Method for separating a krypton-xenon concentrate and a device for carrying out said method
OwnerMikhail Yurievich Savinovinventor
Life of this patent
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Abstract
A krypton-xenon concentrate is first divided into krypton and xenon fractions in a preliminary rectifying column. Semi-volatile impurities are removed from each fraction, and production krypton and xenon are obtained from the refined fractions in krypton and xenon production columns. A recovered krypton flow is produced in a krypton recovery rectifying column. Reflux is formed in condensers-evaporators of rectification columns of the device in such a way that the formation of a solid phase is excluded. The operation of the rectification columns is initiated by supplying krypton to a contacting space.
Claims4
A method for separating a krypton-xenon concentrate comprising the steps of:
- separating a krypton-xenon-concentrate flow in a preliminary rectifying column to produce a krypton-fraction flow and a xenon-fraction flow;
- rectifying the xenon-fraction flow in a xenon rectifying column to produce a purified xenon-fraction flow and a high-boiling-temperature-admixtures flow;
- producing a purified xenon-fraction flow from an upper zone of the xenon rectifying column;
- separating the purified xenon-fraction flow in a production-xenon column to produce a production-xenon flow and a xenon-column blowing gases flow;
- rectifying the krypton-fraction flow in a additional krypton rectifying column to produce a purified krypton-fraction flow and an intermediate admixtures flow;
- separating the purified krypton-fraction flow in a production-krypton column to produce a production-krypton flow and a krypton-column blowing gases flow;
- rectifying the krypton-column blowing gases flow in a krypton recovery rectifying column to produce a recovered krypton flow and a low-boiling-temperature-admixtures flow;
- and
- directing the xenon-column blowing gases flow and the recovered krypton flow into the preliminary rectifying column for separation,
- wherein the preliminary rectifying column, the xenon rectifying column, the krypton rectifying column, and the krypton recovery rectifying column are put into operation with krypton supplied to a respective contacting space in each said rectifying column, and wherein said rectifying columns comprise evaporating condensers.
A device for separating a krypton-xenon concentrate comprising:
- a preliminary rectifying column comprising a contact section and a concentration section with an anticipatory assay nipple, the preliminary rectifying column being fed in by a krypton-xenon concentrate line and fed out by a xenon-fraction line and a krypton-fraction line;
- a xenon rectifying column in communication with the preliminary rectifying column, comprising a xenon concentration unit and a concentration section with an anticipatory assay nipple, an upper zone of the xenon concentration unit being coupled to a purified xenon-fraction-outlet branch pipe, the purified xenon-fraction-outlet branch pipe being coupled to a purified xenon-fraction line of a production-xenon column, the xenon rectifying column being fed in by the xenon-fraction line and fed out by the purified xenon-fraction line and a high-boiling-temperature-admixtures line;
- a krypton rectifying column in communication with the preliminary rectifying column comprising a concentration section with an anticipatory assay nipple, the krypton rectifying column being fed in by the krypton-fraction line and fed out by a purified krypton-fraction line and an intermediate admixtures line;
- the production-xenon column in communication with the xenon rectifying column comprising an evaporating condenser, a thermal converter, and a concentration section with an anticipatory assay nipple, the production-xenon column being fed in by the purified xenon-fraction line and fed out by a xenon-column blowing gases line, wherein the thermal converter is mounted more than the distance between 0.4H and 0.8H above a feed point of the purified xenon-fraction line, wherein H is a height of the concentration section;
- a production-krypton column in communication with the krypton rectifying column, comprising an evaporating condenser, a thermal converter, and a concentration section with an anticipatory assay nipple, the production-krypton column being fed in by the purified krypton-fraction line and fed out by a krypton-column blowing gases line, the thermal converter being mounted more than the distance between 0.4H and 0.8H above a feed point of the purified krypton-fraction line, wherein H is a height of the concentration section;
- a krypton recovery column in communication with the production-krypton column comprising a concentration section with an anticipatory assay nipple, the krypton recovery column being fed in by the krypton-column blowing gases line and fed out by a recovered krypton line and a low-boiling-temperature-admixtures line;
- a purge collection unit, the purge collection unit being coupled to the xenon-column blowing gases line, the high-boiling-temperature-admixtures line, the intermediate admixtures line, the low-boiling-temperature-admixtures line and the recovered krypton line;
- and
- pressure increasing units, wherein the xenon-column blowing gases line, the high-boiling-temperature-admixtures line, the intermediate admixtures line, the low-boiling-temperature-admixtures line and the recovered krypton line are coupled, via the pressure increasing units, to a contact section of the preliminary rectifying column.
Dependencies are inferred from the claim text.