Patent Application
20120297823
The present invention relates to processes and devices for the separation of air by cryogenic distillation. It is known to distill air in a double column comprising a medium-pressure column connected thermally to a low-pressure column which surmounts it.
The thermal connection between the two columns can be obtained by using two evaporators placed one above the other in the low-pressure column. The lower evaporator can be heated by means of a nitrogen flow withdrawn from the medium-pressure column and then compressed in a cold compressor, and the upper evaporator can be heated by a flow of medium-pressure nitrogen taken from the medium-pressure column without having been compressed upstream of the evaporator.
A cold compressor is a compressor having a cryogenic inlet temperature, a cryogenic temperature being less than −50° C.
The nitrogen compressed in the cold compressor has to be condensed in the lower evaporator of the low-pressure column. The fluid compressed under cold conditions thus arrives relatively warm in the evaporator, with a high ΔT, before beginning to condense: this means that even if the evaporator has a low temperature pinch, the ΔT at the hot end is relatively high.
If the evaporator/condenser malfunctions, in particular if a partial blockage or poor distribution occurs, there is a high risk of evaporation to dryness locally, which is harmful to the safety of the device due to the presence of impurities of CnHm type with an oxygen-rich fluid. This is all the more appreciable on a falling-film evaporator/condenser.
FR-A-2 930 329 describes a process according to the preamble to claim 1.
One of the aims of the invention is to overcome malfunctions of the evaporator/condenser.
According to the invention, a calorigenic fluid, for example medium-pressure nitrogen, is cooled at the outlet of a cold compressor, by injecting a portion of the condensed fluid into the evaporator/condenser at the inlet of the evaporator/condenser, in order to bring it to its dew point, before being condensed. This makes it possible to nullify the overheating of the fluid and makes possible a use which is easier in terms of safety for the evaporator, in particular a falling-film evaporator. This takes place without a significant energy penalty.
Injection of other cryogenic fluids can replace this condensed fluid.
According to a subject matter of the invention, provision is made for a process for the separation of air in a system of columns by cryogenic distillation in which compressed air, purified and cooled, is separated in the system of columns in order to form an oxygen-enriched flow and a nitrogen-enriched flow, in which at least one column of the system of columns comprises an evaporator/condenser which has to ensure the evaporation of a liquid enriched in oxygen with respect to the air by means of an exchange of heat with a calorigenic fluid, the calorigenic fluid having been compressed upstream of the evaporator/condenser in a compressor having a cryogenic inlet temperature, the calorigenic fluid being at least partially condensed in the evaporator/condenser, characterized in that a cryogenic liquid is added to the calorigenic fluid upstream of the evaporator/condenser.
According to other optional characteristics:
According to another subject matter of the invention, provision is made for a device for the separation of air in a system of columns by cryogenic distillation, comprising:
The device can comprise the following characteristics:
The invention also comprises an oxy-combustion plant comprising an air separation device as described above and a boiler fed with the oxygen produced by the air separation device.
The invention will be described in more detail with reference to the FIGURE, which shows a process according to the invention.
A flow of air 1 is compressed in a compressor (not illustrated) up to 4 bar and then divided into two; a portion 3 of the air is cooled in an exchange line 9 and is sent to the medium-pressure column 11 of a double column. The double column comprises a medium-pressure column 11 and a low-pressure column 13 connected thermally to one another, the low-pressure column surmounting the medium-pressure column.
The remainder 5 of the air is boosted in a booster 7, cooled in the exchange line, condensed in a product evaporator 23 and then sent to the medium-pressure column 11.
The low-pressure column 13 comprises a vessel evaporator and an intermediate evaporator 17. The intermediate evaporator 17 is heated by means of a fraction 33 of a nitrogen flow 31 drawn off from the medium-pressure column at the pressure of the top of the medium-pressure column.
Another fraction 37 of the medium-pressure nitrogen is compressed in a compressor 61 having a cryogenic inlet temperature. The fraction is cooled at the outlet of this cold compressor 61 by direct contact with a cryogenic liquid 45, in order to be brought to its dew point, before being condensed. The cryogenic liquid 45 preferentially comprises a portion of the fluid which has just been condensed in the vessel evaporator 15. The cryogenic liquid comprises at least 70 mol % of nitrogen, indeed even at least 90 mol % of nitrogen. Thus, a pipe brings, to the outlet of the cold compressor, a portion of the nitrogen condensed in the vessel evaporator.
The operation in which the gas and the liquid 45 are brought into contact can be carried out directly in the pipeline or in a specific installation, using injection nozzles, physical contactors, the liquid 45 being compressed either by hydrostatic height or using a pump.
The remainder of the liquid condensed in the vessel evaporator 15 is sent in part to the top of the low-pressure column 13 to form reflux.
An oxygen-enriched liquid 49 and a nitrogen-enriched liquid 53 are sent from the medium-pressure column 11 to the low-pressure column 13.
A flow of liquid oxygen 19 is withdrawn from the vessel of the low-pressure column, pressurized up to a low pressure of 1.5 to 4 bar by a pump 21 and then evaporated in an evaporator 23 by an exchange of heat with the air. A non-evaporated portion of the oxygen is withdrawn as bleed 25.
The vessel evaporator 15 is preferably a falling-film evaporator.
A portion 39 of the medium-pressure nitrogen is reheated in the exchange line 9, is reduced in pressure in a turbine 41 and is then again reheated in the exchange line 9.
The invention applies to any gas compressed in a cold compressor, which has to condense in an evaporator where there is a risk of evaporation to dryness with regard to oxygen in the presence of an impurity of CnHm type.
In the example, the cryogenic liquid added upstream of the cold compressor comes from the system of columns but the liquid can originate from an external source and can, for example, be taken from a storage tank for feed liquid or for liquid stored in a weighing system.
| Number | Date | Country | Kind |
|---|---|---|---|
| 1050775 | Feb 2010 | FR | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/FR2011/050212 | 2/3/2011 | WO | 00 | 7/31/2012 |
