Patent Grant
9327808
This invention relates to a breathing apparatus particularly, though not exclusively, for use in diving.
WO89/01895 A1 discloses a breathing apparatus for divers in which a double counterlung comprises inlet and outlet chambers joined together in a hinged bellows configuration so as to inflate and deflate together. Shut-off valves isolate the counterlung from the supply circuit when the counterlung in full, and from the return circuit when the counterlung is empty. Relief valves prevent excess pressure or suction on the diver's lungs. The arrangement accommodates fluctuations in flow as the diver breathes, and has the advantages of mechanical simplicity and reliability, among others.
The diver's double counterlung described in WO89/01895 A1 uses a hinged plate to constrain a supply and return counterlung so that they fill and empty together. During normal operation, gas is circulated from the return counterlung to the surface and back down to the diver at a constant rate by a compressor at the surface, typically on a boat. There are no flow or pressure regulators in this breathing circuit so virtually all the pressure drop in the circuit is caused by the umbilical hoses connecting the compressor to the counterlung. The double counterlung compensates for the changes in flow to and from the lungs of the diver as he breathes. The pressure in the breathing circuit at the diver is determined by the pressure acting on the double counterlung. The outlet pressure from the compressor is determined by the pressure at the diver plus the pressure drop in the umbilical supply hose. The inlet pressure to the compressor is determined by the pressure at the diver minus the pressure drop in the return umbilical hose. As the diver descends the pressure in the breathing circuit increases and the gas therein is compressed, so that gas has to be added to the breathing circuit to maintain equilibrium. Gas may also have to be added to compensate for small leaks from the circuit. Similarly as the diver ascends gas needs to be vented from the breathing circuit.
A shortage of gas in the breathing circuit results in there being insufficient gas in the double counterlung, so that it is empty before the diver has finished inhaling. When the counterlung is empty a shut-off valve shuts of the flow of gas from the return counterlung to the return hose and the rate at which the diver can breathe in is limited to the rate at which gas is being supplied to the supply hose from the compressor. Initially this imbalance causes a negligible increase in breathing resistance at the end of inhalation, but as the imbalance increases the double counterlung is empty for longer and the flow of gas from the surface may become insufficient to meet the needs of the diver.
An excess of gas in the breathing circuit results in there being too much gas in the double counterlung so that it is full before the diver has finished exhaling. When the counterlung is full a shut-off valve shuts of the flow of gas from the supply hose and the rate at which the diver can breathe out is limited to the rate at which gas is being drawn back up to the surface through the return hose. Initially this imbalance causes a negligible increase in breathing resistance at the end of exhalation, but as the imbalance increases the double counterlung is full for longer and the flow of gas back to the surface may be insufficient to meet the needs of the diver.
One way of keeping the circuit in balance is to use a pressure regulator and pressure vent valve to add gas to or vent gas from the breathing circuit when the pressure in the circuit at the surface goes outside predetermined limits. The problem with this is that the difference between the upper and lower limits would be relatively small and would need to be adjusted as the depth of the diver changes. Further change would be required should the breathing gas mix be changed. Allowance is required in case the flow coefficients of the various components in the breathing circuit deteriorate over time. Typically, providing an accurate measure of the depth of the diver and the density of the breathing gas is required. Thus the pressure regulator and vent would need constant adjustment while the diver was descending at the beginning of a dive and ascending at the end of a dive, and would need to take into account changes in the composition of the breathing gas.
Typically, two persons are required at the surface to regulate the flow of breathing gas to a diver. A first person monitors actual diving depth, and a second manages the addition and venting of diving gas according to depth and other factors.
What is required is an improved means of detection to allow gas to be added to, or vented from, the breathing circuit as the demand of the diver changes.
According to a first aspect of the invention there is provided a double counterlung breathing circuit comprising a supply duct, a return duct and a source of breathing gas, said circuit including means to detect minimum volume of the counterlung and, in response to add gas from said source to said breathing circuit. Said means may comprise a flow sensor responsive to changes in flow rate in the return duct, but preferably comprise a pressure sensor in the return duct to detect a change in pressure in the breathing circuit. Such a sensor regulator may be a pressure regulator and termed a ‘top-up’ regulator.
According to a second aspect of the invention, there is provided a double counterlung breathing circuit comprising a supply duct, a return duct, and a vent, said circuit including a means to detect maximum volume of said counterlung and, in response to vent gas from said breathing circuit. The means may comprise a flow sensor in the supply duct, similar to that for detecting minimum volume of the counterlung, but preferably comprises a pressure sensor in the supply duct to detect changes in pressure in the supply duct. Such a sensor may be a pressure regulator and termed a ‘Venting’ regulator. The venting regulator may include the vent. The top-up and venting regulators may be unitised, for example in a common housing.
