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dwell-time calculation: axial vs radial



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Old 1st September 2006, 10:10   #1 (permalink)
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dwell-time calculation: axial vs radial

hello, here you find an excel calculation of the dwell-time in a radial and an axial scrubber of exactly the same shape: only for the axial the gas flows in the length, in the radial gas goes from in to out

regards
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Old 1st September 2006, 10:12   #2 (permalink)
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Re: dwell-time calculation: axial vs radial

Quote: (Originally Posted by paulraymaekers) View Original Post
hello, here you find an excel calculation of the dwell-time in a radial and an axial scrubber of exactly the same shape: only for the axial the gas flows in the length, in the radial gas goes from in to out

regards
paul
sorry, seems excel is not supported...
any suggestions?
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Old 1st September 2006, 10:20   #3 (permalink)
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Re: dwell-time calculation: axial vs radial

Quote: (Originally Posted by paulraymaekers) View Original Post
sorry, seems excel is not supported...
any suggestions?
zip the file..
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Old 1st September 2006, 12:21   #4 (permalink)
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Re: dwell-time calculation: axial vs radial

Quote: (Originally Posted by jradomski) View Original Post
zip the file..
thanks joe! :-)

here it is

regards
paul
Attached Files
File Type: zip dwell.zip (6.7 KB, 110 views)
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Old 5th January 2007, 01:46   #5 (permalink)
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Re: dwell-time calculation: axial vs radial

So for the *same dimension* scrubber, the dwell time is the same.. implying that there is..... no difference in efficiency between the two... at least in this proportion.... correct?
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Old 5th January 2007, 02:47   #6 (permalink)
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Re: dwell-time calculation: axial vs radial

Quote: (Originally Posted by Scott) View Original Post
So for the *same dimension* scrubber, the dwell time is the same.. implying that there is..... no difference in efficiency between the two... at least in this proportion.... correct?
Yes, That is Paul's view on it. Many of us disagree however, and feel he doesn't understand the roles gas path length and tidal movement play and is focused on static gas modelling and as a result the only answer he can come up with is volume is the determining factor. One has to ignore how a rebreather works to arrive at this theory. He isn't wrong as such but rather has opted for an over simplified model that results in a part answer.

For the record, it is well understood that gas moves through a rebreather in steps (breaths) and dwell time is directly related to the size of these steps and the distance from one side of the scrubber to the other. In short (and generally speaking) axials, due to their longer bed length have a longer dwell time. The trade off is a higher WOB.
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Last edited by Steve : 5th January 2007 at 02:49.
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Old 5th January 2007, 03:20   #7 (permalink)
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Re: dwell-time calculation: axial vs radial

Steve,

I am not an engineerer.. but..
I can see logic.. in both explainations..

By the flowing along the radius, the Radial scrubber is going either from a larger surface area, to a smaller.. or conversely from a smaller surface area, to a larger.

When passing through the larger surface area, it should have a lower velocity, and while passing through the smaller surface area, should have a higher velocity.. which is shown in theory in Paul's spreadsheet..

As you suggested that his explaination uses static flow, versus more human tidal flow.... I would think, would affect both designs similarly?

On the Axial design, it seems to me, that the dwell time would be Uniform for the entire scrubber, ... where as on the Radial the dwell time would be smallest at the inner diameter, and highest on the outer diameter.

I can see how this could be a negative, resulting in rapidly exhausting the scrubber in the outer diameter volume, and not allowing sufficent dwell time to utilize the inner diameter volume...

Maybe you could explain to me.. in regards to axial scrubbers, why it is more common to have tall, smaller diameter design versus a short, large diameter design.


In my mind, given the same volume, an nearly equivalent amount of gas passing through whether tidal or continual, (difference due possibly due to WOB).. It seems, that the larger diameter cannister would reduce the velocity of the gas such that the dwell time remains the same. In the smaller diameter cannister, the velocity would be higher.

