DSB Heresy

keman said:
..........Now, don't get me wrong-- I'm burying 1/2" PVC tomorrow. :) ... it just may be a year or two before I turn that valve. Maybe I'll turn it when I start thinking my DSB needs a flush ... ;)
Good thought on waiting for the sand bed to develop something before starting the flushing process.
Shoestring, and all others I'm no scientist, just a lowly driver with life expierence. My "gut" feeling still tells me that an eggcrate will work better in the long run without cloging.
From expierence; A while ago I had a 15 gallon DSB/refugium OVER a full size plenium (I could see into the plenium from the side){I have since swaped it out for a 33long, non-plenium DSB}. Over the two years that I operated this tank I noticed an acumulation of a very fine silt at the bottom glass. At the time I was using a UGplate as a seperator. At the time Jalbert mentioned an inch of free water as ideal so I added spacers to raise the plate. (hence the clear view under the plate) Over time I noticed silt droping down and the silt was distintly pilling up directly under the slits of the plate. If I remember correctly it was about an 1/16 of an inch of silt layer acumulated over two years.
WELL;I'm thinking that the volume of the plenium will give the DSB extra years of life before mecenical cloging of the pipes/holes simply by having a place for the mulm/silt to go to without blocking the 1/32 holes. Just have the holes placed on the side of the pipes and nether the top nor bottom so that they draw only water.
Another thing from expierence: I noticed that if I add more Ca (via KALK or calcium reactor) than my corals/halamidia/coroline algae use, the sand bed starts getting compacted regardless of how many worms are working the bed. And I have the full range of critters to work the bed. I have to go in and fork or finger the bed to fluff it up.
So in short, the Idea of CPW sounds realy good to me as a way of extending the life of a DSB and avoiding sulfide pockets. But I still feel that the sand will need replenishment and maintenence every now and then.
Another thought; For those of you that have or had UG plates. Dig them out of your attics and look at them. The slits are NOT uniform but vary in size as you go further from the riser tubes.
Addressing Keman's concern. Maybe a eggcrate is not the way to go but instead using the traditional UG plate. The variably sized holes might address the pressure diferential question.

Getting credit where credit is due;Shoestring My "method" is spelled, The Borecki method. :D
Boys; lets play nice!
Boris.
 
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IME with p/dsb, I've noticed thru the yrs. that from time to time the bed does develop areas of near-solid clumping, especially around the back areas that is difficult to funnel-syphon. I've had to use a ice pick at those times to return the "sand-rock" back to it's original consistency. This occurs from the varying levels of CA/buffer & KW drip & of course, would result in channeling. For CPW to function over time, this will need to be addressed with cleaning the bed periodically,Bob
 
Boris, IMHP, I've always cleaned the bed wkly from the very beginning. I see no benefit in allowing nurient waste build up within the p/dsb & this allows uniformity in the system's parameters,Bob
 
Scleractinian said:
What if you placed a sheet of acrylic, perf'd with uniformly distributed orifices and sealed to the tank sides w silicone, over the eggcrate, or just over a simplified PVC grid...?

AND

Might you also consider and comment on what may be the relationship of the function of your process to the mode of 'wasting'... What would you think of a continouos (non-pulsed, dropwise or via peristaltic pump) withdrawl of 'liquor' vs. your your present method? Are you hoping to move solids through the bed... at relatively very low velocities and only intermittently? Seems slower, uniform flows might make for best hydraulic uniformity, but would perhaps not be compatible w/ the chemistry desired...?

AS WELL AS

...have you considered testing your 'liquor' for PO4, Nx, etc? Might be interesting to relate what's coming out w/ your observed RedOx in another part of the system.


Just wanted to kinda bump a couple of parts of my previous post for all... Especially the sealed-drilled-uniformly-distributed-acrylic plenum (SDUDAP ;) ) idea.

And again... the sarcasm is friendly... I'm a Fluvial Geomorphologist/Ecologist mostly, not an engineer.

