Background of the Invention
Air can be fractionalized by removing various components thereof through the affinity of these components with various molecular sieve materials. Apparatus for fractionalization can be found in U.S. Pat. Nos. 2,944,627, 3,280,536 and 3,142,547. In these cases, air under pressure is communicated to containers holding the molecular sieve material. It has been found that a molecular sieve material having an Angstrom pore size of 5 will continually produce an oxygen enriched effluent by the so-called pressure swing technique. In the above referred to patents, in achieving the proper flow of the air and oxygen enriched effluent for the pressure swing technique, a plurality of control valves are located in the supply conduit and the output conduit. The operation of the control valves are usually controlled by a timer to develop the maximum efficiency for the desired oxygen concentration in the enriched effluent. Because of the presence of inert gases in air the maximum concentration achievable will be 96%.
Summary of the Invention
We have devised a control valve for use in a breathing system utilizing the pressure swing technique of concentrating oxygen to sequentially present air under pressure to a plurality of beds of molecular sieve material and distribute a purge fluid to the atmosphere to achieve an efficient operation.
The control valve has a housing with a plurality of distribution ports for sequentially communicating air under pressure to a corresponding plurality of beds each containing a molecular sieve material to develop the oxygen enriched effluent. The output conduits of beds of molecular sieve material are interconnected to each other to permit a portion of the oxygen enriched effluent to flow through another bed and remove nitrogen retained thereon. A first disc means having sequential openings is located in the housing adjacent the distribution ports. A second disc means has an inlet port for supplying the air under pressure to a single distribution port at one time and an exhaust passage for transmitting the purge product from another distribution port to the atmosphere. Third and fourth discs located in the housing have openings therein to establish an equalization flow path between the plurality of chambers prior to the transmission of air under pressure through the inlet port. A rotary means is connected to the second disc and the third disc to provide an angular rotation to sequentially allow air under pressure to be communicated to the plurality of beds containing the molecular sieve material.
It is therefore the object of this invention to provide a breathing system with a control valve responsive to a rotary means for selectively supplying one bed of a plurality of beds, each of which contain a molecular sieve material, with air under pressure while simultaneously permitting a purge fluid to be communicated from another bed to the atmosphere to provide a continuous output of an oxygen enriched product effluent.
It is another object of this invention to provide a control valve with a rotary means which selectively permits air to flow to a first bed of molecular sieve material while simultaneously allowing a purge fluid to flow from a second bed of molecular sieve material in a first mode of operation, which allows the pressure of air in the first bed and the second bed to be equalized in a second mode of operation, which permits air to flow to the second bed and the purge fluid to flow from the first bed in a third mode of operation, and which allows the pressure of the air in the second bed and the first bed to be equalized in a fourth mode of operation during a single cycle of operation.
It is still a further object of this invention to provide a control valve responsive to rotation to control the supply of air and the release of a purge effluent in a pressure swing oxygen generator.
These and other objects will be apparent to those who read this specification and view the drawing.
Brief Description of the Drawing
FIG. 1 is a schematic illustration of a breathing system having a rotary control means for regulating the flow of air under pressure to a plurality of beds of molecular sieve material to continually produce a supply of oxygen enriched breathable fluid.
FIG. 2 is a sectional view of the rotary valve of FIG. 1.
FIG. 3 is a sectional view taken along line 3--3 of FIG. 2 showing a control disc which provides for pressure equalization between the first bed and the second bed of molecular material in the system of FIG. 1.
FIG. 4 is a sectional view taken along line 4--4 of FIG. 2 showing timing disc which is mated to the control disc in FIG. 3 to allow the pressure equalization to take place during a set sequence in the pressure swing operation.
FIG. 5 is a sectional view taken along line 5--5 of FIG. 2 showing a disc for segregating the flow of air to one of the beds of molecular sieve material while allowing the flow of the purge fluid from the other bed in FIG. 1 during a cycle of the rotary valve in FIG. 2.
FIG. 6 is a sectional view taken along lines 6--6 of FIG. 2 showing a distribution disc for transmitting air under pressure to first bed and second bed and the purge fluid to the atmosphere.
FIG. 7 is a graph showing the flow distribution of the air under pressure during a cycle of rotation of the motor.
Detailed Description of the Preferred Embodiment
The breathing system 10 shown in FIG. 1 has a control valve 12 which sequentially presents air under pressure from source 14 to a first chamber 16 and a second chamber 18 from which a product effluent rich in oxygen which is produced and transmitted through conduit 20 into a storage chamber or plenum 24 before being presented to a recipient through conduit 26. The control valve 12 is connected by shaft 28 to an electric motor 30. The electric motor 30 is connected to an electric power source 32 through a switch 34. The electric motor 30 will provide a rotary torque which will rotate the control valve 12 through which air under pressure is sequentially presented to either the first chamber 16 or the second chamber 18 and while a portion of the product effluent supplied to the storage chamber 24 is communicated through valve or orifice 36 to purge either the second chamber 18 or the first chamber 16 of residue adsorbed by the molecular sieve material in producing the product effluent. The control means will cycle from the first chamber 16 to the second chamber 18 in a direct relationship with the speed at which the electric motor 30 turns the shaft 28. During the shift of operation from the first chamber 16 to the second chamber 18, the control means will provide for equalization of the air pressure between the beds of molecular sieve material retained in each chamber. The molecular sieve material in each chamber in this breathing system will have a nominal pore size of 5 Angstroms which is sufficient for the adsorption of nitrogen from the air to produce the oxygen enriched product effluent used by a recipient.
The control valve 12 which controls the operation of the enrichment of the oxygen in the breathable air supply is shown in more particular detail in FIG. 2.