The top-up and venting regulator(s) may in practice respond to a rapid change of pressure consequent upon activation of closure valves of the counterlung at maximum and minimum volume thereof. Typically gas is shut-off from the return hose as the counterlungs empty at the end of inhalation, and from the supply hose as the counterlung becomes full at the end of exhalation. The closure of such shut-off valves causes cessation of flow and a detectable pressure change, and one or more pressure detectors may be provided to detect such change and thereby signal said regulator(s).
The gas may be added to the counterlung breathing circuit over one or more breathing cycles.
The top-up and venting regulators automatically add breathing gas to the breathing circuit when there is not enough, or release gas from the breathing circuit when there is too much, regardless of the diver's depth. This avoids the need for manual intervention during normal operation.
The two regulators are preferably situated on the surface so that the “top up” regulator is close to a source, such as gas storage cylinders, and so that the gas from the “Venting” regulator can be collected for reprocessing. In this latter respect another aspect of the invention may further include means to collect vented gas for re-use in said breathing circuit.
Thus detection of when the counterlung is full or empty is proposed, rather than having to calculate an optimum pressure in the system, and add or vent gas by means of a manual intervention.
The volume of breathing gas to be added or vented is determined according to the internal volume of the breathing circuit including double counterlung, supply and return ducts, gas reprocessing unit and compressor, the rate that gas leaks from the counterlung breathing circuit, the change in depth of the diver and other associated factors.
The diver's double counterlung described in WO89/01895 A1 uses a hinged plate to constrain a supply and return counterlung so that they fill and empty together. This design exhibits significant hydrostatic imbalance when the double counterlung is in a backpack and the diver is in a horizontal position. This imbalance is caused by the difference in pressure that the water exerts on the diver's lungs and pressure that the water exerts on the double counterlung when they are at different depths in the water. When the diver is upright the counterlungs are approximately at the same depth as the diver's lungs but when the diver is prone the diver's lungs are up to 250 mm deeper than the counterlungs and this makes it harder for the diver to breathe in gas from the supply counterlung. Similarly if the diver is on his back the counterlungs are up to 250 mm deeper than the diver's lungs, making it harder for the diver to exhale gas into the return counterlung.
Relief valves fitted to prevent excessive pressure or suction on the lungs are also influenced by where they are mounted with respect to the lungs and to the orientation of the diver. The opening pressure measured at the lungs will be higher when the relief valves are deeper than the lungs and lower when the lungs are deeper than the relief valves.
What is required is a means and method of alleviating the hydrostatic imbalance when the user is substantially horizontal, so as to reduce the variations in breathing effort.
According to a third aspect of the invention there is provided a wearable breathing apparatus comprising a double counterlung having supply and return chambers connected for inflation and deflation in unison, the counterlung having a common member movable in use towards and away from a user, said common member having a substantial mass.
Attaching heavy material onto or incorporating it into the common member, typically a hinged plate, that constrains the two counterlungs reduces the hydrostatic imbalance by applying a gravitational force that acts on the common member to increase or decrease the pressure in the double counterlung according to the orientation of the member above or below the user's lungs. This reduces the effect that the orientation of the diver has on the effort required to breathe in from and out into the double counterlung.
Typically a double counterlung has a swept volume of between 4.5 and 5 liters, and in accordance with this aspect of the invention an additional mass in the range 3-10 kg is added to the common member, preferably 5-9 kg.
Preferably the common member is an upright hinged plate having a substantially horizontal hinge axis at the lower edge, and the substantial mass comprises a weight member at or close to the free edge of said plate. The weight member may be in the form of a strip or bar attachment, preferably of around 7 kg. The centre of gravity of the weight member is preferably about 200 mm perpendicularly above the hinge axis. The weight member may extend across the full width of the common member.
The relatively heavy common member keeps the pressure in the double counterlung closer to the water pressure acting on a diver's lungs, making it easier for the diver to breathe.
Preferably the double counterlung includes relief valves each having a respective movable plate-like valve element. Preferably such a valve element, typically in the form of a free disc, has a substantial mass.
Making the valve elements of double counterlung relief valves from a heavy material ensures that the relief valve opening pressure varies in the similar way that the pressure in the double counterlung is affected by the weight incorporated into the common member.
Typically such a relief valve has seat diameter of around 10 mm and a valve element having a mass in the range 14-25 gm.
The weighted valve elements on the pressure and suction relief valves means that the pressure at which they open is more closely related to the water pressure acting on the diver's lungs so avoiding any risk of damaging the diver's lungs through over or under pressurization.
The mass of the common member and/or valve elements is a straightforward calculation according to the maximum vertical distance between the effective centre of the lungs of the user (the lung centroid) and the effective centre of the hinged plate of the double counterlung.
Preferably the relief valves are mounted on the common member of the double counterlung, and have respective disc-like valve elements movable substantially perpendicularly to the plane of said common member, typically a hinged plate.
