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AssigneeL'Air Liquide, Societe Anonyme pour l'Etude et l'Exploitation des Procedes Georges Claude
InventorsBernard Darredeau, Jean-Yves Lehman, Jean-Marc Peyron
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A process and installation for the separation of air in a cryogenic distillation apparatus (24) comprising a distillation column (30, 42) and in which the supplied air is separated to produce a fraction rich in oxygen and a fraction rich in nitrogen as products. The purities of these products are maintained substantially constant during variations of demand of either product or of the flow rate or of the pressure of the supplied air by introducing an excess of liquid rich in nitrogen into the distillation apparatus when the demand for the product or the flow rate of the supplied air increases, and by withdrawing an excess of liquid rich in nitrogen from the distillation apparatus, and storing this liquid, when the demand for the product or the flow rate of the supplied air decreases. The apparatus comprises a medium pressure column (30) and a low pressure column (42) and a reflux conduit (44; 11, 12) which permits a reflux liquid to be withdrawn from the medium pressure column (30) and to be injected into the low pressure column (42).
A process for the separation of air in a cryogenic distillation apparatus comprising a distillation column and in which air is separated to produce a fraction rich in oxygen and a fraction rich in nitrogen, comprising maintaining the purity of said oxygen product substantially constant during variations of demand for a said oxygen product or of the flow rate or of the pressure of the supply air by controlling the relative liquid to vapor interstage transfer rate within said distillation column in response to said variations of demand for a said oxygen product or of the flow rate or of the pressure of said supplied air, by increasing the relative liquid to vapor interstage transfer rate in said distillation column when the demand for said oxygen product or the flow rate of the supplied air increases, and decreasing the relative liquid to vapor interstage transfer rate in said distillation column when the demand for said oxygen product or the flow rate of the supplied air decreases, by withdrawing liquid rich in nitrogen from the distillation apparatus, and storing said liquid when the demand for said oxygen product or the flow rate of the supplied air decreases, and introducing at least a portion of said stored liquid rich in nitrogen into the distillation apparatus when the demand for said oxygen product or the flow rate of the supplied air increases.
An installation for the separation of air in a cryogenic distillation apparatus comprising at least one distillation column in which the supplied air is separated to produce a fraction rich in oxygen and a fraction rich in nitrogen, comprising means to control the relative liquid to vapor interstage transfer rate within said distillation column in response to said variations of demand for said oxygen product or of the flow rate or of the pressure of said supplied air, said means to control comprising means to withdraw and means to store an excess of liquid rich in nitrogen from said apparatus, if oxygen product demand or the supplied air flow rate decreases, and means to introduce liquid rich in nitrogen into said apparatus if oxygen product demand or the flow rate of supplied air increases.
Dependencies are inferred from the claim text.