Halcyon Manufacturing set out in the mid 1990s to develop and refine a rebreather system appropriate for the demands of exploring the depths and distances of the underwater cave systems of Wakulla Springs and the Woodville Karst Plain. Halcyon's goal was to produce a rebreather that was more efficient than conventional semi closed units, but with safety and task loading levels more in line with open circuit SCUBA. Although a maximum gas efficiency was a primary design criteria, Halcyon rejected the idea of developing a closed circuit rebreather (CCR) due to unacceptable task loading, potential for diver error, and lack of intuitive alarm systems. Diver safety would not be sacrificed for the last small fraction of gas savings. Halcyon’s design resulted in a semi-closed circuit rebreather that approaches the efficiency of a closed-circuit unit but offers none of the CCR’s complications. It is capable 2 hours of operation at 300 feet on a single 80cf aluminum cylinder. Between 60 and 200 feet, the Halcyon is 5 to 8 times as efficient as open circuit.
We’ve all looked at one time or another at the equations that govern the movement of gases through active addition SCRs. They should now be well understood. There seems however, to be much confusion with respect to passive addition SCRs. There are two main types of passive addition SCRs around, and they all share some common aspects.
Automatic units dump some part of the loop volume with each breath. Generally some specific fraction of the diver’s tidal volume. Automatic units can be further divided into three general categories.
These dump a set percentage of the divers tidal volume overboard (usually from 10-25%) with every breath. Oxygen fraction varies with depth, becoming closer to the drive gas as the diver descends and the effective dump becomes greater.
Depth compensating.
These dump a percentage of the diver’s tidal volume, which varies in inverse proportion to the absolute pressure. On the surface these units generally dump between 20 and 33% of each breath, but that decreases with depth, to keep the Oxygen fraction constant and reduce gas wastage. The fraction dumped falls so that for instance a unit that dumps 33% of each breath at the surface, dumps 3.3% of each breath at 90m (10 Bar absolute). These units will provide a fixed FO2 regardless of depth, when used with the same drive gas because the effective dump remains constant.
Partially depth compensating.
These units are half way between the fixed ratio units, and the depth compensating units. They provide a high dump ratio near the surface, again 20-33% but the dump ratio is not fixed either with relation to a surface equivalent breath, or an actual breath at depth. They usually dump between 75% and 200% of a surface equivalent breath at 10 bar absolute, but of course this varies with design, and sometimes varies from individual unit to unit within one design.
Exactly how this dumpage is achieved varies from unit to unit, but some underlying principals can be discerned.
The factors which determine the composition of the inspired gas are, the Oxygen fraction of the drive gas, the oxygen consumption of the diver and the quantity of gas that is dumped from the loop. Generally it is taken that the composition of the inspired gas is equal to the composition of the dumped gas. This is not always so, as some designs inject the makeup gas (make up gas is the drive gas, injected into the loop to “make up” for the gas that has been dumped or metabolised) just upstream from the diver. Hence the dumped gas, is equal not to the diver’s inspired gas, but rather is equal to the gas that the diver exhales. However, it is bad practice to choose one’s gas limits based on the minimum level of oxygen found in the exhaled gas, as there is no guarantee that fresh gas will be injected on every breathing cycle.
The dumped gas’s composition is critical when it reaches the point where the O2 level is at it’s lowest. This point can be determined by calculation.
The dump gas can be divided into two major components, the inert gas that is “left over” from the metabolism of oxygen by the diver, and an amount of drive gas that has passed through the system, unconsumed. This second component can be thought of as an unavoidable wastage. It’s the part of the dump gas that contains the oxygen that keeps the loop above the minimum O2 level.

At this point, the only difference between the two types of rebreathers emerges. A manual system is calculated based on a time interval between dumps. This is based on the volume of Oxygen metabolised per unit time (VO2), or in other words, a rate of Oxygen metabolism. An automatic system is calculated with respect to individual breathing cycles, and depends on the ratio of tidal volume to the oxygen metabolised. Hence the convenient units are Litres and Tidal Volume Fraction, respectively.