The control valve 12 has a housing 38 with bore 40 therethrough. A first end plate 42 is retained in the bore 40 by a snap ring 44. A first disc 46 fixed in the bore 40 adjacent the first end plate 42 has a seal 48 which prevents communication between the atmosphere and the bore 40. The first disc or restrictive disc 46 has a first equalization opening 50 and a second equalization opening 52 therein to restrict the size of the equalization ports 54 and 56. A second disc or bypass 58 has a first radial groove 60 and a second radial groove 62 which extend from a circular groove 64, see FIG. 4. A slot 66 located along the axial opening 68 engages a key 70 on shaft 78 to locate the second disc 58 with respect to a third disc 72. The third disc or distribution disc 72 has a rectangular opening 74 into which head 76 on shaft 28 is located to provide proper alignment with the second disc 58. An entrance port 78 in the housing 38 directs air under pressure from source 14 into a pressure chamber 80 which is formed between the second disc 58 and the third disc 72. The third disc has an inlet port 82, see FIG. 5, which extends into a first pressurizing opening 84 which is separated from an exhaust opening 86 by a divider wall 88. The exhaust opening or groove 86 extends into an axial opening 90. A fourth disc or control 92 adjacent the third disc 72 has a first distribution opening 94 and a second distribution opening 96 which restricts the flow of air from the pressurization opening 84 into a first distribution port 98 and a second distribution port 100 after a first rotation. The first distribution port 98 is connected to the first chamber 16 which contains the first bed of molcular sieve material by conduit 106. The second distribution port 100 is connected to the second chamber 18 which contains the second bed of molecular sieve material by conduit 104. The fourth disc or restriction 92 has an axial opening 102 which extends from axial opening 90 to an exhaust port 108. A check valve 110 is located in the exhaust port 108 for controlling communication between the atmosphere and the exhaust port 108. A seal 112 is located between the fourth disc 92 and a second end plate 114 to prevent communication between bore 40 and the atmosphere. A snap ring 116 is located in the housing 38 to hold the end plate in place. A spring or resilient means 118 located in the pressure chamber 80 in conjunction with the pressurized fluid urges the second disc 58 into seating engagement with the first disc 46 and the third disc 72 into a seating engagement with the fourth disc 92. The tee-shaped head 120 on the shaft 28 can be equipped with an aligning pin 122 for further engagement with the second disc 58 or mated with raised portions on the second and third discs. The shaft 28 is connected to the electric motor 30 by coupling 124.
Mode of Operation of the Preferred Embodiment
Upon experiencing a need for oxygen enriched breathing fluid an operator in an aircraft will activate switch 34 to provide motor 30 with the electrical energy needed to rotate shaft 28 at a speed which will operate the breathing system to produce the oxygen concentration desired.
Air under presssure will flow through the particle filter 126 through a pressure reducer 128 into conduit 130 for presentation to the entrance port 78.
In a first angular rotation or mode of operation, for a 1st time interval, see FIG. 7, air under pressure present in the pressure chamber 80 will flow through the inlet port 82 into the pressurizing opening 84 and out the distribution port 98 through conduit 106 to the first chamber 16 where the molecular sieve material will retain the nitrogen and produce an oxygen enriched effluent which will flow in conduit 20 past check valve 132 into the supply chamber or plenum 24 for distribution through conduit 26 to the recipient. As the oxygen enriched effluent is flowing in conduit 20, a portion thereof will flow through the interconnecting conduit 134 past the purge or restrictive orifice 36 into conduit 22 for presentation to outlet 136 in the second chamber 18. The oxygen enriched effluent will flow through the second bed of molecular sieve material and desorb nitrogen therefrom before entering conduit 104 connected to the second distribution port 100. The purge effluent will flow past flow distribution opening 94 into the exhaust opening 86 through the axial openings 90 and 102 into the exhaust port 108 for distribution to the atmosphere after overcoming the resiliently held poppet 138 of the check valve 110.
When the motor 30 has rotated the third or distribution disc 72 through an angle equal to the pressurizing opening 84, divider wall 88 will seal the distribution ports 98 and 100. At the same time, the first and second radial slots 60 and 62, respectively, of disc 58 will be moved to open the equalization ports 50 and 52 of disc 46 to establish a second mode of operation for a 2nd time interval, see FIG. 7, through the angular rotation of shaft 28. With the equalization ports 50 and 52 in communication the pressure of the air and product effluent in the first bed will be equal to that in the second bed.
Further rotation of the second disc 58 and third disc 72 will again seal the equalization ports 50 and 52 and bring the pressurizing opening 84 into communication with the second distribution port 100 to allow air under pressure to flow through the inlet port 82 to the second chamber 18 where the molecular sieve material will adsorb nitrogen to produce an oxygen enriched product effluent. The oxygen enriched product effluent will flow through conduit 22 past check valve 138 into the storage chamber 24. A portion of the oxygen enriched product effluent will flow past the purge or restrictive orifice 36 into the outlet 140 of the first chamber 16. The purge effluent will desorb nitrogen in the first bed of molecular sieve material before passing through conduit 106 to distribution port 98. The purge effluent will flow past port segment 96 into the exhaust opening 86 through the axial bores 90 and 102 before exiting to the atmosphere through check valve 110 during a third mode of operation in a 3rd time interval, as illustrated in FIG. 7.
Further rotation of shaft 28 will move the divider wall 88 on the third disc 72 to seal the distribution ports 98 and 100 and to open the equalization ports 54 and 56 by the radial grooves 60 and 62 in the second disc 58 to establish equal pressure in the first and second chamber during a fourth mode of operation or angular rotation in a 4th time interval, see FIG. 7, to complete a single cycle of rotation by shaft 28.
Thus the entire presentation of the air under pressure is controlled by a single valve 12 to provide simplicity in the operation of this on-board oxygen generator for use in an aircraft.