US 5,129,932 AGranted

Cryogenic process for the separation of air to produce moderate pressure nitrogen

AssigneeAir Products and Chemicals, Inc.

InventorsRakesh Agrawal, Donald W. Woodward

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Abstract

This invention relates to a cryogenic process for the separation of air utilizing an integrated multi-column distillation system wherein a nitrogen rich, oxygen rich and argon rich product are generated. In the cryogenic distillation separation of air, air is initially compressed, pretreated and cooled for separation into its components. Moderate pressure, e.g., 25-80 psia nitrogen is generated with enhanced nitrogen product purity and greater recovery of both nitrogen and argon by effecting a high boil-up rate in the bottom of the lower pressure column, thereby creating a reduced liquid flow/vapor flow ratio (L/V) and utilizing a higher than customary nitrogen reflux to the top of the lower pressure column, where the concentration of oxygen in nitrogen is less than about 10 ppm by volume or the nitrogen purity is at least about 99.5% by volume. Refrigeration to drive the system is obtained by recovering the energy from the waste nitrogen stream and oxygen vapor from the lower pressure column. A second method for obtaining refrigeration is to withdraw oxygen as a bottoms liquid from the lower pressure column, expanding that liquid to a lower pressure and using it to condense the nitrogen vapor generated in a higher pressure column which has been expanded in a turbo-expander to provide the refrigeration.

In a process for the separation of an air stream which comprises nitrogen, argon and oxygen in an integrated multi-column distillation system, having a higher pressure column, a lower pressure column and a side arm column for effecting separation of argon from oxygen, wherein the air stream is compressed, freed of impurities, and cooled forming a cooled air stream and then at least a portion is cryogenically distilled in an integrated multi-column distillation system having a higher pressure column, a lower pressure column, and a side arm column for separation of argon, and oxygen, nitrogen, and argon are obtained as products on removal from said multi-column distillation system the improvement for producing moderate pressure nitrogen product, having a pressure ranging from about 25 to 90 psia, while enhancing argon recovery which comprises:

a. feeding substantially all of the cooled air stream to the higher pressure column;
b. removing substantially all nitrogen vapor from the higher pressure column;
c. splitting the nitrogen vapor from the higher pressure column into two portions, a first portion being warmed against process streams, isentropically expanded, and condensed in a reboiler/condenser;
d. introducing a second portion of the nitrogen vapor to a reboiler/condenser in the lower pressure column for evaporating oxygen liquid and forming a condensed nitrogen stream;
e. isenthapically expanding the second portion and combining with the first portion to form a combined nitrogen stream;
f. introducing the combined nitrogen stream to an upper portion of the lower pressure column;
g. withdrawing a portion of oxygen liquid from the bottom of lower pressure column, isenthapically expanding, to form an oxygen stream and warming the oxygen stream against the first portion of nitrogen vapor in the reboiler/condenser in step (c);
h. warming the oxygen stream against process fluids and obtaining refrigeration therefrom;
and,
i. removing a waste nitrogen stream from an upper portion of the lower pressure column and warming against process fluids and recovering refrigeration therefrom
j. removing moderate pressure nitrogen products at a pressure from 25-90 psia from the lower pressure column.

8 more elements

Facts

Application

07/785,596Filed 30 Oct 1991 · division

Priority

12 Jun 1990

Granted

14 Jul 1992

Term ends

Not estimatedThe source records don’t support an estimate.

Classification12 codes

F25J 3/04315
Of nitrogen: lowest pressure or impure nitrogen, so-called waste nitrogen expansion
F25J 3/04212
Including a so-called "auxiliary vaporiser" for vaporising and producing a gaseous product: and simultaneously condensing vapor from a column…
F25J 3/04309
Using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched streams: of nitrogen
F25J 3/04321
Using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched streams: of oxygen

Abstract

Claims1