Method and device for the low-temperature separation of air at variable energy consumption

• US 10,458,702 B2
• Filed: 06/25/2015
• Issued: 10/29/2019
• Est. Priority Date: 07/05/2014
• Status: Active Grant

• Current Assignee: Linde AG (Linde Plc)
• Original Assignee: Linde Aktingesellschaft
• Inventors: Golubev, Dimitri
• Primary Examiner(s): Alosh, Tareq
• Application Number:
  US15/322,468
• Publication Number:
  US 20170131028A1
• Time in Patent Office: 1,587 Days
• CPC Class Codes: F25J 2205/04 in the feed line, i.e. upstream of the fractionation step
• CPC Class Codes: F25J 2240/42 the fluid being air
• CPC Class Codes: F25J 2245/50 the recycled stream being oxygen
• CPC Class Codes: F25J 3/04018 of main feed air
• CPC Class Codes: F25J 3/04024 of purified feed air, so-called boosted air
• CPC Class Codes: F25J 3/0403 of nitrogen
• CPC Class Codes: F25J 3/04054 of air
• CPC Class Codes: F25J 3/04084 of nitrogen
• CPC Class Codes: F25J 3/0409 of oxygen
• CPC Class Codes: F25J 3/04175 at a pressure of substantially more than the highest pressure column
• CPC Class Codes: F25J 3/042 having an intermediate feed connection
• CPC Class Codes: F25J 3/0429 of feed air, e.g. used as waste or product air or expanded into an auxiliary column
• CPC Class Codes: F25J 3/04296 Claude expansion, i.e. expanded into the main or high pressure column
• CPC Class Codes: F25J 3/04345 and comprising a gas work expansion loop
• CPC Class Codes: F25J 3/04393 using multiple or multistage gas work expansion
• CPC Class Codes: F25J 3/04412 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 Class Codes: F25J 3/04678 cooled by oxygen enriched liquid from high pressure column bottoms
• CPC Class Codes: F25J 3/04721 Producing pure argon, e.g. recovered from a crude argon column
• CPC Class Codes: F25J 3/04812 Different modes, i.e. "runs" of operation F25J3/04472 takes precedence

Abstract

A method and device used to variably obtain a compressed-gas product by means low-temperature separation of air in a distillation column system. In a first operating mode, a first amount of first compressed-gas product is obtained, and, in a second operating mode, a second, smaller amount is obtained. In the first operating mode, a first amount of air is compressed in the main air compressor, and in the second operating mode, a second, larger amount is compressed in the main air compressor.

Claims

1. A method for obtaining a pressurized-gas product by means of the low-temperature separation of air in a distillation column system, which has a high-pressure column and a low-pressure column, said method comprising:

compressing feed air, containing at least 78 mol % of nitrogen, in a main air compressor from an inlet pressure to a first pressure, wherein said first pressure is at least 4 bar higher than an operating pressure of the high-pressure column, said feed air constituting a first process stream and wherein said main air compressor is a multi-stage compressor,

cooling a first partial stream of the compressed feed air in the main air compressor to an intermediate temperature in a main heat exchanger and expanding the cooled first partial stream in a first air turbine whereby work is performed,

introducing at least a first part of the expanded first partial stream into the distillation column system,

compressing a second partial stream of the compressed feed air from the main air compressor to a second pressure, which is higher than the first pressure, in a first booster air compressor, which is driven by the first air turbine, cooling the compressed second partial stream in the main heat exchanger, and subsequently expanding the second partial stream and introducing the second partial stream into the distillation column system,

removing a first product stream in liquid form from the distillation column system and increasing the pressure of the first product stream to a first product pressure,

evaporating or pseudo-evaporating the first product stream under the first product pressure and warming the first product stream in the main heat exchanger,

removing the warmed first product stream as first pressurized-gas product, and

wherein, in a first operating mode, a first amount of said first pressurized-gas product is obtained, and a first amount of a second process stream containing at least 78 mol % of nitrogen is mixed with the first process stream downstream of a first stage of the multi-stage compressor, wherein said second process stream is a part of the expanded first partial stream, and wherein said first amount of said second process stream can be zero, and

wherein, in a second operating mode, a second amount of said first pressurized-gas product is obtained, wherein said second amount of said first pressurized-gas product is smaller than said first amount of said first pressurized-gas product, and a second amount of said second process stream is mixed with the first process stream downstream of a first stage of the multi-stage compressor, wherein said second amount of said second process stream is greater than said first amount of the second process stream.