The weighted valve plates on the pressure and suction relief valves mean that the difference between the opening pressures of the relief valves and the mean pressure in the counterlungs can remain substantially constant. This enables that the opening pressures of the relief valves remain close to their optimum setting regardless of the orientation of the diver.
Preferably a double counterlung backpack is provided. In a preferred embodiment the weighted common member, and/or weighted valve elements are incorporated within a double counterlung backpack. Preferably the backpack is contoured to follow the curvature of the user's shoulders, so as to move the counterlung closer to the lungs of the diver, thereby reducing the amount of weight needed to minimize the hydrostatic imbalance. In a preferred embodiment the counterlung comprises a rigid backpack having inflatable counterlung chambers thereon, and a rigid shield over said chambers, said shield having apertures to permit the counterlung to expand and contract by displacement of water through said apertures. The shield is preferably removable for inspection of the double counterlung.
Three factors need to be addressed when designing a compressor for a diver's gas reclaim system:
Both air driven gas boosters and reciprocating compressors are currently used in breathing gas reclaim systems but in both cases considerable modifications of standard equipment is required. Reciprocating compressors are considerably quieter and more efficient than the gas boosters but required specially designed dry running seals on the connecting rods and pistons. There is considerable heat generated by the seals and the possibility of an appreciable leakage through them. Putting an electric motor and pump assembly in a pressure vessel has been tried but is very bulky and if the motor overheats the resins in the motor windings produce toxic gasses that can enter the breathing circuit.
What is required is a better compressor arrangement for the breathing circuit of a diver.
According to a fourth aspect of the invention there is provided a hybrid gas compressor for circulating breathing gas to a double counterlung, and comprising an ejector pump as first stage and a centrifugal compressor as second stage, wherein the centrifugal compressor is substantially over-sized such that excess output therefrom comprises the motive gas for said ejector pump.
Preferably the volume output of the centrifugal compressor is at least five times as great as the breathing volume requirement of a diver. In a preferred embodiment the volume output is 8-10 times greater than the breathing volume requirement.
A double counterlung for a diver considerably reduces pressure drops in the breathing circuit compared to other gas reclaim systems, and this makes an oversize centrifugal compressor a suitable option.
Advantages of the centrifugal compressor are:
Theoretically, the flows and pressures required for a diver's breathing circuit can be achieved in one stage with an 11 mm impeller but it would need to rotate at a million rpm. A two stage centrifugal compressor would half the speeds needed but these are still too high to be practical and the impellers would remain very small and so be very difficult to manufacture.
A centrifugal compressor delivering about half of the required increase in pressure and delivering around 10 times the breathing volume requirement is a practicable possibility. Said compressor would have an impeller of about 35-40 mm, run at around 200,000 rpm and can be driven through gearing by an electrical motor, i.c. engine or hydraulic motor; alternatively it could be driven directly by a gas turbine in a similar arrangement to a turbo charger of an i.c. engine.
The worst case is when the diver is at the surface because the inlet pressure is below ambient, the mass flow is low and the inlet to outlet pressure ratio is high. As the diver descends the gas density increases and the pressure ratio decreases reducing the speed at which the impeller needs to rotate to develop the required increase in pressure.
The diver's double counterlung described in WO89/01895 A1 is used in both the primary gas reclaim breathing circuit and in the secondary or backup rebreather circuit. During normal operation the gas in the double counterlung is prevented from circulating through the rebreather portion of the diver's backpack by closing off the connection between the return counterlung and the carbon dioxide scrubber of the rebreather circuit. The oxygen and diluent gas supplies of the rebreather circuit are also shut-off when the rebreather is not in use. A valve is required that is simple for the diver to operate, and that will open and close all three passage ways of the rebreather simultaneously, on demand.
Pure oxygen is a fire hazard because it increases the combustibility of other materials. This restricts the materials that can be used to contain it.
The breathing system described in WO89/01895 A1 has two backup modes in case of a failure in the gas reclaim system:
This means that no single failure will compromise the diver's safety. The diver decides which backup mode to activate, and this depends on the type of failure in the primary gas reclaim system.
In order for either backup mode to operate effectively a combination of gas passages need to be opened or closed in accordance with the following table.
According to a fifth aspect of the invention a double counterlung assembly comprises valves operable to select one of a gas reclaim breathing circuit, a rebreather circuit and an open circuit breathing circuit, wherein said valves are grouped into three sets of valves. Preferably one, more preferably two and most preferably all of said sets have a single respective actuator.
It will be understood that the open circuit breathing circuit is not a circuit as such, because gas is vented into the water; the gas reclaim and rebreather circuits are closed circuits.
The diver is thus able to activate the selected backup mode with the minimum number of operations, rather than open or close each valve separately.
In the preferred embodiment a first set of valves is operable to close passages a and c to isolate the counterlung from the supply and return hoses connecting it to the surface and maintain communication between the supply hose and a demand regulator via passage b. This first set is operated for backup by rebreather or open circuit.