DarrelH and FredFish, I'm trying to avoid making up my own laws of fluid dynamics (another friendly ;) ), so I'd like to refresh my memory on the hydraulics of slow bed flows before I post anything that might cause people to lose confidence in either the safety of their drinking water or the function of their septic system... ;) (<---still meant in good humor)
 
with the buried pipe idea, flow will not necessarily enter all holes equally, especially if the substrait gets clogged.

The area near each hole will have a higher flow and will tend not to clog. I agree that some clogging may occur between the holes and in the higher levels of the substrate, but at least you have some drainage at discrete points throughout the bottom. With a planar pressure approach, some large areas may shutdown entirely without any drainage.

One other thing to remember is the sand that ldrhawke is recommending is about 10x as coarse (1 mm min) than what Dr. Ron suggests for his DSBs. The coarser sand will tend to clog less (and blow around less...YEAH :)).

Darrell
 
I really think any way people want to set up plumbing-plenum or buried pipe-will probably be OK. That will ultimately be a trial-and-error/learn from experience kind of thing, and I suspect that some people will get either method to work, and some people will have problems with each method.

Two things that I DO think should be explored, at least for my understanding:
1) Phosphate retention and release.
2) The presumed function of the system.

1) Phosphate retention and release:
I think this must be addressed more in-depth because it appears to be the single-largest problem with DSBs. The initial post indicates that by preventing a pH reduction in iron-rich substrait, the release of previously retained phosphate can be prevented.
I am not aware of iron content in DSBs that is significant enough to be part of the driving force in phosphate release. If it is, or if the release of phosphate from calcium-based substraits is triggered by a similar condition, the information would be appreciated. The prevention of phosphate release is required for long-term function of the system.

2) The presumed function of the system:
If water is removed from the bed on a daily basis, or even more often, the detritus and nutrients in the DSB will simply be removed from the tank. Their removal suggests that any biological activity to break them down is not required, with the exception of providing food for tank in habitants (something that is questioned in DSB tanks). Mechanical filtration, such as wet skimming, and turf scrubbing, can perform a similar function of waste removel while preserving tank space, reducing set-up and maintenance complexity, and eliminating uncertainty. In addition, the coarse substrait means many botton sifters can not be kept, and the removal of flow from the bottom means burrowing animals can not be used. Edit<Basically, it sounds to me like a complicated system for mechanical removal and frequent water changes>
In other words, why not just run a wet skimmer and throw some macro algae in the sump? Edit<This system> may be "better than DSBs", but just because a bi-plane is faster and carries more payload than a write flyer doesn't mean we're using bi-planes for fighter jets.

BORECKI said:

Getting credit where credit is due;Shoestring My "method" is spelled, The Borecki method. :D
Boys; lets play nice!
Boris.
Oops, sorry. I kept spelling it Bohreki, as a matter of fact, and was pleased when I removed the "h".:p
 
Questions by Scleractinian

I have no problem trying to answer your questions, as long as you are a "civil" engineer....a little humor back :strooper:

Could you elaborate a bit on the hydraulic problems with using eggcrate over the grid, as suggested?

Keep one basic thing in mind, which I know you understand. Fluids always flow to the lowest pressure area. Or to put it another way, fluids will find the path of least resistance and easiest way out of or into a container. This basic law of Fluid Dynamics is being ignored in trying to justify and make an egg crate plenum work.

When a fluid transfer system is being designed for low flow rates and low pressure. It becomes very difficult to control where and how fluid moves. The slightest change in resistance to flow will cause major maldistribution.

You have several ways to over come this problem, one is to increase the flow rates and/or increase the back pressure to obtain even distribution.

A grate plenum system will develop very little back pressure, unless you have very high flow rates. We don't have this in CPW so I have designed it to work for reduced flow rates.

Tank substrate is never perfectly uniform, and even becomes less uniform as detritus starts to fill voids, currents move the bottom around, and it ages. With low flow rates and low pressure the slightest variation in the bed density or depth will cause the fluid flow to that area or the slightest increase in backpressure will divert the flow around the area. With low flow rate systems flow can virtually stop into areas of very small increases of resistance.

