exchanging heat with said compressed air, as the product nitrogen gas.
Claim 2
Dependent Claim 265 words
In an apparatus comprising means designed for producing highly pure nitrogen gas from the rectification of air, for precluding the need for a subsequent high-temperature catalytic step and for precluding the need of purging large quantities of cooling nitrogen, the combination which comprises means effective to compress the air taken from the outside, a means to remove the carbon dioxide gas and water in the compressed air by the said air compression means, a means to store liquefied nitrogen supplied from the outside, a heat exchanger connected to cool down the compressed air passed through said removing means to ultra low temperature, a rectifying column connected to turn a part of the compressed air cooled by the heat exchanger to ultra low temperature into liquid and to keep only nitrogen in gas form, said rectifying column having evaporating means for converting said liquid nitrogen to gaseous nitrogen, a lead channel connected lead consistently the liquefied nitrogen in said liquefied nitrogen storage means into said evaporating means as a source of cooling for compressed air liquefication in place of cold generated from a gas expander, a means to control the feed rate of said liquefied nitrogen in order to maintain constant rectifying conditions in said rectifying column which is provided to said lead channel, and an outlet channel connected to combine and remove both of the gasified said liquid nitrogen after use as the cooling source and also the gasified nitrogen from the outside source, pass them through said heat exchanger and heat them by exchanging heat with said compressed air, as the product nitrogen gas.
Claim 3
Dependent Claim 36 words
A producing apparatus of highly pure nitrogen gas as set forth in claim 1, in which the rectifying column is provided with a partial condenser section and liquefied nitrogen is conducted to the said partial condenser.
Claim 4
Dependent Claim 40 words
A producing apparatus of highly pure nitrogen gas according to claim 1 or claim 2, wherein the outlet channel is provided with an adsorbing means incorporating the adsorbent which can adsorb oxygen and carbon monoxide selectively at ultra low temperature.
Claim 5
Dependent Claim 50 words
A producing apparatus of highly pure nitrogen gas as defined by claim 1, wherein the outlet channel is provided on the side of rectifying column with a condensing means to condense a part of the product nitrogen gas and to return the condensed nitrogen gas to the said rectifying column.
Claim 6
Dependent Claim 87 words
A producing apparatus of highly pure nitrogen gas in accordance with claim 4 in which the outlet channel is provided on the side of rectifying column with a condensing means to condense a part of the product nitrogen gas and to return the condensed nitrogen gas to the said rectifying column, and the part following the condensing means at the outlet channel is provided with an adsorbing means incorporating the adsorbent which adsorbs oxygen and carbon monoxide in the product nitrogen gas selectively at ultra low temperature.
Claim 7
Dependent Claim 41 words
A producing apparatus of highly pure nitrogen gas according to claim 3 or claim 5 in which the adsorbing means is an oxygen adsorption cylinder filled with synthetic zeolite of pore diameter of about 3 Å, 4 Å or 5 Å.
Claim 8
Dependent Claim 173 words
In an apparatus comprising means designed for performing a low cost method of producing high purity nitrogen gas of a quality sufficient for the electronics industry, for precluding the need for a subsequent high-temperature catalystic step and for precluding the need of purging large quantities of cooling nitrogen, the combination which comprises: rectifying means for rectifying air at a temperature to condense oxygen from the nitrogen contained in said air, separate storage means containing liquid nitrogen as an external source, conduit means connected from said separate storage means to said rectifying means for introducing said liquid nitrogen from said external storage means into said rectifying means for heat exchanging relationship with said air being rectified in said rectifying means, evaporating means operable at low temperature for converting said liquid nitrogen from said external source to gaseous nitrogen while in said heat exchanging relationship, and conduit means extending from said evaporating means for combining the evaporated gaseous nitrogen from said external source with said nitrogen produced by evaporation from the oxygen of said air.
Claim 9
Dependent Claim 173 words
In an apparatus comprising means designed for performing a low cost method of producing high purity nitrogen gas of a quality sufficient for the electronics industry, for precluding the need for a subsequent high-temperature catalystic step and for precluding the need of purging large quantities of cooling nitrogen, the combination which comprises: rectifying means for rectifying air at a temperature to condense oxygen from the nitrogen contained in said air, separate storage means containing liquid nitrogen as an external source, conduit means connected from said separate storage means to said rectifying means for introducing said liquid nitrogen from said external storage means into said rectifying means for heat exchanging relationship with said air being rectified in said rectifying means, evaporating means operable at low temperature for converting said liquid nitrogen from said external source to gaseous nitrogen while in said heat exchanging relationship, and conduit means extending from said evaporating means for combining the evaporated gaseous nitrogen from said external source with said nitrogen produced by evaporation from the oxygen of said air.
Claim 10
Dependent Claim 47 words
An apparatus for producing highly pure nitrogen gas as set forth in claim 7, in which said conduit means connected to said rectifying means contains valve means to control the feeding amount of said liquid nitrogen in order to maintain constant rectifying conditions in said rectifying column.
Claim 11
Dependent Claim 34 words
An apparatus for producing highly pure nitrogen gas as set forth in claim 7, in which said evaporating means comprises a partial condenser section, and said liquid nitorgen is conducted to said partial condenser.
Claim 12
Dependent Claim 54 words
An apparatus for producing highly pure nitrogen gas according to claim 7 or claim 9, wherein said conduit means extending from said evaporating means for combining gaseous nitrogen with nitrogen produced from said air is connected to adsorbing means incorporating an adsorbent which can adsorb oxygen and carbon monoxide selectively at ultra low temperatures.
Claim 13
Dependent Claim 65 words
An apparatus for producing highly pure nitrogen gas as set forth in claim 7, wherein said conduit means extending from said evaporating means for combining gaseous nitrogen with nitrogen produced from said air, is provided on the side of said evaporating means with condensing means to condense a part of the combined nitrogen gas and to return the condensed nitrogen gas to said rectifying means.
Claim 14
Dependent Claim 41 words
An apparatus for producing highly pure nitrogen gas as set forth in claim 11, wherein the conduit means following the condensing means is provided adsorbing means incorporating an adsorbent which can adsorb oxygen and carbon monoxide selectively at ultra low temperatures.

References Cited (Backward Citations)

US3210947A Cited
US3339370A Cited
US4380457A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-10-13 1990-04-14 1990-10-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-10-13 1994-04-14 1994-10-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-10-13 1998-04-14 1998-10-14 $7700.00 Window Closed / Lapsed

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