Air distillation process and plant

Claim 2

A process for high-yield argon production by means of an air distillation plant comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10), comprising: sending to the base of a first mixing column section (K1) gaseous nitrogen which may be impure but is substantially without argon, and to the top of a second mixing column section (K2) liquid oxygen which may be impure but is substantially without argon; sending to the base of the second section (K2) at least a part of the top vapor of the first section and to the top of the first section (K1) at least a part of the liquid produced at the base of the second section; withdrawing between the two mixing column sections a fluid flow, and forming from said fluid flow a residual gas which is a mixture of nitrogen and oxygen comprising about 10 to 30% oxygen; discharging from the second section (K2), at the top of the later, impure oxygen containing at the most a few % nitrogen; and discharging from the first section (K1), at the base of the latter, poor liquid (LP1) constituted by nitrogen containing at the most a few % oxygen, and sending this poor liquid as reflux to the main distillation apparatus (1; 1,18; 1,6A; 1A).

Claim 3

A process according to claim 1, in which said impure oxygen contains less than 15% nitrogen.

Claim 4

A process according to claim 1, in which said fluid flow comprises a part of the top vapor (R) of the first section.

Claim 5

A process according to claim 1, in which the main distillation apparatus comprises a double column (1) which itself comprises a medium pressure column (5) operating under a relatively high pressure and a low pressure column (6) operating under a relatively low pressure and connected to the argon producing column (2) through said argon tapping conduit (10), expanding a part of the top vapor of the medium pressure column (5) in a turbine (17), operating the first mixing column section (K1) and the second mixing column section (K2) at the same pressure which is about the low pressure by feeding the first section (K1) with nitrogen withdrawn from the medium pressure column and expanded in said turbine (17) and directly feeding the second section (K2) with liquid oxygen taken from the bottom of the low pressure column (6).

Claim 6

A process according to claim 1, in which said fluid flow comprises a part of the liquid produced at the base of the second section.

Claim 7

A process according to claim 1, in which the main distillation apparatus (1, 18) comprises a double column (1) which itself comprises a medium pressure column (5) operating under a relatively high pressure and a low pressure column (6) operating under a relatively low pressure and connected to the argon producing column (2) through said argon tapping conduit (10), and operating the first and second mixing column sections (K1, K2) at a recycling pressure slightly higher than the low pressure, distilling a part of the treated air at said recycling pressure by using poor liquid as reflux, and feeding the first mixing column section (K1) with impure nitrogen resulting from this distillation.

Claim 8

A process according to claim 6, characterised in that it comprises blowing into the low pressure column (6) the excess turbined air after expansion in a valve (20).

Claim 9

A process for high-yield argon production by means of an air distillation plant comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10), comprising: sending to the base of a first mixing column section (K1) gaseous nitrogen which may be impure but is substantially without argon, and to the top of a second mixing column section (K2) liquid oxygen which may be impure but is substantially without argon; sending to the base of the second section (K2) at least a part of the top vapor of the first section and to the top of the first section (K1) at least a part of the liquid produced at the base of the second section; withdrawing between the two mixing column sections (K1, K2) a part of the liquid (LR1) produced at the base of the second section (K2) and forming therefrom a mixture of nitrogen and oxygen comprising about 10 to 30% oxygen by effecting a remixing of the withdrawn liquid with gaseous nitrogen which may be pure but is substantially without argon in a third mixing column section (K3), the top vapor of this third section constituting residual gas (R1) while the liquid (LP2) produced at its base constitutes refluxing supplementary poor liquid for the main distillation apparatus (1; 1,18; 1,6A; 1A), this liquid being constituted by nitrogen containing at the most a few % oxygen; discharging from the second section (K2), at the top of the latter, impure oxygen containing at the most a few % nitrogen; and discharging from the first section (K1), at the base of the latter, poor liquid (LP1) constituted by nitrogen containing at the most a few % oxygen, and sending this poor liquid as reflux to the main distillation apparatus (1; 1,18; 1,6A; 1A).

