System and method for recovery of non-condensable gases such as neon, helium, xenon, and krypton from an air separation unit

Patent metadata

Field	Value
Publication number	US-10295254-B2
Application number	US-201715695381-A
Country	US
Kind code	B2
Filing date	Sep 5, 2017
Priority date	Sep 5, 2017
Publication date	May 21, 2019
Grant date	May 21, 2019

Abstract

A system and method for recovery of rare gases such as neon, helium, xenon, and krypton in an air separation unit is provided. The rare gas recovery system comprises a non-condensable stripping column linked in a heat transfer relationship with a xenon-krypton column via an auxiliary condenser-reboiler. The non-condensable stripping column produces a rare gas containing overhead that is directed to the auxiliary condenser-reboiler where most of the neon is captured in a non-condensable vent stream that is further processed to produce a crude neon vapor stream that contains greater than about 50% mole fraction of neon with the overall neon recovery exceeding 95%. The xenon-krypton column further receives two streams of liquid oxygen from the lower pressure column and the rare gas containing overhead from the non-condensable stripping column and produces a crude xenon and krypton liquid stream and an oxygen-rich overhead.

First claim

What is claimed is:

1. A rare gas recovery system for an air separation unit, the air separation unit comprising a main air compression system, a pre-purification system, a heat exchanger system, and a rectification column system having a higher pressure column and a lower pressure column linked in a heat transfer relationship via a main condenser-reboiler, the neon recovery system comprising:
a non-condensable stripping column configured to receive a portion of a liquid nitrogen condensate stream from the main condenser-reboiler and a stream of nitrogen rich shelf vapor from the higher pressure column, the non-condensable stripping column configured to produce a liquid nitrogen column bottoms and a rare gas containing overhead;
a xenon-krypton column linked in a heat transfer relationship with the non-condensable stripping column via an auxiliary condenser-reboiler, the xenon-krypton column configured to receive a first stream of liquid oxygen pumped from the lower pressure column of the air separation unit and a first boil-off stream of oxygen rich vapor from the auxiliary condenser-reboiler, the xenon-krypton column configured to produce a xenon and krypton containing column bottoms and an oxygen-rich overhead;
the auxiliary condenser-reboiler configured to receive the rare gas containing overhead from the non-condensable stripping column and a second liquid oxygen stream from the lower pressure column of the air separation unit as the refrigeration source, the auxiliary condenser-reboiler is further configured to produce a condensate reflux stream that is released into or directed to the non-condensable stripping column, the first boil-off stream of oxygen rich vapor that is released into the xenon-krypton column and a non-condensable containing vent stream;
a reflux condenser configured to receive the non-condensable containing vent stream from the auxiliary condenser-reboiler and a condensing medium, the reflux condenser further configured to produce a condensate that is directed to the non-condensable stripping column, a crude neon vapor stream that contains greater than about 50% mole fraction of neon;
wherein all or a portion of the liquid nitrogen column bottoms is subcooled to produce a subcooled liquid nitrogen stream and the condensing medium for the reflux condenser is a portion of the subcooled liquid nitrogen stream; and
wherein a portion of the xenon and krypton containing column bottoms is taken as a crude xenon and krypton liquid stream.

2. The rare gas recovery system of claim 1 , wherein the crude neon vapor stream further contains greater than about 10% mole fraction of helium.

3. The rare gas recovery system of claim 1 , wherein all or a portion of the oxygen-rich overhead is directed back to the lower pressure column of the air separation unit.

4. The rare gas recovery system of claim 1 , wherein all or a portion of the oxygen-rich overhead is directed to the main heat exchange system of the air separation unit.

5. The rare gas recovery system of claim 1 , wherein all or a portion of the oxygen-rich overhead is taken as a gaseous oxygen product.

6. The rare gas recovery system of claim 1 , wherein the subcooled liquid nitrogen stream is subcooled via indirect heat exchange with a nitrogen column overhead of the lower pressure column of the air separation unit.

7. The rare gas recovery system of claim 1 , wherein a first portion of the subcooled liquid nitrogen stream is directed to the reflux condenser as the condensing medium and a second portion of the subcooled liquid nitrogen stream is directed to the lower pressure column of the air separation unit as a reflux stream.