As an example: The substrate bed in a tank is never perfectly flat. Density or porosity is not perfectly uniform. Also many tanks are set up with the substrate lower in the front of the tank and get higher in the back. If you had and egg crate plenum on the bottom you with very low resistance to flow, and if you removed a gallon of fluid from the plenum, what area on the surface of the substrate do you think the plenum would be replenished from.

Obviously nearly all the fluid would be pulled into the plenum from the front that has the shallowest depth and the lowest pressure drop. Little or no flow would come from the back.

Also when you pull the fluid out of the plenum, the closest lowest pressure drop zone, to that point of discharge, will be the area the fluid is pulled from.

An example. Exaggerated for effect. If you had your egg crate plenum 30 feet long and you where removing fluid from one end. How much fluid to you think would move down into the plenum chamber from the far end of the tank...Zero or non-measureable to be more accurate.


If you're trying to avoid short circuiting and channeling, it seems that drawing a small volume from a more discrete plenum space would actually help to accomplish this...

Ido not I understand your question? But drawing a small volume assures of short circuiting. You are not trying to avoid short circuiting as much as you are control it. Short circuiting will always happen. You are just trying to make it happen more uniformly and over a larger area.

What is your meaning of discrete plenum space?

Visual Maldistribution a couple of Examples:

Picture a 20 foot long piece of 1" pipe, capped at one end and connect a water hosed to the other end. The same size 1" hole drilled every 6 inches. To make it easier to visualize flow is out not in. (Fluid flowing in or out not much difference in the principle I want to demonstrate. ) Open the valve wide open hold the pipe horizontal with the holes up,. What do you think you will see. Most of the water will come out of the holes closets to the hose with the end. Make the 1" hole 1/32".....because you have water pressure and are restricting the flow, the water will shoot up a stream close to the same height uniformly from each of the holes.

1. If the pipe is large enough in diameter so it had little pressure drop from friction, water would shoot out of the all holes, and all the streams would rise to about the same height.

2. If the pipe was a small diameter you may have water shooting out at decreasing height as you moved away from the hose end.

3. Now take and add a very short riser pipe, 1/4" in height, to some of the holes. With high flow rates, which causes a pressure drop across the holes, the water will still shoot out relatively the same height.

Now slowly close the water valve and reduce the flow. As you reduce the flow you will see As you reduce flow, the holes slight 1/4" risers, will stop flowing any water at all and all the water would come out of the holes without the riser. That is caused by only a 1/4" in water column back pressure.

What does this have to do with a plenum on the bottom of the tank.....everything. The only way you can equalize the flow into or out of the plenum is to either increase the flow rate or reduce the outlet area, both of which are causing an artificial pressure drop. What you are doing is causing a controlled short circuiting. The more small holes simply control where you want the short circuiting to happen.

If you now covered this plenum piping I describe, or used no piping, and had the flow into our out of the egg crate plenum, which had little or no pressure drop at low flow. You would have accomplished nothing. You would be right back to the original maldistribution of the 20' long pipe with 1/4" risers.


What if you placed a sheet of acrylic, perf'd with uniformly distributed orifices and sealed to the tank sides, over the eggcrate...?
This is probably the next closest approach that could be made to work. A sheet with a lot of small holes. The problem would be plugging. So to try and avoid plugging you would cover the holes with filter material. If you used a thick spun filter material, similar to the Poly Filter a lot of us use to remove phosphates, it would actually add a plenum space above the holes. For the most you would now have nearly the same maldistribution conditions your went to all the trouble to get around with a plastic sheet drilled with holes.


What would you think of a continuous (non-pulsed, dropwise or via peristaltic pump) withdrawal of 'liquor' vs. your your present method
This is back to the low flow condition which will cause maldistribution.