So a couple of examples,
First for a manual system.
The drive gas is 50% O2, and the minimum dump gas O2 percentage is 20%. This allows the diver to surface at any time, and still have a breathable mixture. The O2 consumption is considered to be 3 litres per minute, which is normally a maximal VO2.
Now, the dump gas can be divided into two parts, for ease of analysis. One is the wasted gas. That’s the O2 and it’s associated inert gas that must never be removed from the loop gas. 20% of the dump gas must be Oxygen, and given that the drive gas is 50/50 mix, the inert gas associated with that will be the same volume, at 20%. Hence, adding those together, the wasted gas must represent 40% of the dump gas. The other 60% of the dump gas must then be the remaining inert gas that is left over after metabolism of the oxygen. If the diver is metabolising 3 litres/minute, then given that the drive gas is a 50/50 mix, the inert gas volume associated with 3 litres of Oxygen is also 3 litres. (Can you see why I picked 50 mix as the drive gas?). Now we can see that 3 litres is 60% of the total volume that must be dumped per minute.
I happen to have a tidal volume of 3 litres, so when diving 50% mix, I must dump twice per minute at the surface, and at 5/3rds of a bar (7m) I can dump once per minute. At 10/3rds of a bar (24m) I can dump once every other minute. This particular depth is rather awkwardly deeper than I’m really supposed to go on 50 mix, and in real life I usually use 60 mix and switch to a different drive gas below 18 metres. I also combine these procedures with the normal SCR safe practices such as a flush-through prior to commencing ascent and use of non narcotic mixtures.
In an automatic system the calculations are based on the fraction of each tidal cycle that is metabolised by the diver. There is a manufacturer at the moment who promotes a 26 to 1 ratio between tidal volume and volume metabolised. This equates to an Oxygen consumption of 3.85% of a tidal volume and is a normal human consumption rate. Divers however are notorious for maintaining exceptionally low ventilation rates, even with high workloads. You may be well advised to measure your own exhaled gas and compare the expired O2 level with inspired O2 level. I’ve done this experiment on myself, and found a worst case figure of a 10% difference. This was at the very end of an exhalation, and I would use 8% as my own worst case. My own open circuit gas consumption figures are not good however, and if you’re a gas miser, you may wish to use a more conservative figure.
Calculations proceed in a similar manner to the manual system, except that we’re not trying to find a litres per minute figure, but rather a fraction of tidal volume.
Using a 50/50 mix again, we can say that we will consume 0.08 of a tidal volume of oxygen, and the volume of inert gas associated with this will be the same (because of the fact that the drive gas has the same amount of oxygen and inert gas). Hence each dump must contain 0.08 of a tidal volume of inert gas. Again, we’ll look at a minimum FO2 of 20%, so the dump gas must contain 20% Oxygen, and it’s associated inert gas, another 20%. So 40% of the dump gas is wasted flushing gas. If 40% is flushing gas, then the other 60% gas must be the inert gas remaining after metabolism. You can arrange the figures in a similar way to the preceding calculation; 100/60 = ?/0.08 or multiplying both sides by 0.08 gives; 8/60 This is the fraction of each tidal volume that must be dumped overboard with each breathing cycle. To find the ratio of tidal to dumping, which is how these things are usually expressed, take the reciprocal, which is 60/8, or 7.5 to 1.
So for a 50/50 mixture, used from the surface, with a minimum FO2 of 20%, the minimum dump ratio is 7.5 to 1.
Now a fixed ratio rebreather will have the FO2 climb as the diver descends because the absolute amount of Oxygen metabolised remains constant while the quantity of gas that moves through the divers lungs and rebreather increases in proportion to absolute pressure. It is easy to calculate gas consumption ahead of time, simply calculate as for an OC dive, and divide by the dump ratio. Careful observers will note that this doesn’t include the metabolised O2. A very rough correction for the diver’s RMV can be made by adding the metabolised O2 to the dump volume, and recalculating the effective usage ratio. In the example above, the O2 consumption was 0.08. 0.08 plus 8/60 is 0.2133 and the reciprocal is 4.6875 at the surface. When the diver goes deeper, the oxygen consumption doesn’t change with depth, so the advantage over OC increases. As the depth increases the advantage tends toward the dump ratio, but never quite reaches it. So for an automatic dumper, using 50/50 drive gas, the advantage over open circuit is between about four and seven times better.
