^ Got it. So you simply flow "normal" rate of water through the sulfur media and that allows you to build up enough biofilm to produce nitrification/denitrification 20x greater? Interesting. I guess it's not that hard to try it out.
The fluidized biofilm wastewater management systems never reported 20x greater denitrification. If you read about those systems you quickly realize there is nothing special about biofilm reactors. What you are saying is different. You are simply saying to flow the water through the media in an oxic style and allow the inner depth of biofilm perform denitrification. Worth a try.
The BADES/biofilm reactor works with sulfur only right? In other words, 20x greater denitrification is attributed to sulfur biofilm, and it will not grow as successful on other media?
Not at all. Heterotroph denitrification is a lot more effective as is autotroph denitrification but needs an organic food source. Elemental sulphur is used as a base and substratum to grow a biofilm containing autotroph sulphur bacteria on the surface. b
The flow rate is not unlimited as we want to have control over the nitrate removal rate. The nitrate removal rate is controlled by the flow in accordance with the nitrate level. The reactor must be big enough! to handle the amount of oxygen entered. Once in balance with the system a BADESS is self-regulating.
At very high flow control over the nitrate removal rate is lost but the reactor will still remove ammonia and nitrate. When the flow is to high the biofilm may detach from the substrate and or the erosion may become to high to be replaced in time.
A sulphur denitrator ( with closed loop) managed following the guidelines of Longouet will remove 10 to 20 times more nitrate compared to a sulphur reactor of the same volume that is kept anoxic, this at low nitrate levels. At high to very nitrate levels the results become more equalized . An anoxic kept sulphur-reactor will not remove ammonia.
To lower the nitrate level only a bit more as the daily production must be removed daily. At a high nitrate level the flow may be very limited to achieve that. At a low nitrate level a high flow is necessary to remove the same production. The water contains +- 6 ppm free oxygen which at some point makes it impossible to keep a reactor anoxic at the flow needed for removing the production.
The best results are achieved when the sulphur is mixed with +- 30% Calcium Carbonate media (CC) and used in batch reactors. We use continues flow reactors.
BADES should be used in combination with a calcium carbonate source.
it is known that the best results are realized when mixing the sulphur with the calcium carbonate(CC) media. In seawater addition of CC will neutralize the effect of nitrification and autotroph denitrification on the alkalinity and produce some calcium.
oyster grit, aragonite, a commercial product for calcium reactors? One dissolves more easily as the other but it will certainly clog together after some time. If a lot of ammonia is removed daily chalk may be produced. Sulphate precipitates. This means that the calcium carbonate source has to be replaced ore cleaned regularly meanwhile removing the precipitated sulphate. In the case it is mixed with the sulphur we have to replace everything, certainly when it is clogged together. This way the activated sulphur is lost.
In a reef aquarium the ammonia production is very low compared to a commercial aqua-culture system. Must the Sulphur be mixed with the CCmedia ?
One can use one reactor with two chambers or two separate reactors?
In a BADES biofilm reactor we want to cultivate a healthy biofilm without clogging the media and the reactor, which will occur when an organic food source is added We do not want a biofilm growing on the CCmedia as the contact with the water column will be lost.
We prefer to use separate reactors.
For to be used in a BADES bio-filter we use activated sulphur pellets mixed with 50% CC to make the sulphur rolls.
We advice to use activated sulphur ( sulphur that was conditioned).