Are you hoping to move solids through the bed... at relatively very low velocities and only intermittently?
NO....the idea is to allow the bacteria in the bed to eat the solids and only see waste in solution.


Seems slower, uniform flows might make for best hydraulic uniformity, but would perhaps not be compatible w/ the chemistry desired...?

Back to the maldistribution problem. The chemistry aspect is a whole topic by itself. The best rate of removal of the concentrating waste on the bottom of the DSB using CPW has yet to be established. What I am doing removing a gallon a day in a 60 gallon system works. It is optimum, probably not.

Several things affect this. Everyone's tank size and bio loading is different. Also, there is a lot of analysis to do in the chemistry of what is happening at the bottom of a DSB. The Theil data indicates that the build up of nitrates and phosphates may be accelerating with time and concentration of the anoxic sulfite soup that is building up. It appears that phosphates may be going back into solution which may be because of the chemistry and pH reduction. If that is the case, this could possibly be used to our advantage and allow us to remove more phosphate build up then we would get without the drop in pH. But, it also appears the reverse is true with Nitrates. They are also increasing which may indicate the sulfide reduction is taking over the bed and slowing the nitrate cycle down. So we may want to waste more frequently to stop that. This is a topic I am discussing with Dr. Randy or chemist whizard.

On the other hand, we may find wasting more once a week is more beneficial that wasting smaller amounts daily. This will only be know with more time and more study. I don't believe anyone reviewing the CPW concept and Theil's data can scientifically or logically reach the conclusion that a DSB will work better without using it.

Also, have you considered testing your 'liquor' for PO4, Nx, etc? Might be interesting to relate what's coming out w/ your observed RedOx in another part of the system.

You have not read or looked at the referenced sites at the beginning of this thread. Theil did an excellent study and collected great data years ago, the impact and significance of of this data has been ignored. It was for a DSB with a plenum, but I contend you would see very similar data from a non-plenum DSB. There is no sound logic to believe otherwise. A lot of study of this has been and is being done. It is the basis of believing CPW will benefit our tanks and improve water quality.

I just stumbled across this thread, and had been considering installing a small (2"x2") plenum connected to a 1/4" poly line to be sampled occasionally by withdrawl via a syringe (primarily 'cause I'm crazy and wanted to see what was going on in the sandbed) in a tank currently being assembled. I might just scale that plenum up a bit.

I am not sure that only doing CPW in a small area of a tank will demonstrate or prove anything.

All of the fluid flow principles, I am trying to explain, I have been using for 20 years in processing waste. There is little to no difference in how they apply and how they benefit fluid flow equalization. The same physical and engineering principles apply at the bottom of a reef tank or maintaining an optimum growth environment for microbes in our patented organic waste treatment process.

Plugging......I have been using the CPW plenum system I describe for over 6 months in my tank. The velocities are low enough to avoid rapid plugging. The flow rate of my system has not changed all, which would the indication of partial plugging. IF.... plugging did start to occur, I would simply back flush and open up the holes. All I need to do is open and close a couple of valves for a minute to accomplish this the way my system is piped. Just like is done with all sand filters in water treatment plants.

I have no intention of getting into any more ****ing contest trying to convince anyone, that uses this forum only to get attention and be noticed, that believes that water flows up hill and uses babble to prove it. I will discuss any topic or gray area on CPW with a "civil" engineer, or non-insulting lay person.

Babbling insulting idiots will be ignored. :p I think if you review my past posts, you will see doing it with a sense of humor has always been my manner. :mixed: :p
 
Quote w/ commentary and clarifications

SNIP


You have not read or looked at the referenced sites at the beginning of this thread. Theil did an excellent study and collected great data years ago, the impact and significance of of this data has been ignored. It was for a DSB with a plenum, but I contend you would see very similar data from a non-plenum DSB. There is no sound logic to believe otherwise. A lot of study of this has been and is being done. It is the basis of believing CPW will benefit our tanks and improve water quality.

