Separation of air
AssigneeThe BOC Group, Inc.
InventorPaul Higginbotham
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AssigneeThe BOC Group, Inc.
InventorPaul Higginbotham
Estimating the term…
A first stream of air is compressed in a main air compressor and a booster compressor is cooled at a first pressure by passage through a main heat exchanger. The cooled stream is introduced without further compression into the higher pressure column of a double rectification column including in addition to the column a lower pressure column and a condenser-reboiler. A second stream of compressed air is expanded from a second pressure in an expansion turbine with the performance of external work. The expanded second stream of air is introduced into the lower pressure column. An oxygen product, typically impure, is taken from the bottom region of the lower pressure column. The second pressure is less than the first pressure column. The second pressure is less than the first pressure, the second air stream being taken from intermediate the compressors.
A method of separating air by rectification including cooling a first stream of compressed air taken from a first compression stage, at a first pressure, in a main heat exchanger to a temperature suitable for its separation by rectification, introducing the cooled first stream without further compression into the higher pressure column of a double rectification column including, in addition to the higher pressure column, a lower pressure column, in which a bottom liquid oxygen fraction is formed and a condenser-reboiler placing the higher pressure column in indirect heat exchange relationship with the lower pressure column, expanding in an expansion turbine from a second pressure with the performance of external work a second stream of compressed air taken from a second compression stage at the second pressure, introducing the expanded second stream of air into the lower pressure column, and taking an oxygen product from the bottom region of the lower pressure column, wherein the second pressure is less than the first pressure, the cooled first stream is introduced into the higher pressure column at essentially the first pressure, the first compression stage is downstream of the second compression stage, and the expansion turbine is the sole expansion turbine used in the method.
A plant for separating air by rectification comprising at least two compression stages in series for compressing a flow of air, a main heat exchanger having at least one first passage for the cooling at a first pressure of a first stream of the compressed air to a temperature suitable for its rectification, the at least one first passage communicating with a first chosen one of the compression stages, whereby the first pressure is essentially the outlet pressure of the first chosen compression stage, and at least one second passage for the cooling at a second pressure of a second stream of the compressed air to a temperature above that suitable for its rectification, the at least one second passage communicating with a second chosen one of the compression stages whereby the second pressure is essentially the outlet pressure of the second chosen compression stage, a double rectification column including a higher pressure column, a lower pressure column, and a condenser-reboiler placing the higher pressure column in indirect heat exchange relationship with the lower pressure column, the higher pressure column being arranged to operate under a pressure at its bottom not greater than the first pressure, and the lower pressure column being arranged to operate so as to produce therein an bottom liquid oxygen fraction;
A plant for separating air by rectification comprising at least two compression stages in series for compressing a flow of air, a main heat exchanger having at least one first passage for the cooling at a first pressure of a first stream of the compressed air to a temperature suitable for its rectification, the at least one first passage communicating with a first chosen one of the compression stages, whereby the first pressure is essentially the outlet pressure of the first chosen compression stage, and at least one second passage for the cooling at a second pressure of a second stream of the compressed air to a temperature above that suitable for its rectification, the at least one second passage communicating with a second chosen one of the compression stages whereby the second pressure is essentially the outlet pressure of the second chosen compression stage, a double rectification column including a higher pressure column, a lower pressure column, and a condenser-reboiler placing the higher pressure column in indirect heat exchange relationship with the lower pressure column, the higher pressure column being arranged to operate under a pressure at its bottom not greater than the first pressure, and the lower pressure column being arranged to operate so as to produce therein an bottom liquid oxygen fraction;
Dependencies are inferred from the claim text.