In the preferred embodiment a second set of valves is operable to open passage d, e & f to activate the rebreather.
In the preferred embodiment a third set of valves is operable to close passages g and to open passage h, to isolate the diver from the backpack and connect the supply to the open circuit demand regulator. The third set of valves can be incorporated into a mouthpiece, full face mask or a sealed helmet.
In a preferred embodiment the first set of valves is provided on a chest mounting for a diver. Preferably the second set of valves are provided on the backpack. The third set of valves is at the mouth, preferably on the mouthpiece, mask or helmet.
To avoid accidental operation the actuators of said valves preferably include a latch which must be released to permit operation thereof. Said latch may comprise a squeeze release, and said actuators may be push-pull or pivotable. A lock may be provided to maintain said actuators in one or other operating condition.
According to a sixth aspect of the invention there is provided a three part spool valve for a double counterlung comprising a casing defining three independent flow passageways, and a spool pivotable in said casing to open and close said passageways in unison. Preferably the spool is of PTFE, and said casing is of an oxygen compatible material, for example brass. The spool is preferably cylindrical, and may have several diameters in a stepped arrangement.
In use said passages respectively control a diluent gas supply, an oxygen supply and a connection to a gas scrubber, and are separated by suitable seals, such as O-rings.
The pressure differential between the counterlung and the rebreather scrubber is very small but the passage way is relatively large. The oxygen and diluent are at a medium pressure and accordingly the passageways are relatively small. A large diameter of a stepped spool comprises a passage for the re-breather scrubber, whereas a relatively small diameter has passages for the diluent gas and oxygen. The spool diameters have a typical ratio of 3:1.
Such a spool valve is preferably incorporated within a double counterlung backpack and said spool comprises a pivotable shaft protruding from the backpack and having an external actuator, such as a lever, for operation thereof by a wearer of the backpack, whereby said spool may be pivoted between open and closed positions.
Rebreather systems for a diver use chemical granules known as soda-lime to react with the carbon dioxide in expired air from the diver, and remove it from the system through a chain of reactions with the various chemicals in the granules. The soda-lime is contained in a scrubber that channels the expired gas through the soda-lime granules. The efficiency of the soda-lime, i.e. the amount of CO2 that is removed by a given quantity of soda-lime, is dependent on;
A significant proportion of the work that the lungs of the diver expend circulating gas around the rebreather is due to the pressure drop in the scrubber, which is dependent on;
Some dust is generated by the movement of the soda-lime granules and the filter material that constrains the soda-lime needs to capture a significant proportion of this dust so that it does not get into the lungs of a diver. For most rebreather systems, expired gas is only moved through the scrubber during exhalation. It then remains static in the scrubber during inhalation which gives the carbon dioxide in the expired gas more time to react with the soda-lime.
In the diver's breathing system described in WO89/01895 A1 the configuration of the double counterlung causes half the expired gas to be moved through the scrubber during exhalation and half during inhalation. Whilst this does not affect the total time that the expired gas spends in the scrubber the way that it moves through the soda-lime is changed, as compared with other prior art.
According to a seventh aspect of the invention there is provided a carbon dioxide scrubber for breathing gas of a double counterlung and comprising concentric tubes containing soda-lime, an inlet being provided at one of said concentric tubes, and said tubes being porous to permit gas to pass through the tubes, but to prevent particles of soda-lime from passing the tubes. The tubes are structural and a filter material.
The scrubber is in use mounted within an enclosure so that gas passing through the outer tube enters the supply side of the rebreather breathing circuit.
Preferably the tubes are of sintered metal or plastic, and are circular. The tubes are preferably closed by one or more removable end plates, and said end plates are adapted to apply a compressive load upon soda-lime granules contained within the tubes, for example by pressure from a spring.
Oxygen needs to be added to a rebreather as it is used up by the diver. Add too much and the oxygen becomes toxic, add too little and the diver is starved of oxygen. The partial pressure of oxygen needs to remain between 0.2 bar absolute and 1.6 bar absolute. Partial pressure is a measure of the concentration of a gas and is the product of the percentage of a gas in a mixture and the absolute pressure of the mixture. As the diver descends and the pressure increases, the percentage of oxygen required to maintain a safe partial pressure decreases. The rate at which the diver uses up oxygen is dependent on how hard they are working and is closely aligned with the rate at which they are breathing (around 4% of the rate of breathing). The relationship between oxygen usage and rate of breathing not only varies from diver to diver but also during a dive as work rate changes.
Fully closed circuit rebreathers tend to use electrical oxygen sensors and electronic controls to main the partial pressure within predetermined limits. There is however always the risk that water will get into the electronics, particularly at depths at which water pressure puts considerable strain on the housing and seals.