I did read them, might have missed this somewhere, but was just wondering if you were actually monitoring nutrient export via your system... and wondering if you could eventually relate easily monitored water-column ORP to what you're exporting.

If so, w/ an AquaController, for example, you might be able to automatically vary wasting interval and dose (I guess waste in this case) to compensate for change in system nutrient balance (accidental heavy feeding, algal succession, etc.)...

By more 'discrete plenum space' I meant sealing the acrylic to the aquarium sides... would a larger number (say every 1/4", OC) of small perf's in such a plate help w/ distribution... still (unfortunately) unclear as to how this might promote channeling more than the buried pipes would... BUT, as I noted, I'm no engineer (civil or otherwise, though my business cards have occasionally referred to me as one... noone knows what an RS or REHS is... in my State I can only cert designs up to 3000GPD) :)

Also, my intention in installing the tiny plenum in my system was for purposes of monitoring rather than processing. Might be interesting to install on a few exisiting DSB's to see how variable the chemistry is among different systems, especially over time...

I have no intention of getting into any more ****ing contest trying to convince anyone, that uses this forum only to get attention and be noticed, that believes that water flows up hill and uses babble to prove it. I will discuss any topic or gray area on CPW with a "civil" engineer, or non-insulting lay person.

Babbling insulting idiots will be ignored. :p

I'm an idiot... but I don't think I was babbling... :)

I think if you review my past posts, you will see doing it with a sense of humor has always been my manner. :mixed: :p

Thanks for this last bit... Humor's hard to convey via text, and harder so in forums such as this one.
 
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I am somewhat intrigued by the conflicting views on this system.
I for one would be greatful for more informative guidance on how to set up this system for my own Reef Tank.
I would be greatful for all relevant info to allow me to go and instal it into my new 5 x 2 x 2 Reef Tank with sump etc. Would also like some info on what constitutes a good sump design, and some good explination on how to design it.

I have run Plennums in the past and had to remove it from my old reef tank due to concreation. One point that I think was missed is that concreation of the substrate can be caused by Alk / Ca imbalance, thus it is crucial to keep in control (I was unaware of this at first, thus the concreation of my Plennum.)
I would like to point out that my aquarium looked magnificent whilst running the Plennum, it was only my uncertanty that made me remove it. I never had any traces on Ammonia, Nitrite, Nitrate, Phosphate (controlled by Rowa Phos)

Any advice will be greatly appreciated for my new design. I am not one to critisize, only add different perspectives.

Regards and thanks
Jay.
United Kingdom

:)
 
ldrhawke,

I was thinking some about pulling water from all areas of the sandbed, and i came up with an idea that i think might allow equal flow from everywhere while avoiding the problem of clogging easily. My idea is to use a pvc grid, but start at the center of the tank and repeatedly tee it off in a symmetrical pattern, and then cover the ends with a fine screen material. The idea by using a symmetrical pattern is that all the water being pulled from the sandbed, no matter where it is coming from, has to travel through the same number of tees and the same lenght of piping. I think this piping pattern would work in a conventional plenum as well.

I have attached a drawing of my idea (red arrows indicate flow direction). What do you think?

later,
steve
 
.
I am somewhat intrigued by the conflicting views on this system.

The only conflicting views are from people that simply do not want to accept the data below and feel they have some way to improve upon what I have described it takes to build a CPW system to work effectively.


This is the Theil report again.....


Below are the results for NO3, PO4, SiO2, pH and and O2. I did not measure any other parameters.

"the data below is based on 30 day interval reading from the plenum"


NO3 PO4 SiO2 pH O2
11 0.7 0.2 7.9 5.4
34 1.8 0.9 7.2 4.9
71 4.1 3.7 6.4 4.2
117 8.1 5.4 6.0 3.9
243 14.7 7.1 5.4 3.7

skipped a few months
for reporting purposes
_
520 19.4 11.3 4.9 3.2
614 21.6 14.7 4.9 3.2
803 23.4 15.3 4.7 3.2

This independent data. Not mine, although I suspected this was happening. This should give anyone looking at the data concern as to what is transpiring in any DSB w/or wo a plenum.

