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

An air separation and recovery system technology, used in refrigeration and liquefaction, cold treatment separation, solidification, etc.

Active Publication Date: 2020-04-24
PRAXAIR TECH INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

In addition, since none of the above-mentioned prior art neon recovery systems have the ability to easily and efficiently co-generate xenon and krypton, further needs include noble gas recovery systems that have a total neon recovery greater than about 95%, and Can co-produce a crude neon vapor stream containing greater than about 50 mole percent neon and greater than about 50 mole percent helium, and can produce xenon and krypton in commercial quantities

Method used

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

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Embodiment

[0068] For various embodiments of the system and method for recovering neon of the present invention, various process simulations were performed using various air separation unit operating models to characterize: (i) recovery of neon and other noble gases; (ii) crude The composition of the neon vapor stream; and (iii) the net loss of nitrogen from the distillation column system; when operating an air separation unit using the neon or noble gas recovery system and associated methods described above and shown in the accompanying drawings.

[0069] Table 1 shows the reference for figure 2 Results of computer-based process simulations of the described recycling system and associated method. As shown in Table 1, the air separation unit was operated with an incoming feed air stream of 4757.56 kcfh and a liquid air stream of 37.86 kcfh entering the high pressure column at a pressure of approximately 97 psia. Approximately 45.00 kcfh of tray nitrogen vapor is transferred from the hi...

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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 columnlinked 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 containingoverhead from the non-condensable stripping column and produces a crude xenon and krypton liquid stream and an oxygen-rich overhead.

Description

technical field [0001] The present invention relates to systems and methods for recovering noble gases such as neon, helium, xenon and krypton from air separation plants, and more particularly to systems and methods for recovering neon and other noncondensable gases, Including a thermally coupled non-condensable stripping column and a xenon-krypton column arranged in operative association with an auxiliary condenser-reboiler and a second reflux condenser, all fully integrated within the air separation unit. The recovered crude neon vapor stream contains greater than about 50 mole percent neon with an overall neon recovery of greater than about 95%. Additionally, crude xenon and krypton streams are produced in the xenon-krypton column. Background technique [0002] A cryogenic air separation unit (ASU) is typically designed, constructed and operated to meet the baseload product make-up needs / requirements of one or more end-user customers, and optionally to meet local or merc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F25J3/04
CPCF25J3/04872F25J3/0406F25J3/0409F25J3/04624F25J3/04642F25J3/04678F25J2200/32F25J2215/30F25J2235/50F25J2245/50F25J2250/02F25J2250/10F25J3/04745F25J3/04412F25J3/04296F25J2200/34F25J2215/32F25J2205/30F25J3/04672F25J2200/06F25J2205/70F25J2210/06F25J2210/40F25J2215/04F25J2215/34F25J2215/36F25J2215/42F25J2215/50F25J2220/02F25J2230/30F25J2235/52F25J2240/10F25J2270/02F25J2270/42
Inventor V·S·查克拉瓦西脱瀚斐M·R·谢莱特J·R·德雷N·J·德根斯坦
Owner PRAXAIR TECH INC
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