Claim 10

A process for high-yield argon production by means of an air distillation plant comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10), comprising: sending to the base of a first mixing column section (K1) gaseous nitrogen which may be impure but is substantially without argon, and to the top of a second mixing column section (K2) liquid oxygen which may be impure but is substantially without argon; sending to the base of the second section (K2) at least a part of the top vapor of the first section and to the top of the first section (K1) at least a part of the liquid produced at the base of the second section; withdrawing between the two mixing column sections (K1, K2) a part of the liquid (LR1) produced at the base of the second section (K2) and forming therefrom a mixture of nitrogen and oxygen comprising about 10 to 30% oxygen by effecting a remixing of the withdrawn liquid with gaseous nitrogen which may be pure but is substantially without argon in a third mixing column section (K3), the top vapor of this third section constituting residual gas (R1) while the liquid (LP2) produced at its base constitutes refluxing supplementary poor liquid for the main distillation apparatus (1; 1,18; 1,6A; 1A), this liquid being constituted by nitrogen containing at the most a few % oxygen; discharging from the second section (K2), at the top of the latter, impure oxygen containing at the most a few % nitrogen; and discharging from the first section (K1), at the base of the latter, poor liquid (LP1) constituted by nitrogen containing at the most a few % oxygen, and sending this poor liquid as reflux to the main distillation apparatus (1; 1,18; 1,6A; 1A).

Claim 11

A process according to claim 8, in which the main distillation apparatus comprises a double column (1) which itself comprises a medium pressure column (5) operating under a relatively high pressure and a low pressure column (6) operating under a relatively low pressure and connected to the argon producing column (2) through said argon tapping conduit (10), and operating the first and second mixing column sections (K1, K2) at the medium pressure by feeding the first section (K1) with nitrogen withdrawn from the medium pressure column (5) and the second section (K2) with liquid oxygen withdrawn from the bottom of the low pressure column (6) and brought to the same pressure.

Claim 12

An air distillation plant having a high-yield argon production, of the type comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10) this installation comprising: a first mixing column section (K1), and means for feeding the base of this section with gaseous nitrogen which may be impure but is substantially without argon; a second mixing column section (K2), and means for feeding the top of this section with liquid oxygen which may be impure but is substantially without argon; means for feeding the base of the second section (K2) with at least a part of the top vapor of the first section and the top of the first section (K1) with at least a part of the liquid produced at the base of the second section; intermediate fluid withdrawing means provided between the two mixing column sections; means for forming from said fluid a residual gas which is a mixture of nitrogen and oxygen comprising about 10 to 30% oxygen; means for discharging said residual gas from the installation; means for sending the liquid (LP1) to the base of the first section (K1) as reflux in the main distillation apparatus (1; 1,18; 1,6A; 1A); and means for discharging from the second section (K2) the top vapor of the latter.

Claim 13

An air distillation plant having a high-yield argon production, of the type comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10) this installation comprising: a first mixing column section (K1), and means for feeding the base of this section with gaseous nitrogen which may be impure but is substantially without argon; a second mixing column section (K2), and means for feeding the top of this section with liquid oxygen which may be impure but is substantially without argon; means for feeding the base of the second section (K2) with at least a part of the top vapor of the first section and the top of the first section (K1) with at least a part of the liquid produced at the base of the second section; intermediate fluid withdrawing means provided between the two mixing column sections; means for forming from said fluid a residual gas which is a mixture of nitrogen and oxygen comprising about 10 to 30% oxygen; means for discharging said residual gas from the installation; means for sending the liquid (LP1) to the base of the first section (K1) as reflux in the main distillation apparatus (1; 1,18; 1,6A; 1A); and means for discharging from the second section (K2) the top vapor of the latter.

Claim 14

A plant according to claim 10, of the type in which the main distillation apparatus (1) comprises a double column which itself comprises a medium pressure column (5) operating under a relatively high pressure and a low pressure column (6) operating under a relatively low pressure and connected to the argon producing column (2) through said argon tapping conduit (10), a turbine (17) for expanding the top vapor of the medium pressure column (5), means connecting an outlet of the turbine to the base of said first section, and means connecting the base of said low pressure column to the top of said second section.

Claim 15

A process for high-yield argon production by means of an air distillation plant comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10), comprising: sending to the base of a first mixing column section (K1) gaseous nitrogen which may be impure but is substantially without argon, and to the top of a second mixing column section (K2) liquid oxygen which may be impure but is substantially without argon; sending to the base of the second section (K2) at least a part of the top vapor of the first section and to the top of the first section (K1) at least a part of the liquid produced at the base of the second section; effecting between the base of the first section (K1) and the top of the second section (K2) at least one intermediate withdrawal (R, LR1) and forming therefrom a mixture of nitrogen and oxygen comprising about 10 to 30% oxygen; discharging from the second section (K2), at the top of the latter, impure oxygen containing at the most a few % nitrogen; and discharging from the first section (K1), at the base of the latter, poor liquid (LP1) constituted by nitrogen containing at the most a few % oxygen, and sending this poor liquid as reflux to the main distillation apparatus (1; 1,18; 1,6A; 1A); and condensing the impure oxygen by vaporization of liquid oxygen of the main distillation apparatus (1A), the liquid obtained being sent as reflux to this column at a level located above the argon tapping conduit (10).