My head hurts =(

Thank you for any education I will soon likely receive =)

-Scott
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Old 5th January 2007, 05:34   #8 (permalink)
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Re: dwell-time calculation: axial vs radial

Quote: (Originally Posted by Scott) View Original Post
Steve,

I am not an engineerer.. but..
I can see logic.. in both explainations..

By the flowing along the radius, the Radial scrubber is going either from a larger surface area, to a smaller.. or conversely from a smaller surface area, to a larger.

When passing through the larger surface area, it should have a lower velocity, and while passing through the smaller surface area, should have a higher velocity.. which is shown in theory in Paul's spreadsheet..

As you suggested that his explaination uses static flow, versus more human tidal flow.... I would think, would affect both designs similarly?

On the Axial design, it seems to me, that the dwell time would be Uniform for the entire scrubber, ... where as on the Radial the dwell time would be smallest at the inner diameter, and highest on the outer diameter.

I can see how this could be a negative, resulting in rapidly exhausting the scrubber in the outer diameter volume, and not allowing sufficent dwell time to utilize the inner diameter volume...

Maybe you could explain to me.. in regards to axial scrubbers, why it is more common to have tall, smaller diameter design versus a short, large diameter design.


In my mind, given the same volume, an nearly equivalent amount of gas passing through whether tidal or continual, (difference due possibly due to WOB).. It seems, that the larger diameter cannister would reduce the velocity of the gas such that the dwell time remains the same. In the smaller diameter cannister, the velocity would be higher.

My head hurts =(

Thank you for any education I will soon likely receive =)

-Scott


Hello Scott, first off if you look at a spent radial scrubber in-out flow, you will notice the spent sorb clustering around the inner tube and less color change on the outside edge, showing that most of the radial dwell takes place on the exhale side.

I think Steve is right that the tidal cycle is the missing factor in the comparison, it's the only explanation for why a radial works at all as without it and if the gas was flowing at a constant rate, it would fill up the scrubber and just keep flowing out at whatever rate the flow and restrictions dictate and would in fact be no different than an axial of the same weight.

Paul may believe that the pressure drop btw the inner and outer side of a radial is inconsequential, but I don't, especially when you factor in the tidal/step cycle that the breathing gas follows in a CCR powered by a set of human lungs. The flow of the gas is nowhere near constant, it ebbs and flows and I think this is where the radial shines as it's asymetrical gas path interacts more favorably with the tidal cycle. During an inhale or an exhale, you have lower velocity at the begining and end and the gas will slow and actually stop before being drawn through the inhale side of the loop. And any pressure drop at all is going to affect the dwell as that exhaled gas runs out of velocity, IMHO. -Andy
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Old 5th January 2007, 08:06   #9 (permalink)
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Re: dwell-time calculation: axial vs radial

What is also not taken into consideration is the gas will travel at different speeds in different parts of the scrubber, for instance gas will travel faster (less dwell time) on the edges where the granules meet the smooth face of the cannister. I think this is less likely in a radial can which may contribute to the supposed better performance of the radial scrubber, at least in terms of duration.

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Old 5th January 2007, 08:20   #10 (permalink)
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Re: dwell-time calculation: axial vs radial

Quote: (Originally Posted by dave t) View Original Post
What is also not taken into consideration is the gas will travel at different speeds in different parts of the scrubber, for instance gas will travel faster (less dwell time) on the edges where the granules meet the smooth face of the cannister. I think this is less likely in a radial can which may contribute to the supposed better performance of the radial scrubber, at least in terms of duration.

Dave
hello dave, this type of non-uniform gas-speed distribution is not taken into account, but this does not influence the 'overall' dwell time, as the scrubber is not a 'gas stocking device'

I will not restart the debate about dwell-time, I made my point and I know what I know...

But as you all know, I never said that a radial can not be more efficiant than an axial, I think we all agree on that. But this is due to other factors, like thermal design (isolation), non-uniform gas-flow due to 'water-stocking' in the sorb, non-uniform sorb packing due to position of the cannister during diving etc etc etc

regards
paul
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