Semi-closed circuit rebreathers tend to add oxygen rich gas mixtures mechanically. The amount added is sufficient to provide the expected oxygen usage. This means that more gas is added to the breathing circuit than is used by the diver so a small amount of gas has to be vented from rebreather whenever a counterlung becomes full. As the gas in the breathing circuit has a lower proportion of oxygen in it than the oxygen rich gas mix that is being added to the circuit, this means that there is some oxygen in the gas vented from the rebreathing circuit. If the amount of oxygen being added is more than what the diver is using and the oxygen being vented, the proportion of oxygen in the breathing circuit increases and so the amount of oxygen in the vented gas also increases until a balance is achieved. If less oxygen is being added than is being used by the diver and being vented from the breathing circuit the proportion of oxygen reduces, and so the amount of oxygen vented from the circuit also reduces until a balance is achieved. The vented gas therefore stabilizes the oxygen content to some extent by releasing more oxygen when the diver is using up less oxygen than the projected and releasing less oxygen when the diver is using more oxygen than projected. The more gas vented the more of a stabilizing effect that the vented gas has but the more gas is used over a given period.
There are various methods of adding the gas to the breathing circuit, the main ones relying upon constant mass flow or constant volume flow. Volume added is a proportion of the volume breathed and mass added is a proportion of the mass breathed. The bigger the depth range the harder it is to get the gas composition right.
According to an eighth aspect of the invention there is provided a rebreather device for a breathing circuit of a diver, and comprising two independent systems for adding oxygen thereto, the first system being adapted to add an oxygen rich gas mix as a proportion of the breathing rate of a diver, and the second system being adapted to add oxygen at a pre-determined diving depth, and to provide an increasing flow of oxygen as the diver ascends from said depth.
The hinged plate in the double counterlung of WO89/01895 A1 moves in and out as the diver breaths. Preferably this movement is used to drive a small bellows metering pump that adds oxygen rich gas to the breathing circuit at a proportion of the rate that the diver is breathing when the double counterlung is being used as part of a rebreather. A demand regulator provides gas to the metering pump at the diver's ambient pressure. Because the volume is constant the mass of oxygen added increases with depth. The demand regulator also adds gas to the breathing circuit if the double counterlung is empty.
At shallower depths additional oxygen is added at a constant absolute pressure through a flow restrictor. As the diver goes deeper the ambient pressure increases and so the pressure differential across the flow restrictor gets less and the flow of oxygen into the breathing circuit is reduced until the pressure at which the oxygen is supplied is equal to or less than the diver's ambient pressure and the flow of oxygen stops.
The bellows metering device provides a simple and reliable method of adding oxygen at the divers operating depth with a relatively high rate of gas conservation, and without the need to rely on electronic control systems.
Losses from leaks are automatically made up by providing a demand regulator in the breathing circuit.
The supplementary method of adding oxygen at the shallower depths substantially eliminates any risk of the diver becoming hypoxic during surfacing and decompression.
An open-circuit supplied compressed gas diving apparatus with a demand regulator has to have an umbilical supply hose that is big enough to supply the peak flow of about 240 l/min demanded by a diver breathing at 75 l/min. This hose could be considerably smaller if the flow through the hose could be spread out over the breathing cycle. This in turn would reduce the size of the umbilical that the diver has to take with them. If the supply hose is sized to carry about 120 l/min at a constant rate, as is the case with the breathing system described in WO89/01895 A1, there would be insufficient gas supplied during inhalation to enable an open circuit demand regulator to operate correctly.
According to a ninth aspect of the invention there is provided a double counterlung backpack for a diver and including an accumulator to supplement the flow of gas to the open circuit demand regulator of the diver during periods of peak inhalation. During exhalation the accumulator is re-charged from the supply duct. Peak flow in the supply umbilical is thereby reduced, so that the size of the umbilical can also be reduced. Such an arrangement is useful when the diver is on open circuit regulator connected to a supply umbilical, with the counterlung isolated, and the return umbilical closed.
Other features of the invention will be apparent from the following description of preferred embodiments illustrated by way of example only in the accompanying drawings in which:—
In this specification, the term upright refers to the orientation with respect to a standing user wearing a double counterlung backpack. Other references to orientation should be interpreted accordingly.
With reference to
By resolving the forces acting on the counterlung in the water it can be shown that the average pressure in the two counterlungs will be the same as the water pressure at a point about two thirds of the distance from the hinge to the opposite edge of the plate and equidistant from the other two edges as indicated by point D. This is the effective centre of the counterlung.
Either attaching a weight to the hinged plate or making the hinged plate out of a heavy material makes the gravitational force acting on the hinged plate significant. When the diver is prone the gravitational force pushes down on the hinged plate. To balance out this force the pressure in the two counterlungs increases. If the right amount of weight is added to the hinged plate the pressure in the counterlungs becomes the same as the pressure of water acting on the lungs. The leverage provided by the hinge means that the amount of weight needed for the pressure in the counterlung to match the pressure acting on the diver's lungs is reduced as the centre of gravity of the weight gets further from the hinge.
