System and method for enhanced recovery of argon and oxygen from a nitrogen producing cryogenic air separation unit

Patent metadata

Field	Value
Publication number	US-10969168-B2
Application number	US-202016742965-A
Country	US
Kind code	B2
Filing date	Jan 15, 2020
Priority date	Apr 25, 2018
Publication date	Apr 6, 2021
Grant date	Apr 6, 2021

Abstract

A moderate pressure air separation unit and air separation cycle is disclosed that provides for up to about 96% recovery of argon, an overall nitrogen recovery of 98 percent or greater and limited gaseous oxygen production. The air separation is configured to produce a first high purity oxygen enriched stream and a second lower purity oxygen enriched stream from the lower pressure column, one of which is used as the refrigerant to condense the argon in the argon condenser, with the resulting vaporized oxygen stream used to regenerate the temperature swing adsorption pre-purifier unit. All or a portion of the first high purity oxygen enriched stream is vaporized in the main heat exchanger to produce the gaseous oxygen products.

First claim

What is claimed is:

1. A method of separating air to produce one or more high purity nitrogen products in a cryogenic air separation unit with a total nitrogen recovery of 98 percent or greater, the method comprising the steps of:
compressing a stream of incoming feed air to produce a compressed air stream;
purifying the compressed air stream in an adsorption based pre-purification unit configured to removing water vapor, carbon dioxide, nitrous oxide, and hydrocarbons from the compressed air stream to producing a compressed and purified air stream;
splitting the compressed and purified air stream is split into at least a boiler air stream and a turbine air stream;
expanding the turbine air stream in a turboexpander to form an exhaust stream;
cooling the boiler air stream against a pumped oxygen stream to produce a cooled boiler air stream at a temperature suitable for rectification in a cryogenic distillation system and a gaseous oxygen product stream;
directing the cooled boiler air stream and the exhaust stream to the cryogenic distillation column system, the cryogenic distillation system having a higher pressure column and a lower pressure column linked in a heat transfer relationship via a condenser-reboiler, the cryogenic distillation column system also having an argon column arrangement operatively coupled with the lower pressure column, the argon column arrangement having at least one argon column and an argon condenser;
rectifying the cooled boiler air stream and the exhaust stream in the cryogenic distillation column system configured to produce a first oxygen enriched stream taken from a first location at the bottom of the lower pressure column having a first oxygen concentration greater than or equal to 99.5 percent oxygen, a second oxygen enriched stream taken from a second location a few stages above the first location and having a second oxygen concentration greater than 93 percent and lower than the first oxygen concentration, an oxygen enriched kettle stream from the bottom of the higher pressure column, a nitrogen overhead stream from the lower pressure column, and a condensed nitrogen stream from the condenser-reboiler;
rectifying an oxygen-argon stream extracted from the lower pressure column in the argon column arrangement, the argon column configured to produce an argon-enriched overhead that is directed to the argon condenser and a third oxygen enriched stream that is returned to the lower pressure column;
directing the first oxygen enriched stream to the argon condenser by opening a first valve while closing a second valve and thereafter condensing the argon-enriched overhead in the argon condenser against the first oxygen enriched stream to produce a crude argon stream, an argon reflux stream and an oxygen enriched waste stream and wherein the argon recovery in the crude argon stream is greater than 75 percent of the argon in the incoming feed air stream; and
directing the second oxygen enriched stream to the argon condenser by closing the first valve while opening the second valve and thereafter condensing the argon-enriched overhead in the argon condenser against the first oxygen enriched stream to produce a crude argon stream, an argon reflux stream and an oxygen enriched waste stream and wherein the argon recovery in the crude argon stream is greater than 30 percent of the argon in the incoming feed air stream.

2. The method of claim 1 further comprising the step of subcooling the oxygen enriched kettle stream from the higher pressure column and the condensed nitrogen stream from the condenser-reboiler via indirect heat exchange with the nitrogen overhead stream from the lower pressure column.

3. The method of claim 1 further comprising the step of subcooling the first oxygen enriched stream from the lower pressure column or the second oxygen enriched stream from the lower pressure column via indirect heat exchange with the oxygen enriched waste stream.

4. The method of claim 1 wherein the adsorption based pre-purifier unit is a multi-bed temperature swing adsorption unit configured to purifying the compressed air stream, the multi-bed temperature swing adsorption unit is configured such that each bed alternates between an on-line operating phase adsorbing the water vapor, carbon dioxide, nitrous oxide, and hydrocarbons from the compressed air stream and an off-line operating phase where the bed is regenerated with the oxygen enriched waste stream having greater than 90.0 percent oxygen content, and wherein the nitrogen recovery in the one or more nitrogen products is greater than 98 percent of the nitrogen in the incoming feed air stream.

5. The method of claim 4 further comprising the step of heating the oxygen enriched waste stream to a temperature less than or equal to about 450° F. for use in regenerating the adsorbent beds in the temperature swing adsorption unit.

6. The method of claim 1 , wherein the higher pressure column is configured to operate at a pressure between 6.0 bar(a) and 10.0 bar(a), the lower pressure column is configured to operate at a pressure between 1.5 bar(a) and 2.8 bar(a), and the argon column is configured to operate at a pressure of between about 1.3 bar(a) and 2.8 bar(a).

Assignees

• Kromer Brian R
• Handley James R
• Prosser Neil M
• Praxair Technology Inc

Inventors

• Kromer Brian R
• Handley James R
• Prosser Neil M

Classifications

• Y02C20/40

  of CO2 · CPC title

• F25J2210/42

  Nitrogen · CPC title

• F25J2200/20

  in an elevated pressure multiple column system wherein the lowest pressure column is at a pressure well above the minimum pressure needed to overcome pressure drop to reject the products to atmosphere · CPC title

• F25J3/0426

  The cryogenic component does not participate in the fractionation · CPC title

• F25J2210/40

  Air or oxygen enriched air, i.e. generally less than 30mol% of O2 · CPC title