2. The method as claimed in claim 1, wherein the second process stream is mixed with the first process stream at an intermediate stage of the multi-stage compressor.

3. The method as claimed in claim 1, wherein, in the second operating mode, an oxygen gas stream is removed from a lower region of the low-pressure column and mixed with a nitrogen-enriched stream from an upper region of the low-pressure column and the resultant mixture is warmed in the main heat exchanger.

4. The method as claimed in claim 1, further comprising

cooling a third partial stream of the compressed feed air compressed to an intermediate temperature in the main heat exchanger and expanded in a second air turbine whereby work is performed, and

introducing at least a first part of the expanded third partial stream into the distillation column system.

5. The method as claimed in claim 4, wherein,

downstream of the first booster air compressor, the second partial stream of the compressed feed air is cooled to an intermediate temperature in the main heat exchanger, the second partial stream is further compressed to a third pressure in a second booster air compressor wherein said third pressure is higher than the first pressure, and said second booster air compressor is a cold compressor and is driven by the second air turbine, the second partial stream is then cooled under the third pressure in the main heat exchanger, and subsequently the second partial stream is expanded and introduced into the distillation column system.

6. The method as claimed in claim 4, further comprising cooling a fourth partial stream of the compressed feed air, under the first pressure in the main heat exchanger and subsequently expanding the fourth partial stream and introducing the expanded fourth partial stream into the distillation column system.

7. The method as claimed in claim 6, wherein

the third partial stream is expanded in the second air turbine to a pressure that is at least one bar higher than the operating pressure of the high-pressure column, and

the expanded third partial stream is cooled in the main heat exchanger and subsequently introduced into the distillation column system.

8. The method as claimed in claim 1, wherein

in the first operating mode, a first amount of feed air is compressed in the main air compressor and

in the second operating mode, a second amount of feed air is compressed in the main air compressor,

wherein the ratio of the second amount of feed air to the first amount of feed air is greater than the ratio of the second amount of first pressurized-gas product to the first amount of first pressurized-gas product.

10. The method as claimed in claim 4, wherein the turbine inlet pressure of the second air turbine is equal to the first pressure.

11. The method as claimed in claim 8, wherein the ratio of the second amount of feed air to the first amount of feed air is more than 3% higher than the ratio of the second amount of first pressurized-gas product to the first amount of first pressurized-gas product.

12. The method as claimed in claim 1, further comprising compressing a third process stream in a nitrogen product compressor from an inlet pressure to a final pressure, wherein said third process stream is formed by a first gaseous nitrogen stream from the low-pressure column.

9. An apparatus for producing a pressurized-gas product by means of low-temperature separation of air, said apparatus comprising:

a distillation column system having a high-pressure column and a low-pressure column,

a main air compressor which is a multi-stage compressor for compressing feed air to a first pressure, which is at least 4 bar higher than an operating pressure of the high-pressure column,

a main heat exchanger comprising means for cooling a first partial stream of compressed feed air to an intermediate temperature,

a first air turbine for expanding the cooled first partial stream such that work is performed,

means for introducing the expanded first partial stream into the distillation column system,

a first booster air compressor for further compressing a second partial stream of compressed feed air to a second pressure, which is higher than the first pressure, wherein the booster air compressor is driven by the first turbine,

said main heat exchanger further comprising means for cooling the further compressed second partial stream,

means for expanding the cooled second partial stream and means for introducing the expanded second partial stream into the distillation column system,

means for removing a first product stream in a liquid form from the distillation column system and means for increasing the pressure of the first product stream to a first product pressure,

said main heat exchanger further comprising means for evaporating or pseudo-evaporating the first product stream under the first product pressure and then warming the first product stream,

means for obtaining the warmed first product stream as a first pressurized-gas product,

said multi-stage compressor compressing a first process stream which is said feed air and which contains at least 78 mol % of nitrogen, from an inlet pressure to a final pressure,

means for mixing a second process stream, which contains at least 78 mol % of nitrogen, with the first process stream downstream of a first stage of the multi-stage compressor, the second process stream being formed by part of the expanded first partial stream,

means for switching over between a first operating mode and a second operating mode, wherein said means for switching over provides for;

in the first operating mode, obtaining a first amount of first pressurized-gas product, and compressing a first amount of the second process stream in the multi-stage compressor from an inlet pressure to a final pressure, wherein said first amount of the second process stream can be zero, and

in a second operating mode, obtaining a second amount of first pressurized-gas product, which is smaller than the first amount first pressurized-gas product, and compressing a second amount of the second process stream, which is greater than the first amount of the second process stream, in the multi-stage compressor.