When the diver is upright the gravitational force of the weight tends to work straight through the hinge and so has little effect on the pressure in the two counterlungs. When the diver is on his back the gravitational force on the weight pulls the counterlung open reducing the pressure in the counterlungs so that it more closely matches the water pressure acting on the lungs.
The overall effect that the weight has is to move the effective centre of the double counterlung towards the middle of the lungs of the diver, thus making breathing easier when the diver is horizontal. A typical added weight is around 7 kg.
The counterlung of the invention incorporates pressure and suction relief valves 11,12 on the supply and return sides. (
The valve plates 10 (
Typically the pressure relief valve 11 (
The double counterlung of the invention is preferably incorporated into a backpack 13 (
With reference to
When the supply side counterlung 24 is full the hinged plate 28 closes against a supply valve seat 30 that stops the supply gas from the surface as indicated by arrows. This only happens when an excess of gas in the breathing circuit causes the double counterlung fill at the end of the diver's exhalation.
When the double counterlung is empty the hinged plate 28 closes against a return valve seat 29 in the return counterlung, thus stopping gas from returning to the surface and indicated by arrow R. This only happens when there is not enough gas in the breathing circuit to prevent the double counterlung from emptying at the end of the diver's inhalation.
An arrangement that detects when the flow to or from the diver has stopped can be utilized to add or vent gas from the breathing circuit. In the present invention the main indicator that the flow has stopped is the rapid change in flow and pressure that is caused in the umbilical by closure of the valves 29, 30. The hinged plate acts as a very large diaphragm with a high mechanical advantage on the valve. This means that a small change in pressure (typically 0.0025 bar) in the double counterlung can overcome a far larger pressure (typically 10 bar) in the supply or return umbilical hoses.
When either the supply from the surface or the return to the surface is shut off the pressure in the hoses changes rapidly. A regulator valve and vent valve at the surface are activated by the rate of change in pressure in the breathing circuit, and in consequence gas can be added or vented from the circuit. This arrangement is not dependent on the diver's depth and will automatically adjust as the diver descends or ascends.
A diaphragm 47 divides a chamber, and is subjected to pilot pressure on one side, and pressure in the breathing circuit at the opposite side. Movement of the diaphragm 47 in response to a reducing pressure in the breathing circuit causes a valve plate 48 to lift from a valve seat 49, and to permit gas under pressure to enter the breathing circuit via duct 50.
The dome loaded regulator thus will add gas to the breathing circuit for the period that the pilot pressure is greater than the reduced pressure in the breathing circuit. This will either be until the pilot pressure has dropped to the pressure in the breathing circuit or the breathing circuit pressure has increased because the shut-off valve in the return counterlung has opened because the diver is now exhaling. The length of time that it takes for the pilot pressure to equalize is dependent on the flow coefficient of the flow restrictor and the size of the damping volume in the pilot pressure line, and may be designed empirically to suit the intended use.
If insufficient gas is added the first time that the double counterlung empties the cycle will be repeated at the end of the next inhalation. The amount of gas added each cycle can be increased by adding the gas to the breathing circuit through a venturi 46 that draws gas from the pressure regulator and therefore keeps it open for longer. The sensitivity of the venturi can be tuned to prevent the regulator staying open permanently.
The dome loaded vent valve will thus vent gas from the breathing circuit for the period that the pilot pressure is lower than the increased pressure in the breathing circuit. This will either be until the pilot pressure has risen to the pressure in the breathing circuit or the breathing circuit pressure has reduced because the shut off valve in the supply counterlung has opened because the diver is now inhaling. The length of time that it takes for the pilot pressure to equalize is dependent on the flow coefficient of the flow restrictor and the size of the damping volume in the pilot pressure line, and can be determined empirically.
If insufficient gas is vented the first time that the double counterlung fills the cycle will be repeated at the end of the next exhalation.
The first stage jet/ejector compressor 151 uses the momentum from the motive gas 152 to draw in the suction flow 153 as the two gas streams mix. The mass of gas discharged 154 is the sum of the mass of motive gas and the mass of suction gas. The gas is discharged at a higher pressure than the suction pressure and a lower pressure than the motive gas.
In this case the term suction is relative because, whilst the suction pressure is below the ambient pressure acting on the diver, it may be considerably more than atmospheric pressure.
The second stage centrifugal compressor 155 is sized to pump both the gas returned from the diver and the motive gas that is mixed with it by the first stage. After the second stage the flow of gas is split so that a required amount of gas is pumped via supply line 156 to the diver 158 and the remainder 157 is used as the motive gas for the first stage ejector compressor creating a second recirculating loop at the surface.