When the pH dropped into the 6's it appears phosphate starts to go back into solution. The problem is to get to a pH of 6 you need a pretty polluted sulfide reduction soup building in the bed. It's release and leaching back into the tank even slowly has rapid negative affects. I have demonstrated this in my tank on numerous occasions. A half cup full of this sulfide soup will drop ORP 150 points in minutes.

Without using CPW, it should be obvious where this data is leading. You have a DSB that is simply a garbage can starting to over flow.

Careful husbandry, monthly stirring, reduced Bio loads, will all help to push back the inevitable. Unless you remove it, the waste building is slowly leaching back into the tank. It has nowhere else to go

concreation
What is concreation....it sounds like a cross between the theory of evolution and portland cement;)

This is not a static plenum system, as you used before. It has no comparison. As the data above should make clear. It is designed to remove that waste you had building in your plenum.



Scleractinian
Quote w/ commentary and clarifications

I did read them, might have missed this somewhere, but was just wondering if you were actually monitoring nutrient export via your system... and wondering if you could eventually relate easily monitored water-column ORP to what you're exporting.
YES..again reference back to what I have stated and published. I have been able to increase my ORP above the set point of ozone feed, by simply increasing the wasting rate. Which was initially on a couple of pints a day

If so, w/ an AquaController, for example, you might be able to automatically vary wasting interval and dose (I guess waste in this case) to compensate for change in system nutrient balance (accidental heavy feeding, algal succession, etc.)...

[/QUOTE] All possible, but over complicating a simple process may cause more trouble than it is worth.

By more 'discrete plenum space' I meant sealing the acrylic to the aquarium sides... would a larger number (say every 1/4", OC) of small perf's in such a plate help w/ distribution... still (unfortunately) unclear as to how this might promote channeling more than the buried pipes would... BUT, as I noted, I'm no engineer (civil or otherwise, though my business cards have occasionally referred to me as one... noone knows what an RS or REHS is... in my State I can only cert designs up to 3000GPD)

[/QUOTE] [ On a large flat plated, you will need a filter material covering the holes to keep substrate from plugging. The substrate will lay right on top of it. When you use a filter material like a spun fiber, its passages will reconnect all the holes and it will again become one large plenum that will cause significant short circuiting. A piping system I describe will still have some short circuiting but with the multiple independent legs, it is less apt to reconnect itself and become one large plenum again. We are trying to control the degree of short circuiting that will always occur[/B]

'm an idiot... but I don't think I was babbling...

I'm not sure about either..... :p
 
SORRY FOR ASKING THE QUESTION!!!!!

I was not after more of the aforementioned insulting remarks that you seem to be directing at others on this board.
You seem too preocupied with your own self indulgance to read thoroughly the wording of the posted replys, to even acknowledge the fact that some on here actually believe in your modified system.
I was interested for you to pass on the correct way of installing this into my own aquarium without trying to decifer all the previous posts, however you seem to indulge yourself in trying to belittle everyone who comments on this quite complicated area that it is pointless in me trying to get any further information out of this post!!!!!

Regards
Jay.

:mixed:
 
On second thought, there may be a way of making a flat plate work

By more 'discrete plenum space' I meant sealing the acrylic to the aquarium sides... would a larger number (say every 1/4", OC) of small perf's in such a plate help w/ distribution... still (unfortunately) unclear as to how this might promote channeling more than the buried pipes would...

If you took and layered out a grid of boxes with a raised 1/2" ridge to make the grid, on top of the flat plate. You could inserted small pieces of filter material into each grid square to cover the holes. The raised ridges would break up the continuous passage made by a single sheet of filter media. A little more complex but with merit if the system was mass produced.
 
Reefer


SORRY FOR ASKING THE QUESTION!!!!!