A depth compensating rebreather will use the same gas at depth as it does on the surface, and the FO2 will remain constant. To calculate gas consumption, do the same thing, but there’s no need to consider depth when calculating duration. The set will give an advantage over OC that is constant, and as though the diver remained at the surface. In this example the set would use the divers RMV divided by 4.6875 per minute. Of course none of this takes into account loop flushing and suit inflation, not insignificant factors with very small cylinders.
A partially depth compensating rebreather will fall part way between these two. Calculating gas consumption ahead of time is virtually impossible unless you know the exact dump ratio throughout the unit’s operating range. Unfortunately construction of a truly depth compensating rebreather has proven a formidable challenge, and from the figures that get bandied about, the units which claim full depth compensation are in fact at best, partially compensated. The key to picking this out is claims that the unit will come closer to the drive gas FO2 as depth increases. This is of course counter productive for a single gas system, however, it has safety advantages, allowing a lower FO2 drive gas to be used at great depth.
In all, it can be seen that gas dumping rebreathers can offer many advantages over OC, SCR and CC units, however, they, like all units, have drawbacks as well. Like everything else, these units are not majic carpet rides and a good grasp of what is happening inside your unit is essential, both during the design phase and during the actual operation of the unit.
Recently the issue of sensor testing and sensor storage came up on the list, and most of it is wrong or misleading. Some hints to get things right:
Modification of rebreathers is one of those things that seems to be easy, and yet is almost insanely difficult. Rebreathers, perhaps more so than any other device made by man, operate as a synergistic whole. I know that sounds rather new-age, but it’s true. Every component has to work together to produce a dynamic state that ranges around a set of values that have been imposed by human metabolic needs.
Designing a rebreather, as anyone who has done so can tell you, is sort of like a juggling act. You need to keep dozens of influences in mind to keep all the balls flowing along. It’s not like most machines, where each component can be worked out in isolation, and then the parts combined to make the finished product.
Everyone who comes in contact with a rebreather becomes an instant expert. They all want to be rebreather designers, and they’re all convinced that a few modifications to whatever it is in front of them will be a vast improvement. Ask yourself when you are in the same position, whether or not you can improve on the original designer's decisions with the few seconds of thought that you’ve put into it. Perhaps you can. Technology marches on, and all designers know that any design can be improved. The designers all know that with just a few more weeks, they can make it better, but eventually the point comes where they have to stop designing and start building. You may be tempted to step in and correct the designer’s errors.
Tread cautiously. Even the simplest modifications, to what appear to be external systems, quite apart from the core of the rebreather can have devastating results. I’ve seen a modification where the harness of the set was replaced by a jacket style BC. A simple update, that would modernise the set. No more innocuous seeming modification could possibly have been made. The entire loop was left untouched. However, the attachment for the BC was in a different location to the attachment for the harness. It interfered very slightly with the operation of the over pressure relief valve. In normal operation this had absolutely no effect and it wasn’t picked up in tests, or during extensive use. However during an emergency buoyant ascent, with a viscous nitrox mixture, the reduction in flow through the valve caused a pressure buildup inside the loop that made the scrubber lid blow off. The original designer would have been aware of the maximum performance needed from that valve, and designed it to meet those requirements. The tiny interference was enough to mean the set would no longer perform as intended at the outer edge of the envelope.
Returning to the juggling analogy, modifying a rebreather is like taking over from another juggler in mid juggle. You need to have an intimate awareness of the location, and direction of every ball before you take over, or the whole plot can come crashing down. Unless you have an awareness of the thoughts of the original designer that are at least equal to his own, combined with a good deal of hindsight gathered since the release of the set, you’re just courting disaster.
