Method and installation for producing breathable air

• US 20060060082A1
• Filed: 02/05/2003
• Published: 03/23/2006
• Est. Priority Date: 02/07/2002
• Status: Active Grant

• Current Assignee: Commissariat a L'Energie Atomique (AES Corporation), Compagnie Generale DES Etablissements Michelin SCA
• Original Assignee: Commissariat a L'Energie Atomique (AES Corporation), Compagnie Generale DES Etablissements Michelin SCA
• Inventors: Barre, Didier, Baudet, Roland
• Granted Patent: US 7,309,376 B2
• Time in Patent Office: Days
• US Class Current: 95/117
• CPC Class Codes: A62B 15/00 Installations affording protection against poisonous or injurious substances, e.g. with separate breathing apparatus preventing escape of dirt or fumes from the area where they are produced B08B15/00; building aspects E04H9/00 ; use of air currents for screening F24F9/00
• CPC Class Codes: A62B 7/14 for high-altitude aircraft
• CPC Class Codes: A62B 9/003 Means for influencing the temperature or humidity of the breathing gas
• CPC Class Codes: Y10S 55/17 Compressed air water removal

Abstract

The invention relates to a process for producing respirable air comprising the following stages: treatment of compressed air comprising an air-drying operation rehumidification of the treated dry air.

According to the invention, the rehumidification stage of the treated dry air comprises an operation of controlled distribution of the treated dry air on the one hand in a rehumidification line (24), and on the other hand in a dry line (22).

The invention also relates to an installation (1) for utilising such a process. Application to the area of nuclear installation dismantling.

Claims

1. A process for production of respirable air comprising the following stages:

treatment of compressed air comprising an operation for drying the air;

rehumidification of the treated dry air, characterised in that the rehumidification stage of the treated dry air comprises an operation for controlled distribution of the treated dry air on the one hand in a rehumidification line (24), and on the other hand in a dry line (22).

2. The process as claimed in claim 1, characterised in that the distribution of treated dry air is controlled by means of a regulating valve (38) mounted on the rehumidification line (24) and controlled by pilot means (48) sensitive to the signal emitted by a probe (42) measuring the rate of humidity, said probe (42) being mounted on an outlet pipe (26), attached at one end to the rehumidification line (24), and at the other end to the dry line (22).

3. The process as claimed in claim 2, characterised in that a difference in pressure is created between the rehumidification line (24) and the dry line (22), so as to favour the passing of treated dry air coming from the dry line (22), in the outlet pipe (26).

4. The process as claimed in any one of the preceding claims, characterised in that the processing stage of compressed air comprises the following operations:

filtering of condensates in the compressed air;

drying the air so as to eliminate any trace of humidity in the air;

filtering dust dislodged during the drying operation;

transformation of carbon monoxide contained in the compressed air to carbon dioxide;

filtering the air by means of an active carbon filter (16).

5. The process as claimed in any one of the preceding claims, characterised in that the processing stage of the compressed air is followed by a permanent analysis stage of quantities of carbon monoxide and carbon dioxide present in the treated air, then by an alert stage when the values of these quantities exceed maximum values to be respected.

6. The process as claimed in any one of the preceding claims, characterised in that after the rehumidification stage of the treated dry air the air has a rate of humidity of between approximately 40 and 50%.

7. The process as claimed in any one of the preceding claims, characterised in that the rehumidified treated air is provided to supply at least one ventilated suit of an operator carrying out dismantling work on nuclear installations.

8. An installation (1) for production of respirable air comprising:

processing means (2) for compressed air comprising means for drying the air (11);

rehumidification means (4) of treated dry air;

characterised in that the rehumidification means (4) of the treated dry air comprise a rehumidification line (24) and a dry line (22), as well as distribution means (38) for controlled distribution of the treated dry air in each of said lines (22, 24).

9. An installation (1) as claimed in claim 8, characterised in that the rehumidification means (4) of the treated dry air also comprise:

an inlet pipe (18) containing treated dry air attached at one end to a main pipe of dry air (28) constituting the dry line (22), and at the other end to a pipe for derivation of dry air (32) belonging to the rehumidification line (24);

an outlet pipe (26) attached ay one end to a pipe of air saturated in humidity (36) belonging to the rehumidification line (24), and at the other end to said main dry air pipe (28)

a water tank (34) belonging to the rehumidification line (24), communicating at one end with said pipe for derivation of dry air (32), and at the other end with said pipe of air saturated in humidity (36).

10. The installation (1) as claimed in claim 9, characterised in that the means for distributing the treated dry air are made up of a regulating valve (38) mounted on said pipe for derivation of dry air (32), said regulating valve being controlled by pilot means (48), sensitive to the signal emitted by a probe (42) measuring the rate of humidity, mounted on said outlet pipe (26).

11. The installation (1) as claimed in claim 9 or the claim 10, characterised in that the rehumidification means (4) of the treated dry air further comprise an anti-return valve (30) with known loss of load, mounted on said main dry air pipe (28).

12. The installation (1) as claimed in claim 11, characterised in that the anti-return valve (30) with known load loss causes a drop in pressure in the main dry air pipe (28) of around 300 mbar.

13. The installation (1) as claimed in any one of claims 9 to 12, characterised in that the rehumidification means (4) of the treated dry air further comprise an anti-return valve (40) mounted on said pipe of air saturated in humidity (36).

14. The installation (1) as claimed in any one of claims 8 to 13, characterised in that the processing means (2) for compressed air comprise:

an oil separator filter (6) at 0.01 ppm;

an adsorption dryer (11) with a dew point of −

73°

C.;

a 1-micron particle filter (13);

a catalyst (14) for transforming carbon monoxide into carbon dioxide;

an active carbon filter (16).

15. The installation (1) as claimed in any one of claims 8 to 14, characterised in that it further comprises, at the outlet processing means (2) for compressed air, analysis means (44) for permanently controlling the quantities of carbon monoxide and carbon dioxide present in the treated air.

16. The installation (1) as claimed in claim 15, characterised in that the analysis means (44) communicate with the pilot means (48) for controlling triggering a sound and/or visual alarm, and/or deflection to a reserve of treated air (50), and/or a change in the source of compressed air.

17. The installation (1) as claimed in any one of claims 8 to 16, characterised in that it is capable of supplying respirable air at a rate of humidity of between approximately 40 and 50%.

18. The installation as claimed in any one of claims 8 to 17, characterised in that it is attached to at least one ventilated suit of an operator carrying out dismantling work on nuclear installations.