Method for controlling production of high pressure gaseous oxygen in an air separation unit

Patent metadata

Field	Value
Publication number	US-10359231-B2
Application number	US-201715485635-A
Country	US
Kind code	B2
Filing date	Apr 12, 2017
Priority date	Apr 12, 2017
Publication date	Jul 23, 2019
Grant date	Jul 23, 2019

Abstract

A method for controlling production of high pressure gaseous oxygen in a cryogenic air separation unit that uses a high pressure gaseous oxygen bypass together with adjustments to the split of the incoming compressed and purified air between the boiler air circuit and the turbine air circuit such that the volumetric ratio of the boiler air stream to the turbine air stream is reduced to between about 0.15:1 and 0.35:1.

First claim

What is claimed is:

1. A method for producing a high pressure gaseous oxygen product in an air separation plant comprising a primary heat exchanger and a distillation column system with a higher pressure column, a lower pressure column, and a main condenser-reboiler disposed in the lower pressure column and in a heat exchange relationship with the lower pressure column and higher pressure column, the air separation unit is configured to be operated in a high pressure gaseous oxygen full product mode and a high pressure gaseous oxygen bypass mode, the method comprising the steps of:
(a) compressing and purifying a stream of feed air, the stream of feed air having a first volumetric flow rate;
(b) splitting the stream of compressed and purified feed air into two or more streams including a boiler air stream and a turbine air stream, wherein the volumetric flow ratio of the boiler air stream to the turbine air stream is between about 0.40:1 and 0.70:1;
(c) directing the boiler air stream to a boiler air circuit configured to further compress the boiler air stream in a boiler air compressor and directing the turbine air stream to a turbine air circuit configured to partially cool the turbine air stream in the primary heat exchanger and expand the turbine air stream and produce refrigeration for the distillation column system;
(d) cooling the further compressed boiler air stream in the primary heat exchanger via indirect heat exchange with a stream of liquid oxygen taken from the lower pressure column to produce a first cooled, compressed feed air stream and a gaseous oxygen product;
(e) directing the first cooled, compressed feed air stream to the higher pressure column, the lower pressure column or both columns and directing the expanded turbine air stream to the higher pressure column or the lower pressure column;
(f) rectifying the cooled, compressed feed air stream and the expanded turbine air stream in the distillation column system to produce a stream of gaseous nitrogen product, a stream on liquid nitrogen, a stream of waste nitrogen, the stream of liquid oxygen; and optionally one or more argon products; and
(g) warming all or a portion of the liquid oxygen stream in the primary heat exchanger to produce the high pressure gaseous oxygen product;
wherein when in the air separation plant operates in a high pressure gaseous oxygen bypass mode, the method further comprises the steps of:
(h) extracting a stream of gaseous oxygen from the lower pressure column at a location above the main condenser-reboiler;
(i) recovering part or all of the refrigeration from the extracted gaseous oxygen stream in the primary heat exchanger; and
(j) reducing the volumetric ratio of the further compressed boiler air stream directed to the primary heat exchanger to the turbine air stream directed to the primary heat exchanger to between about 0.15:1 and 0.35:1.

2. The method of claim 1 wherein between about 10% less power and 20% less power is used to make same volume of liquid nitrogen and liquid oxygen when operating in the high pressure gaseous oxygen bypass mode compared to operating in the high pressure gaseous oxygen full product mode.

3. The method of claim 1 wherein between 5% and 10% additional of liquid products are made when operating in the high pressure gaseous oxygen bypass mode compared to operating in the high pressure gaseous oxygen full product mode.

4. The method of claim 1 wherein the volumetric flow rate of the stream of feed air during the high pressure gaseous oxygen bypass mode is about equal to the first volumetric flow rate.

5. The method of claim 1 wherein the volumetric flow rate of the stream of feed air during the high pressure gaseous oxygen bypass mode is between about 85% and 100% of the first volumetric flow rate.

6. The method of claim 1 wherein the air separation plant is operated in a turndown mode wherein the first volumetric flow rate is less than 85% of the designed volumetric flow rate of the air separation plant.

7. The method of claim 1 wherein the step of reducing the volumetric ratio of the further compressed boiler air stream directed to the primary heat exchanger to the turbine air stream directed to the primary heat exchanger to between about 0.15:1 and 0.35:1 further comprises diverting a portion of the further compressed boiler air stream from a location upstream of the primary heat exchanger to the turbine air circuit.

8. The method of claim 1 wherein the step of reducing the volumetric ratio of the further compressed boiler air stream directed to the primary heat exchanger to the turbine air stream directed to the primary heat exchanger to between about 0.15:1 and 0.35:1 further comprises recirculating a portion of the further compressed boiler air stream from a location upstream of the primary heat exchanger to a location in the boiler air circuit upstream of the boiler air compressor.

9. The method of claim 1 further comprising the step of diverting a portion of the boiler air stream from a location in the boiler air circuit upstream of the boiler air compressor to a location in the boiler air circuit downstream of the boiler air compressor so as to avoid further compression of said portion of the boiler air stream.

10. The method of claim 1 wherein the step of reducing the volumetric ratio of the further compressed boiler air stream directed to the primary heat exchanger to the turbine air stream directed to the primary heat exchanger to between about 0.15:1 and 0.35:1 further comprises diverting a portion of the further compressed boiler air stream from a location upstream of the primary heat exchanger to the turbine air circuit and further comprising the step of diverting a portion of the boiler air stream from a location in the boiler air circuit upstream of the boiler air compressor to a location in the boiler air circuit downstream of the boiler air compressor so as to avoid further compression of said portion of the boiler air stream.

11. The method of claim 1 wherein the boiler air compressor is a multi-stage boiler air compressor arrangement.

12. The method of claim 11 wherein the step of reducing the volumetric ratio of the further compressed boiler air stream directed to the primary heat exchanger to the turbine air stream directed to the primary heat exchanger to between about 0.15:1 and 0.35:1 further comprises diverting a portion of the boiler air stream from an intermediate stage of the multi-stage boiler air compressor arrangement to the turbine air circuit.

13. The method of claim 11 wherein the step of reducing the volumetric ratio of the further compressed boiler air stream directed to the primary heat exchanger to the turbine air stream directed to the primary heat exchanger to between about 0.15:1 and 0.35:1 further comprises further comprises diverting a portion of the boiler air stream from an intermediate stage of the multi-stage boiler air compressor arrangement to a location in the boiler air circuit downstream of the last stage of the multi-stage boiler air compressor arrangement so as to avoid further compression of said portion of the boiler air stream.

14. The method of claim 11 wherein the step of reducing the volumetric ratio of the further compressed boiler air stream directed to the primary heat exchanger to the turbine air stream directed to the primary heat exchanger to between about 0.15:1 and 0.35:1 further comprises diverting a first portion of the boiler air stream from an intermediate stage of the multi-stage boiler air compressor arrangement to the turbine air circuit and further comprising the step of diverting a second portion of the boiler air stream fro

Assignees

• Degenstein Nick J
• Praxair Technology Inc

Inventors

• Degenstein Nick J

Classifications

• F25J3/04836

  Variable air feed, i.e. "load" or product demand during specified periods, e.g. during periods with high respectively low power costs (F25J3/0483 takes precedence) · CPC title

• F25J3/04303

  Lachmann expansion, i.e. expanded into oxygen producing or low pressure column · 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

• F25J2245/40

  the recycled stream being air · CPC title

• F25J2215/54

  Oxygen production with multiple pressure O2 · CPC title