Two, 9 cf, 2100 psi steel gas cylinders were used for O2 and inert gas. These were lightweight models FAA certified for use in aircraft. Initially we used chrome plating to protect them, later we went to teflon coating. Beckman liked the more military look and there was some concern over possible hydrogen embrittlement from the chroming process.
Standard, old style, "K" valves were used as cylinder valves. On the inert side a SCUBA regulator-type yoke was used to mount a high pressure 1/8" NPT needle valve operated by rotary action of a T-shaped handle. Inert gas was valved in manually directly from the tank as needed using this valve. In use it had a very smooth precise feel. Inert gas was valved into the plenum at the bottom of the absorbent canister so that some mixing would take place before it got to the sensors.
On the O2 side a piston type first stage of a U.S. Divers single hose regulator was used to reduce tank pressure to about 60 psi. This is somewhat lower than such first stages normally deliver and was achieved by using a weaker piston spring. The normal hose to the second stage was used to connect the O2 supply to the solenoid valve. The octopus port of the first stage was used to attach an O2 bypass valve. This was a spring action, lever activated low pressure valve and it was protected by an enclosure which required opening a spring closed cover to get at the valve. The manual bypass valved O2 directly into the sensor compartment so the result was immediately readable.
I will digress briefly on O2. In addition to the physiological risks recently discussed in some detail on the list there is also the danger of fire and explosion. Valves, regulators, fittings and any other equipment used for O2 have to be thoroughly degreased of any petroleum based lubricants. If lubrication is required, as for example with the o-ring seal of a regulator piston, non-combustible silicone based lubricants must be used. Be aware that even a fingerprint oily with suntan lotion can start an explosive fire with O2. Once an O2 fire starts all sorts of things you might not ordinarily think of as combustible burn ferociously. I have heard stories of chamber fires in which everything inside, including the occupants, was reduced to ash.
My partner Kanwisher was on one of the advisory panels to NASA in connection with the Apollo program. Although he recommended using a mixed gas atmosphere in the Apollo capsule he was over-ridden by the engineers who felt that monitoring the PPO2 was too difficult. John knew better as he had been doing it for several years in conjunction with his work on respiration but the engineers prevailed. The result was the fire which killed three astronauts.
The solenoid valve we used was a miniature 12 volt one made for pneumatic control. We equipped it with a miniature screw adjusted needle valve outlet. When the setpoint is reached and the solenoid is triggered it takes perhaps three or four seconds for the sensors to respond and rise enough to cut it off again. The solenoid needle valve was adjusted so that the O2 injected raised the PPO2 to a peak pulse of about 0.75 Atm and would usually trigger a couple of beeps from the audible alarm. Within a couple of breaths mixing brought the level back to perhaps 0.65 after which it dropped more slowly as it was consumed by metabolism until the setpoint was reached again after about a minute or so. That would be for moderate activity such as easy swimming. At complete rest it would of course take longer to drop back to the set point and less time if you were actively swimming.
If the needle valve was adjusted to a lower flow rate solenoid activation would be more frequent and of longer duration placing an unnecessary drain on the solenoid batteries. If much higher flow was adjusted for the O2 spikes would be too high and the alarm would be sounding much of the time. I think there are now smaller, more power efficient solenoid valves available.
The solenoid and manual bypass valves were of the downstream type so that if high pressure leakage from the regulator occured it would release when it reached the level where it overcame the spring tension which normally closed the valve. This is important to prevent either valve lockup or blowing out the supply hose in the event of a high pressure leak. In the event of O2 leakage from either valve the cylinder valve could be used to cut it off.
The gas cylinders were mounted on either side of the central larger cylinder containing the absorbent canister and electronics section. This assembly was worn as a back pack with the valves at the bottom at hip level. Inert gas had to be added several times on descent and at other times if you lost any from nasal exhalation. Manual O2 was normally only used in decompression. The inert gas valve was therefore on the divers left side leaving the right hand free for more complex tasks. Swapping sides for southpaws would have been easy but I don't recall anyone ever raising the question. It was no big thing either way.
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by Scott Leimroth ©