8. The rare gas recovery system of claim 1 , wherein a first portion of the subcooled liquid nitrogen stream is directed to the reflux condenser as the condensing medium; a second portion of the subcooled liquid nitrogen stream is directed to the lower pressure column as a reflux stream; and a third portion is taken as a liquid nitrogen product stream.

9. The rare gas recovery system of claim 1 , wherein the vapor portion of the second boil-off stream formed from the vaporization or partial vaporization of the condensing medium is combined with a waste nitrogen stream of the air separation unit.

10. A method for rare gas recovery in an air separation unit, the air separation unit comprising a main air compression system, a pre-purification system, a heat exchanger system, and a rectification column system having a higher pressure column and a lower pressure column linked in a heat transfer relationship via a main condenser-reboiler, the method comprising the steps of:
directing a stream of liquid nitrogen from the main condenser-reboiler and a stream of nitrogen rich shelf vapor from the higher pressure column to a non-condensable stripping column configured to produce a liquid nitrogen column bottoms and a rare gas containing overhead;
subcooling all or a portion of the liquid nitrogen column bottoms to produce a subcooled liquid nitrogen stream;
condensing nitrogen from the rare gas containing overhead in an auxiliary condenser-reboiler against a first stream of liquid oxygen from the lower pressure column of the air separation unit to produce a condensate and a non-condensable containing vent stream while vaporizing or partially vaporizing the liquid oxygen to produce a first boil-off stream formed from the vaporization or partial vaporization of the liquid oxygen;
pumping a second stream of liquid oxygen from the lower pressure column of the air separation unit to a xenon-krypton column linked in a heat transfer relationship with the non-condensable stripping column via the auxiliary condenser-reboiler;
releasing the first boil-off stream from the auxiliary condenser-reboiler into the xenon-krypton column;
directing the non-condensable containing vent stream and a first portion of the subcooled liquid nitrogen stream to a reflux condenser, the reflux condenser configured to produce a condensate stream that is directed to the non-condensable stripping column, a second boil-off stream formed from the vaporization or partial vaporization of the portion of the subcooled liquid nitrogen stream, and a crude neon vapor stream that contains greater than about 50% mole fraction of neon; and
taking a portion of the xenon and krypton containing column bottoms as a crude xenon and krypton liquid stream.

11. The method for rare gas recovery of claim 10 , wherein the crude neon vapor stream further contains greater than about 10% mole fraction of helium.

12. The method for rare gas recovery of claim 10 , further comprising the step of directing all or a portion of the oxygen-rich overhead back to the lower pressure column of the air separation unit.

13. The method for rare gas recovery of claim 10 , further comprising the step of directing all or a portion of the oxygen-rich overhead to the heat exchange system of the air separation unit.

14. The method for rare gas recovery of claim 10 , further comprising the step of taking all or a portion of the oxygen-rich overhead as a gaseous oxygen product.

15. The method for rare gas recovery of claim 10 , wherein the step of subcooling all or a portion of the liquid nitrogen column bottoms to produce a subcooled liquid nitrogen stream further comprises subcooling all or a portion of the liquid nitrogen column bottoms via indirect heat exchange with a nitrogen column overhead of the lower pressure column of the air separation unit to produce the subcooled liquid nitrogen stream.

16. The method for rare gas recovery of claim 10 , further comprising the step of directing a sec

Assignees

• Chakravarthy Vijayaraghavan S
• Tuo Hanfei
• Shelat Maulik R
• Dray James R
• Degenstein Nick J
• Praxair Technology Inc

Inventors

• Chakravarthy Vijayaraghavan S
• Tuo Hanfei
• Shelat Maulik R
• Dray James R
• Degenstein Nick J

Classifications

• F25J2200/34

  using a side column fed by a stream from the low pressure column · CPC title

• F25J3/04745 Primary

  Krypton and/or Xenon · CPC title

• F25J3/04296

  Claude expansion, i.e. expanded into the main or high pressure column · CPC title

• F25J2215/32

  Neon · CPC title

• F25J3/04412

  in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column · CPC title