Typically the breathing volume requirement of a diver is 120 liters per minute whereas the output from the centrifugal compressor is 1200 liters per minute. Thus 90% of compressor output comprises motive gas for the ejector pump, which entrains the divers exhaled volume of about 120 liters per minute.
The volume of motive gas used to power the ejector compressor is considerably more than the volume of gas being circulated to the diver. The energy put into the additional gas compressed in the second stage is used to power the first stage.
Heat exchangers 159 cool the gas after the ejector 151 and compressor 155 to keep the temperature at manageable levels. In an alternative embodiment, the heat exchanger 159 after the compressor 155 is omitted, but a heat exchanger is included in the supply line 156 to cool the gas being pumped to the diver 158. This arrangement takes advantage of the condition that the jet pump 151 is more efficient with hot gas, but the compressor 155 is more efficient with cooled gas.
Air bearings or other non lubricated bearings support the impeller shaft as it turns. A labyrinth seal or other dry seal is used to minimize the amount of breathing gas that escapes between the impeller shaft and the impeller housing.
A variety of high speed power sources can be used to drive the impeller of the centrifugal compressor including gas turbine, hydraulic turbine, is motor and electric motor. Depending on the power supply a gear box may be needed to achieve the final driving speed.
The pressure rise and the gas flow to the diver are controlled by varying the speed at which the impeller of the second stage is driven, and the volume of gas that is split off to power the ejector pump 51.
Advantages of this aspect of the invention are:
Shut-off valves a, c are connected so that they are opened and closed together by one movement. They are situated in the primary breathing circuit between the supply and return hoses 83, 84, which are typically in an umbilical of the diver, and the supply and return counterlungs 85, 86 in a backpack 87. The loop in the gas reclaim circuit is completed by the pair of hoses and mouthpiece 88 that connects the diver to the counterlungs.
The connection between supply hose 83 and the hose b to the open circuit demand regulator 89 is situated upstream of the supply shut-off valve a so that the connection between the surface and the demand regulator is maintained in all positions of valve a.
Shut off valves d, e and f are also connected for operation in unison so that the passage between the return counterlung and the carbon dioxide scrubber 81 in the diver's backpack, the oxygen supply 82, and the diluent gas supply 90 are all opened and closed together. The backup rebreather circuit is activated when these valves are opened but in order ensure that it will operate effectively valves a and c also need to be closed.
The shut off valves g and h are connected for operation in unison so that when the valves g are open the valve h is closed and vice-versa. The backup open circuit regulator is activated when the valves g are closed and valve h is open but in order to ensure that it will operate effectively valves a and c also need to be closed.
The gas reclaim shut-off valves a and c are preferably mounted on the chest of the diver for easy access. They could however be mounted in the backpack, provided that easy access to the mechanism is maintained. Depending on the valve arrangement, the valves are preferably shut either by pushing a plunger or turning a handle clockwise. To prevent accidental operation a squeeze release latch stops either the plunger or handle from moving until it is squeezed. The valves can be opened by either pulling the plunger or turning the handle anticlockwise, depending on the type of actuator fitted. Other kinds of actuator are possible.
Both gas reclaim valves a, c must be closed in order to ensure that the back-up systems can operate effectively in all scenarios. The arrangement means that simple actions by the diver will shut down the primary gas reclaim system and allow the rebreather and the open circuit demand backup systems to operate effectively, depending on the back-up system selected by the driver.
The action is reversible so diver can test the backup systems.
The spool 62 has three passage ways through it. These are arranged so that when the valve is open all three passageways align with the ports in the body and when the valve is closed the ports are blocked. The largest passage 66 connects the return counterlung to the carbon dioxide scrubber. A second passage 65 is for the diluent gas and the third passage 64 is for the oxygen. The spool is held in the body by an end plate 68. The spool is turned by a shaft 69 that runs through a bulkhead connector and fits into a square socket 70 in the spool. A lever 67 attaches to the shaft where it penetrates through the backpack casing. A pull push rod 71 constrained by a guide 72 is used to pivot the lever. The bulkhead connector in the backpack casing restricts the lever so that it can only turn through 90°. ‘O’ ring seals stop leaks through the bulkhead connector. Wiper rings stop dirt getting between the shaft and the bulkhead connector and damaging the bearing faces and the moving seals.
The simple operation of pulling the lever will open the valve, and pushing the lever will close the valve. The lever is preferably biased to one or other end portion to ensure that the rebreather circuit is fully closed or fully open.
The operation of the backup rebreather can be checked at any time before or during a dive and then turned off again.
PTFE is both oxygen compatible and a dry lubricant.
Oxygen is added to the rebreather upstream of the carbon dioxide scrubber so that it will be well mixed with the breathing gas by the time it reaches the diver.