I was not after more of the aforementioned insulting remarks that you seem to be directing at others on this board.
You seem too preocupied with your own self indulgance to read thoroughly the wording of the posted replys, to even acknowledge the fact that some on here actually believe in your modified system.
I was interested for you to pass on the correct way of installing this into my own aquarium without trying to decifer all the previous posts, however you seem to indulge yourself in trying to belittle everyone who comments on this quite complicated area that it is pointless in me trying to get any further information out of this post!!!!!

Regards

I thought the English had a sense of humor....sorry about the answer to yourquestion

"What is concreation? ....it sounds like a cross between the theory of evolution and portland cement"

I still don't know what concreation is?

Some times you English don't always say what we hear across the pond.

I remember staying in London at Jerrime Fry's flat. The maid asked me as she was leaving, "what time do you want to get knocked up."

I thought it was a great idea, I told he about 11 pm, she didn't see the humor either... :rolleyes:
 
ldrhawke said:
.

Scleractinian
Quote w/ commentary and clarifications

YES..again reference back to what I have stated and published. I have been able to increase my ORP above the set point of ozone feed, by simply increasing the wasting rate. Which was initially on a couple of pints a day


OK. Again, I'm an idiot (seriously :) ), and I have re-read the posts here, and had (and have re-) read the Thiel info. I fully understand that the plenum space accumulates nutrients. I may have missed theanswer to the questions posed below, but I don't think so... The question that I'm doing such a poor job in asking clearly is this:

With your tank (utilizing the 'CPW' process), are you presently monitoring nutrients in your 'waste'... Are you checking PO4, Nx, etc, and logging it over time, especially w/ relation to observed ORP in the upper water column? Not 'has anyone done this' (I read the Thiel essay, and I don't think that many will disagree w/ his data, even if they disagree w/ his conclusions), but are you currently doing this?

I did realize that you are monitoring ORP w/ an ozone controller (see I read it above!) and that your ORP has shown a relationship to volume and frequency of 'waste' (told ya I read above!), even independent of O3 application.

What might be interesting is that one might eventually be able automatically control wasting using water column ORP as a signal to what's accumulating in the plenum... as you are doing manually now.

SO... are YOU testing YOUR the effluent for nutrients? If so, do you notice any relationship between nutrient levels in the effluent and the temporally related ORP observations?

And also, again because I'm an idiot (really, and probably babbling too ;) ) do you think that we should care about what's actually going on chemically in the plenum, or simply watch tank ORP?

And, as always... :)
 
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I was thinking some about pulling water from all areas of the sandbed, and i came up with an idea that i think might allow equal flow from everywhere while avoiding the problem of clogging easily. My idea is to use a pvc grid, but start at the center of the tank and repeatedly tee it off in a symmetrical pattern, and then cover the ends with a fine screen material. The idea by using a symmetrical pattern is that all the water being pulled from the sandbed, no matter where it is coming from, has to travel through the same number of tees and the same lenght of piping. I think this piping pattern would work in a conventional plenum as well.

I have attached a drawing of my idea (red arrows indicate flow direction). What do you think?

That will work. You will still need to cap the pipe ends and drill small holes in the pipe to equalize the flow. With open ends most of the flow would come fron the pipe opening closest to your discharge out let pipe.

You may find with all the connections, you will become size limited very quickly and have trouble fitting it on the bottom.

A simplier approach maybe a few straight runs made up of crosses with legs running off in both directions. Or a straight run the length of the back of the tank made from t's with legs running to the front of the tank.

There is no right or wrong way. You just want to cover the bottom with as much connected piping as you can fit into the tank.
 
ldrhawke said:
On second thought, there may be a way of making a flat plate work

If you took and layered out a grid of boxes with a raised 1/2" ridge to make the grid, on top of the flat plate. You could inserted small pieces of filter material into each grid square to cover the holes. The raised ridges would break up the continuous passage made by a single sheet of filter media. A little more complex but with merit if the system was mass produced.

