Main heat exchange system and method for reboiling

Patent metadata

Field	Value
Publication number	US-9920988-B2
Application number	US-201615242961-A
Country	US
Kind code	B2
Filing date	Aug 22, 2016
Priority date	Dec 16, 2013
Publication date	Mar 20, 2018
Grant date	Mar 20, 2018

Abstract

A method and main heat exchange system for use in a cryogenic air separation plant in which down-flow and thermosiphon heat exchangers are employed to partially vaporize an oxygen-rich liquid produced in a lower pressure column and to condense the nitrogen-rich vapor in a higher pressure column. A greater proportion of the oxygen-rich liquid can be partially vaporized in the down-flow heat exchangers than in the thermosiphon heat exchangers and the nitrogen-rich vapor condensed in the thermosiphon heat exchangers can have a higher oxygen content than the nitrogen-rich vapor condensed in the down-flow heat exchangers. This allows the higher pressure column to operate at a lower pressure than would otherwise be possible. A central conduit can extend from the higher pressure column into the lower pressure column to introduce the nitrogen-rich vapor into at least the down-flow heat exchangers for purposes of reducing pressure drop and column height.

First claim

We claim:

1. A main heat exchange system for reboiling a lower pressure column of a double column arrangement, the main heat exchange system comprising:
a plurality of down-flow heat exchangers and a plurality of thermosiphon heat exchangers situated below the plurality of down-flow heat exchangers for partially vaporizing an oxygen-rich liquid produced as a result of a distillation of an oxygen and nitrogen containing mixture within the lower pressure column and initiating the formation of an ascending vapor phase of the oxygen and nitrogen containing mixture to be distilled within the lower pressure column;
the plurality of the down-flow heat exchangers configured to partially vaporize a greater proportion of the oxygen-rich liquid than the plurality of the thermosiphon heat exchangers and the plurality of the down-flow heat exchangers and the plurality of thermosiphon heat exchangers having condensing sides connected to the higher pressure column of the double column arrangement so that at least one nitrogen-rich vapor stream condenses through indirect heat exchange with the oxygen-rich liquid occurring within the down flow heat exchangers and through indirect heat exchange with residual liquid occurring within the thermosiphon heat exchangers, the residual liquid formed from partial vaporization of the oxygen-rich liquid within the down-flow heat exchangers;
the condensing sides of the down-flow heat exchangers and the thermosiphon heat exchangers also connected to the higher pressure column and the lower pressure column so that at least one liquid condensate produced through condensation of the at least one nitrogen-rich vapor stream is introduced into the higher pressure column and the lower pressure column;
a central conduit extending from a dome forming a top end of the higher pressure column and into the lower pressure column;
the plurality of the down-flow heat exchangers radially situated in radial locations with respect to the central conduit and connected to a shell of the lower pressure column;
the condensing sides of the down-flow heat exchangers connected to the central conduit to receive the at least part of the at least one nitrogen-rich vapor stream from the higher pressure column;
the plurality of thermosiphon heat exchangers radially situated in radial locations with respect to the central conduit and between the down-flow heat exchangers and the dome such that the residual liquid collects within a region of the lower pressure column defined by the shell of the lower pressure column and the dome of the higher pressure column;
wherein the at least one liquid condensate comprises a first reflux introduced into the higher pressure column, and a second reflux introduced into the higher pressure column at a location below the first reflux.

2. The main heat exchange system of claim 1 wherein the plurality of down flow heat exchangers each have heat exchange tubes, within which the oxygen-rich liquid partially vaporizes and a shell enclosing the heat exchange tubes and into which the at least part of the at least one nitrogen-rich vapor stream is introduced to perform the indirect heat exchange with the oxygen-rich liquid and thereby forms the condensing side thereof.

3. The main heat exchange system of claim 1 wherein:
a return conduit is in flow communication with the condensing side of the down-flow heat exchangers and with the higher pressure column so that part of the at least one condensate returns to the higher pressure column as the first reflux; and
a flow control valve is positioned within the return conduit so that during turn-down or restart operations, flow of the first reflux to the higher pressure column is restricted to partially flood the condensing side of down-flow heat exchangers and thereby preventing partial dry-out thereof on a vaporization side thereof located opposite to the condensing side.

Assignees

• Chakravarthy Vijayaraghavan S
• Lockett Michael J
• Bonaquist Dante P
• Shelat Maulik R
• Kibler Karl K
• Praxair Technology Inc

Inventors

• Chakravarthy Vijayaraghavan S
• Lockett Michael J
• Bonaquist Dante P
• Shelat Maulik R
• Kibler Karl K

Classifications

• F25J3/04884

  Arrangement of reboiler-condensers · CPC title

• F25J2250/20

  Boiler-condenser with multiple exchanger cores in parallel or with multiple re-boiling or condensing streams · CPC title

• F25J3/04412 Primary

  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

• F25J2200/52

  in the high pressure column of a double pressure main column system · CPC title

• F25J3/0486 Primary

  of vaporisers for oxygen enriched liquids, e.g. purging of liquids · CPC title