Since oxygen transfer efficiency (OTE) is directly related to submergence, it would make sense that a diffuser manufacturer would locate the diffusers as close to the tank floor as possible. While that is true to an extent, best practice dictates that the piping and diffusers should not be located too close to the tank floor. Piping and diffusers too close to the tank floor could result in the creation of eddies and low velocity spots around the aeration equipment, leading to deposition of solids and an anoxic condition within the accumulated sludge.
However, locating the equipment slightly off of the floor means that an acceptable scouring velocity can be maintained between the piping and the floor – preventing solids build-up. Positioning the diffuser surface above the floor requires balancing:
In general, the height of the diffusers is determined by the following factors:
The final submergence can be calculated after these variables have been finalized and the grid arranged.
To calculate At/Ad, the tank area in square feet (or square meters) is divided by the membrane area in square feet (or square meters). In the case of a 9” diameter disc diffuser, the area is 0.41 ft2 (0.038 m2) per diffuser. Typical diffuser densities will range from approximately 4.5-20, with an allowable range of 4-40 without the need for special consideration.
The percent floor coverage is simply the inverse of At/Ad, so an At/Ad of 4.0 will equate with a floor coverage of 25%, while an At/Ad of 40 equates to 2.5% floor coverage.
High density grids are generally considered zones with an At/Ad of less than ~5, while low density grids are zones with an At/Ad of greater than ~15. Any grid design with an At/Ad greater than 40 is not considered ‘full floor coverage,’ and therefore would be prone to solids separation and tank stratification unless supplemental mixing is incorporated.