Since we could backwash, why worry about the filter media? What about filling the grid cells w/ a coarser, more spherical media (CC or granular dolomite maybe) before applying the SeaFlor Special Grade? Many columnar rapid sand filters use exactly this approach.

...or would backwashing aggressively enough to clear the orifices disrupt the substrate enough to make the microbes unhappy......

All... keep in mind... I'm an idiot (seriously) :wildone: .
 
OK. Again....

With your tank (utilizing the 'CPW' process), are you presently monitoring nutrients in your 'waste'... Are you checking PO4, Nx, etc, and logging it over time, especially w/ relation to observed ORP in the upper water column?

I have been monitoring. There are continuous low levels of phopshate, pH, and nitrates in the wasted fluid....I have not mesured for SiO2.

There is little or no measureable level in the water column above. The most obvious thisng is the rotten egg odor present for several weeks in the low level wasting fluid. After a several weeks of wasting the rotten egg smell in the wasted fluid went away. The low levels of nitrates and phosphates remained. pH is always about .4 to .5 lower in the wasted fluid.

After about a month into my testing the ORP meter was struggling to stay at the 350mv set point even with ozone being fed, which indicated to me my water quality was dropping. WHich meant I was still leaching somthing back into the tank from the DSB. The measurements in the water column and the wasted plenum liquid were not varying much.

I decided to increase the wasting rate to nearly a gallon a day from 2 pints a day. This was still far below my normal water change volume. During all this time I have stopped doing water changes.

I was pleased to see the ORP start climbing, and move close to 400mv. All without changing the 350 mv set point for ozone feed. Presently it always remains above 350, unless I feed heavy, and then it dips for a few hours. The ORP readings have never been thsi high before.

Bottomline...CPW has eliminated my need to feed ozone to control ORP. The nitrate, pH, and phosphate readings in the wasted fluid remain very constant.


QUOTE]Not 'has anyone done this' (I read the Thiel essay, and I don't think that many will disagree w/ his data, even if they disagree w/ his conclusions), but are you currently doing this?[/QUOTE]

Yes..read above




What might be interesting is that one might eventually be able automatically control wasting using water column ORP as a signal to what's accumulating in the plenum... as you are doing manually now.

I have it on an automatic timer using an X10 controller and my computer. I know it can be hooked up to an even more automated system controlled maybe by ORP. I would not do this for two reasons.

Controlling wasting from an ORP meter would be a nightmare of over and undershooting. ORP response in the positive direction can take hours to work back to a high level. I am not sure you could control wasting from the readout without having a smart controller than learned.

SO... are YOU testing YOUR the effluent for nutrients? If so, do you notice any relationship between nutrient levels in the effluent and the temporally related ORP observations?

see above.

And also, again because I'm an idiot (really, and probably babbling too ) do you think that we shoud care about what's actually going on chemically in the plenum, or simply watch tank ORP?

Yes and No.....understanding what is happening more fully will probably help to learn more about wasting rate and frequency.

On the other hand, it appears so far that it is very easy to control water quality using CPW without knowing anything about the chemistry.

If you simply set up the system with an ORP meter and waste slightly more than is neccessary to keep it above 350, I don't think the most automated system or knowledge of the chemistry will neccesarily improve upon the end result. I could be wrong.

To put it another way...look at what most everone is doing right now in an effort to make DSB's amd BB's work. It is now almost accepted fact by most that DSB's will fail. The only question is when.

CPW is simplifying not complicating what exists.

This why I have trouble understanding all the debate. No one has been able to say to me look..."here is the potential damage and high risk you are causing my reef system by using CPW".

It's a no brainer to me. I wish someone could tell me what I am missing.
 
Thanks for the response... and note that not everyone has questioned the premise of the process, and that at least a couple have primarily been trying to get enough info to implement it.

I'm still intrigued by the possibility of automating the release of effluent (hence my questions about monitoring the nutrient parameters of the effluent and about the dose/waste volume interval and periodicity)... I realize that the plenum ORP/tank ORP relationship wouldn't be quick or tight...
 
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