The radial flow and length of the scrubber provide a large cross sectional area and a short distance for the gas to flow through, significantly reducing the breathing resistance whilst ensuring an even flow of expired gas through the scrubber. The design also retains the heat from the chemical reaction further improving the efficiency of the soda-lime. A removable end plate 94 allows the used pellets to be replaced. It is spring loaded and designed to keep the pellets lightly compressed so that they do not form voids or rub against each other producing dust. The illustrated design has the expired air flowing in through the smaller cylinder and then out through the larger cylinder but the flow could be reversed in an alternative design. The volume of soda-lime held in the illustrated counterlung is about 1.5 liters, which is sufficient when used with the double counterlung described WO89/01895 A1 as the maximum volume of a pulse of expired gas through the system is 1.5 liters or half the 3 liters tidal volume when a diver is working at a rate of 75 liters per minute. For conventional rebreathers the volume of soda-lime in the scrubber would need to be increased to over 2 liters which is the tidal volume that is used when testing the endurance of a carbon dioxide scrubber.
With reference to
This mechanism therefore supplies gas at a volume flow that is 3% of the rate at which the diver is breathing so that the harder the diver breathes the more gas is added. Once the diver has reached the planned depth the mass flow of added oxygen exceeds what the diver will be using up with the excess being vented from the circuit.
Should the counterlungs be empty the counterlung diaphragm presses and opens on the diaphragm of the demand regulator so that breathing gas can be added to inflate the supply counterlung. When in rebreather mode this adds more gas to the circuit, and ensures that there is sufficient gas in the rebreather circuit when the rebreather is first activated (i.e. the umbilical connection is turned off). The arrangement also allows top up the rebreather circuit if more gas is lost from the system than is being added by the metering pump.
At shallower depths, i.e. during descent and decompression, the oxygen added in this way may be insufficient to match the respiration demand of the diver, so additional oxygen needs to be added to the circuit. With reference to
A control valve comprises a body 110 having a diaphragm 111 closing a sealed chamber 112, and biased by a coiled compression spring 113 within the chamber 112. The body further defines a valve seat 114 and a poppet valve 115 movable off the seat 114 by movement of the diaphragm 111. An inlet connection 116 to the oxygen storage cylinder is upstream of the valve 115, and a connection 117 to the breathing gas circuit is on the downstream side of the valve 115. A restrictor 118 is provided in the connection 117.
The chamber 112 provides a constant reference pressure so that as the diver rises, and pressure in the breathing circuit reduces, a point is reached at which the force from the spring 113 overcomes the pressure in the breathing circuit and moves diaphragm 111 away from the chamber 112 to admit oxygen past the valve seat 114 into the connection 117. The restrictor 118 ensures that oxygen flow is controlled. The reference pressure in the chamber 112 is kept as low as is practical, preferably a vacuum, to minimise the amount that the pressure changes with changes in temperature.
As the diver's depth decreases the difference between the regulated pressure and the reference pressure increases causing the flow of oxygen to increase correspondingly. The maximum flow of oxygen added in this way occurs when the diver is at the surface. As the depth increases the flow reduces until the flow stops when the diver's ambient pressure equals or exceeds the reference pressure. This depth is set to match the depth at which the metering pump of
The volume of gas in the breathing circuit slows down any changes in the percentage of oxygen so that short term changes in the rate at which oxygen is added or used up will have little impact on the concentration of oxygen breathed. For example a diver breathing at 40 liters per minute from a 10 liter volume would take 5 minutes to drop the oxygen partial pressure from 1.0 bar to 0.2 bar if not oxygen was being added.
An accumulator as shown in
The accumulator comprises a body 120 having two chambers 121, 122 separated by a piston 123 that is sealed by a rolling diaphragm 124. One chamber is connected to the gas supply via port 125 and the other is open to the ambient pressure. The piston 123 is held in alignment by a guide rod 126. A spring 127 loads the piston so that the gas in the chamber 121 is maintained at a high enough pressure for the diver's demand regulator to operate.
When a demand regulator is used as a backup to the double counterlung described in WO89/01895 A1 an umbilical shut-off valve a, c as shown in
The accumulator 120 is preferably incorporated into or mounted upon the backpack of the diver.
| Number | Date | Country | Kind |
|---|---|---|---|
| 0903320.0 | Feb 2009 | GB | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/GB2010/000345 | 2/26/2010 | WO | 00 | 8/16/2011 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2010/097594 | 9/2/2010 | WO | A |
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| Number | Date | Country |
|---|---|---|
| 2 622 459 | May 1989 | FR |
| 63-59797 | Apr 1988 | JP |
| WO 8901895 | Mar 1989 | WO |
| Entry |
|---|
| International Search Report for Application No. PCT/GB2010/000345 dated Apr. 27, 2011. |
| Written Opinion for Application No. PCT/GB2010/000345 (undated). |
| Number | Date | Country | |
|---|---|---|---|
| 20110297153 A1 | Dec 2011 | US |