Claim 16

A process for high-yield argon production by means of an air distillation plant comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10), comprising: sending to the base of a first mixing column section (K1) gaseous nitrogen which may be impure but is substantially without argon, and to the top of a second mixing column section (K2) liquid oxygen which may be impure but is substantially without argon; sending to the base of the second section (K2) at least a part of the top vapor of the first section and to the top of the first section (K1) at least a part of the liquid produced at the base of the second section; effecting between the base of the first section (K1) and the top of the second section (K2) at least one intermediate withdrawal (R, LR1) and forming therefrom a mixture of nitrogen and oxygen comprising about 10 to 30% oxygen; discharging from the second section (K2), at the top of the latter, impure oxygen containing at the most a few % nitrogen; and discharging from the first section (K1), at the base of the latter, poor liquid (LP1) constituted by nitrogen containing at the most a few % oxygen, and sending this poor liquid as reflux to the main distillation apparatus (1; 1,18; 1,6A; 1A); and condensing the impure oxygen by vaporization of liquid oxygen of the main distillation apparatus (1A), the liquid obtained being sent as reflux to this column at a level located above the argon tapping conduit (10).

Claim 17

A process for high-yield argon production by means of an air distillation plant comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10), comprising: sending to the base of a first mixing column section (K1) gaseous nitrogen which may be impure but is substantially without argon, and to the top of a second mixing column section (K2) liquid oxygen which may be impure but is substantially without argon; sending to the base of the second section (K2) at least a part of the top vapor of the first section and to the top of the first section (K1) at least a part of the liquid produced at the base of the second section; effecting between the base of the first section (K1) and the top of the second section (K2) at least one intermediate withdrawal (R, LR1) and forming therefrom a mixture of nitrogen and oxygen comprising about 10 to 30% oxygen; discharging from the second section (K2), at the top of the latter, impure oxygen containing at the most a few % nitrogen; and discharging from the first section (K1), at the base of the latter, poor liquid (LP1) constituted by nitrogen containing at the most a few % oxygen, and sending this poor liquid as reflux to the main distillation apparatus (1; 1,18; 1,6A; 1A); the main distillation apparatus comprising a double column (1) which itself comprises a medium pressure column (5) operating under a relatively high pressure and a low pressure column (6) operating under a relatively low pressure and connected to the argon producing column (2) through said argon tapping conduit (10), the process further comprising distilling the impure oxygen in an auxiliary low pressure column (14) fed with the liquid taken from the low pressure column (6) above the argon tapping conduit (10), the top vapor of this auxiliary low pressure column (14) being sent at roughly the same level into the low pressure column (6) while its bottom liquid is sent as reflux into the second mixing column section (K2).

Claim 18

A process for high-yield argon production by means of an air distillation plant comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10), comprising: sending to the base of a first mixing column section (K1) gaseous nitrogen which may be impure but is substantially without argon, and to the top of a second mixing column section (K2) liquid oxygen which may be impure but is substantially without argon; sending to the base of the second section (K2) at least a part of the top vapor of the first section and to the top of the first section (K1) at least a part of the liquid produced at the base of the second section; effecting between the base of the first section (K1) and the top of the second section (K2) at least one intermediate withdrawal (R, LR1) and forming therefrom a mixture of nitrogen and oxygen comprising about 10 to 30% oxygen; discharging from the second section (K2), at the top of the latter, impure oxygen containing at the most a few % nitrogen; and discharging from the first section (K1), at the base of the latter, poor liquid (LP1) constituted by nitrogen containing at the most a few % oxygen, and sending this poor liquid as reflux to the main distillation apparatus (1; 1,18; 1,6A; 1A); the main distillation apparatus comprising a double column (1) which itself comprises a medium pressure column (5) operating under a relatively high pressure and a low pressure column (6) operating under a relatively low pressure and connected to the argon producing column (2) through said argon tapping conduit (10), the process further comprising distilling the impure oxygen in an auxiliary low pressure column (14) fed with the liquid taken from the low pressure column (6) above the argon tapping conduit (10), the top vapor of this auxiliary low pressure column (14) being sent at roughly the same level into the low pressure column (6) while its bottom liquid is sent as reflux into the second mixing column section (K2).

