Plant and method for low-temperature air separation
Abstract
The invention relates to a plant for low-temperature air separation, having a rectification column system comprising a high-pressure column, a divided low-pressure column and a divided argon column, and a cold box system comprising a first cold box and a second cold box. The high-pressure column is arranged beneath the lower section of the low-pressure column. The high-pressure column together with the lower section of the low-pressure column is located in the first cold box, and the top section of the low-pressure column in the second cold box. It is proposed to arrange the base section of the argon column in the first cold box and the top section of the argon column in the second cold box, or vice versa. The present invention likewise provides a corresponding method.
Claims
exact text as granted — not AI-modified1 . A plant for low-temperature air separation, having a rectification column system comprising a high-pressure column, a low-pressure column and an argon column, and a cold box system having a first cold box perimeter and a second cold box, wherein
the low-pressure column is divided into at least a base section and a top section, the base section and the top section of the low-pressure column are arranged next to one another in such a manner that an orthogonal projection of the base section of the low-pressure column onto the horizontal plane does not intersect with an orthogonal projection of the top section of the low-pressure column onto the horizontal plane, the high-pressure column is arranged below the base section of the low-pressure column in such a manner that an orthogonal projection of the high-pressure column onto the horizontal plane intersects with the orthogonal projection of the base section of the low-pressure column onto the horizontal plane, the high-pressure column together with the base section of the low-pressure column is located in the first cold box and the top section of the low-pressure column is arranged in the second cold box, wherein the argon column is divided at least into a base section and a top section, wherein the base section and the top section of the argon column are arranged next to one another in such a manner that an orthogonal projection of the base section of the argon column onto the horizontal plane does not intersect with an orthogonal projection of the top section of the argon column, wherein the base section of the argon column is arranged in the first cold box, and the top section of the argon column is arranged in the second cold box, or the base section of the argon column is arranged in the second cold box and the top section of the argon column is arranged in the first cold box.
2 . The plant according to claim 1 , wherein the argon column is designed as a crude argon column and further a pure argon column is provided, wherein the pure argon column is arranged in the first cold box or the second cold box, in particular in the cold box in which the top section of the argon column designed as a crude argon column is arranged.
3 . The plant according to claim 1 , wherein the rectification column arrangement has a pure oxygen column.
4 . The plant according to claim 3 , wherein the pure oxygen column is arranged in the first cold box, the second cold box or an additionally provided third cold box.
5 . The plant according to claim 3 , wherein the pure oxygen column and the base section of the argon column are arranged side by side in such a way that an orthogonal projection of at least one upper part of the pure oxygen column onto the horizontal plane does not overlap with the orthogonal projection of the base section of the argon column onto the horizontal plane.
6 . The plant according to claim 3 , wherein the pure oxygen column has a feed point for a first transfer liquid and the base section of the argon column has an extraction point for the first transfer liquid, wherein the pure oxygen column and the base section of the argon column are arranged such that the extraction point for the first transfer liquid is geodetically above the feed point for the first transfer liquid.
7 . The plant according to claim 6 , wherein the extraction point for the first transfer liquid is 1 to 30, preferably 1 to 15, theoretical plates above a sump of the base section of the argon column.
8 . The plant according to claim 1 , wherein the base section of the argon column has a feed point for a second transfer liquid, and the top section of the low-pressure column has an extraction point for the second transfer liquid, wherein the top section of the low-pressure column and the base section of the argon column are arranged such that the extraction point for the second transfer liquid is above the feed point for the second transfer liquid.
9 . The plant according to claim 1 , comprising a subcooling heat exchanger which is arranged in the first or second cold box, in particular in the second cold box below the top section of the low-pressure column.
10 . The plant according to claim 1 , wherein the top section of the low-pressure column has a feed point for a second transfer liquid, and the base section of the argon column has an extraction point for the second transfer liquid, wherein the base section of the argon column and the top section of the low-pressure column are arranged in such a way that the extraction point for the second transfer liquid is above the feed point for the second transfer liquid.
11 . The plant according to claim 10 , comprising a subcooling heat exchanger which is arranged below the base section of the argon column.
12 . The plant according to claim 1 , in which all cold apparatus parts are arranged in the first or the second cold box and no third cold box is used.
13 . A method for the low temperature separation of air, wherein a system according to claim 1 .Cited by (0)
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