Claim 19

A process for high-yield argon production by means of an air distillation plant comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10), comprising: sending to the base of a first mixing column section (K1) gaseous nitrogen which may be impure but is substantially without argon, and to the top of a second mixing column section (K2) liquid oxygen which may be impure but is substantially without argon; sending to the base of the second section (K2) at least a part of the top vapor of the first section and to the top of the first section (K1) at least a part of the liquid produced at the base of the second section; effecting between the base of the first section (K1) and the top of the second section (K2) at least one intermediate withdrawal (R, LR1) and forming therefrom a mixture of nitrogen and oxygen comprising about 10 to 30% oxygen; discharging from the second section (K2), at the top of the latter, impure oxygen containing at the most a few % nitrogen; and discharging from the first section (K1), at the base of the latter, poor liquid (LP1) constituted by nitrogen containing at the most a few % oxygen, and sending this poor liquid as reflux to the main distillation apparatus (1; 1,18; 1,6A; 1A); and using the residual gas (R, R1) for regenerating adsorption cylinders serving to purify the incoming air.

Claim 20

A process for high-yield argon production by means of an air distillation plant comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10), comprising: sending to the base of a first mixing column section (K1) gaseous nitrogen which may be impure but is substantially without argon, and to the top of a second mixing column section (K2) liquid oxygen which may be impure but is substantially without argon; sending to the base of the second section (K2) at least a part of the top vapor of the first section and to the top of the first section (K1) at least a part of the liquid produced at the base of the second section; effecting between the base of the first section (K1) and the top of the second section (K2) at least one intermediate withdrawal (R, LR1) and forming therefrom a mixture of nitrogen and oxygen comprising about 10 to 30% oxygen; discharging from the second section (K2), at the top of the latter, impure oxygen containing at the most a few % nitrogen; and discharging from the first section (K1), at the base of the latter, poor liquid (LP1) constituted by nitrogen containing at the most a few % oxygen, and sending this poor liquid as reflux to the main distillation apparatus (1; 1,18; 1,6A; 1A); and using the residual gas (R, R1) for regenerating adsorption cylinders serving to purify the incoming air.

Claim 21

An air distillation plant having a high-yield argon production, of the type comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10) this installation comprising: a first mixing column section (K1), and means for feeding the base of this section with gaseous nitrogen which may be impure but is substantially without argon; a second mixing column section (K2), and means for feeding the top of this section with liquid oxygen which may be impure but is substantially without argon; means for feeding the base of the second section (K2) with at least a part of the top vapor of the first section and the top of the first section (K1) with at least a part of the liquid produced at the base of the second section; intermediate withdrawing means provided between the base of the first section (K1) and the top of the second section (K2); means for sending the liquid (LP1) to the base of the first section (K1) as reflux in the main distillation apparatus (1; 1,18; 1,6A; 1A); means for discharging from the second section (K2) the top vapor of the latter; a third mixing column section (K3), means for feeding the base of this section with gaseous nitrogen which may be impure but is substantially without argon and its top with liquid (LR1) withdrawn through said intermediate withdrawing means, and means for withdrawing from the top of this third section a residual gas of the plant (R1).

Claim 22

An air distillation plant having a high-yield argon production, of the type comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10) this installation comprising: a first mixing column section (K1), and means for feeding the base of this section with gaseous nitrogen which may be impure but is substantially without argon; a second mixing column section (K2), and means for feeding the top of this section with liquid oxygen which may be impure but is substantially without argon; means for feeding the base of the second section (K2) with at least a part of the top vapor of the first section and the top of the first section (K1) with at least a part of the liquid produced at the base of the second section; intermediate withdrawing means provided between the base of the first section (K1) and the top of the second section (K2); means for sending the liquid (LP1) to the base of the first section (K1) as reflux in the main distillation apparatus (1; 1,18; 1,6A; 1A); means for discharging from the second section (K2) the top vapor of the latter; a third mixing column section (K3), means for feeding the base of this section with gaseous nitrogen which may be impure but is substantially without argon and its top with liquid (LR1) withdrawn through said intermediate withdrawing means, and means for withdrawing from the top of this third section a residual gas of the plant (R1).

Claim 23

An air distillation plant having a high-yield argon production, of the type comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10) this installation comprising: a first mixing column section (K1), the means for feeding the base of this section with gaseous nitrogen which may be impure but is substantially without argon; a second mixing column section (K2), and means for feeding the top of this section with liquid oxygen which may be impure but is substantially without argon; means for feeding the base of the second section (K2) with at least a part of the top vapor of the first section and the top of the first section (K1) with at least a part of the liquid produced at the base of the second section; intermediate withdrawing means provided between the base of the first section (K1) and the top of the second section (K2); means for sending the liquid (LP1) to the base of the first section (K1) as reflux in the main distillation apparatus (1; 1,18; 1,6A; 1A); means for discharging from the second section (K2) the top vapor of the latter; the main distillation apparatus (1) comprising a double column which itself comprises a medium pressure column (5) operating under a relatively high pressure and a low pressure column (6) operating under a relatively low pressure and connected to the argon producing column (2) through said argon tapping conduit (10), an auxiliary column section (14) fed at its top with liquid withdrawn from the low pressure column (6) above the argon tapping conduit (10), means for returning the top vapor of this auxiliary column into the low pressure column roughly at the same level, the auxiliary section (14) being fed at its base with the top vapor of the second mixing column section (K2) while the bottom liquid of this auxiliary section is sent as reflux to the top of the second mixing column section.

Claim 24

An air distillation plant having a high-yield argon production, of the type comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10) this installation comprising: a first mixing column section (K1), the means for feeding the base of this section with gaseous nitrogen which may be impure but is substantially without argon; a second mixing column section (K2), and means for feeding the top of this section with liquid oxygen which may be impure but is substantially without argon; means for feeding the base of the second section (K2) with at least a part of the top vapor of the first section and the top of the first section (K1) with at least a part of the liquid produced at the base of the second section; intermediate withdrawing means provided between the base of the first section (K1) and the top of the second section (K2); means for sending the liquid (LP1) to the base of the first section (K1) as reflux in the main distillation apparatus (1; 1,18; 1,6A; 1A); means for discharging from the second section (K2) the top vapor of the latter; the main distillation apparatus (1) comprising a double column which itself comprises a medium pressure column (5) operating under a relatively high pressure and a low pressure column (6) operating under a relatively low pressure and connected to the argon producing column (2) through said argon tapping conduit (10), an auxiliary column section (14) fed at its top with liquid withdrawn from the low pressure column (6) above the argon tapping conduit (10), means for returning the top vapor of this auxiliary column into the low pressure column roughly at the same level, the auxiliary section (14) being fed at its base with the top vapor of the second mixing column section (K2) while the bottom liquid of this auxiliary section is sent as reflux to the top of the second mixing column section.

Claim 25

An air distillation plant having a highyield argon production, of the type comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10) this installation comprising: a first mixing column section (K1), and means for feeding the base of this section with gaseous nitrogen which may be impure but is substantially without argon; a second mixing column section (K2), and means for feeding the top of this section with liquid oxygen which may be impure but is substantially without argon; means for feeding the base of the second section (K2) with at least a part of the top vapor of the first section and the top of the first section (K1) with at least a part of the liquid produced at the base of the second section; intermediate withdrawing means provided between the base of the first section (K1) and the top of the second section (K2); means for sending the liquid (LP1) to the base of the first section (K1) as reflux in the main distillation apparatus (1; 1,18; 1,6A; 1A); means for discharging from the second section (K2) the top vapor of the latter; the main distillation apparatus (1, 18) comprising a double column (1) which itself comprises a medium pressure column (5) operating under a relatively high pressure and a low pressure column (6) operating under a relatively low pressure and connected to the argon producing column (2) through said argon tapping conduit (10), and a turbine (19) for expanding a part of the incoming air and a second auxiliary column section (18) operating at a pressure slightly higher than the low pressure and producing at the top impure nitrogen which is fed to the base of the first mixing column section (K1).

Claim 26

An air distillation plant having a highyield argon production, of the type comprising a main distillation apparatus (1; 1,18; 1,6A; 1A) associated with an argon producing column (2) through an argon tapping conduit (10) this installation comprising: a first mixing column section (K1), and means for feeding the base of this section with gaseous nitrogen which may be impure but is substantially without argon; a second mixing column section (K2), and means for feeding the top of this section with liquid oxygen which may be impure but is substantially without argon; means for feeding the base of the second section (K2) with at least a part of the top vapor of the first section and the top of the first section (K1) with at least a part of the liquid produced at the base of the second section; intermediate withdrawing means provided between the base of the first section (K1) and the top of the second section (K2); means for sending the liquid (LP1) to the base of the first section (K1) as reflux in the main distillation apparatus (1; 1,18; 1,6A; 1A); means for discharging from the second section (K2) the top vapor of the latter; the main distillation apparatus (1, 18) comprising a double column (1) which itself comprises a medium pressure column (5) operating under a relatively high pressure and a low pressure column (6) operating under a relatively low pressure and connected to the argon producing column (2) through said argon tapping conduit (10), and a turbine (19) for expanding a part of the incoming air and a second auxiliary column section (18) operating at a pressure slightly higher than the low pressure and producing at the top impure nitrogen which is fed to the base of the first mixing column section (K1).