Simple Steps to Save: The Economics of Clean

From the earliest days, water was a convenient and efficient way of conveying the collected wastes to a centralized location to where they could be processed. Since then, great strides have been made transitioning the Wastewater Treatment Plant (WWTP) from simply capturing and treating collected sewerage into a valuable resource generator. As populations increased and climate conditions stressed the availability of water, it became practical to develop techniques to harvest the transport water for reuse back into the community.

In both the articles: “Don’t Waste That Energy. Put It To Work.” and “Resource Hero: The Treatment Plant Operator” the focus was on the effect of extracting resource from the waste stream to offset the costs associated with the operation of the facility. In particular the focus was on energy generation and energy savings.

HUBER Screenings Wash Press WAP® SL - volume, weight and disposal cost reduction of up to 85%
Screenings amount for various types of screens

When looking at the operational costs of a wastewater treatment plant, the top two categories of expenditures are energy, and disposal costs. By taking a closer look at existing techniques being employed in a WWTP it is possible to continue lowering operational costs. In many cases, it is possible to actually pay for newer technologies with the savings realized through that process of optimization.

The makeup of material for disposal in a WWTP is typically comprised of screenings captured at the headworks, grit collected in the settling chambers, and sludge separated in the clarifiers and digesters. The trend in WWTP design is to move to finer levels of both screenings and grit capture. This is largely driven by the need to protect the addition of technologies being employed further into the process to achieve increasing treatment objectives and performance goals.

What Is Entering The Headworks?

The screen type selected for the primary screening in the headworks can have a radical effect of the actual quantity of screenings captured and isolated out of the waste stream flow. In the article “Screening Considerations – A Guide to Selection” a comparison was shown of various screen types and the effect of screenings capture. For instance, going from a ½” bar screen (510 ft3/Mgal) to a ¼” bar screen (7-20 ft3/Mgal) can double the volume of screenings captured.

As the screening elements get smaller and the screenings capture efficiency increases, higher levels of organics are captured along with the inert screenings debris. Not only does this affect the volume of the screenings, it also removes valuable energy laden organics from the process that could be used in digestion and nutrient removal processes.

By looking at the captured screenings and how they are processed for disposal it is possible to greatly reduce the volume to be disposed. Additionally, the organics can be separated and returned to process. Wash Presses play an integral role in processing the captured screenings prior to disposal.

HUBER Coanda Grit Washing Plant RoSF4: Grit separation, washing, dewatering in one system
Washed grit removed at a wastewater treatment plant

Grit is another area that optimization can provide operational savings. Quantifying the actual volume of grit entering the plant is much more elusive. Grit is less predictable because the presence of grit has more to do with the location of the facility and the condition of the related collection network. The actual potential of grit concentrations in the incoming stream to a wastewater plant can range from 0.53-5.0 FT3/MG. Much of the current debate of recent is in the size range of the grit particle a given technology can actually remove. Some technologies currently have the ability to capture as far down to >75 micron.

Changing Classification

In an immediate sense, the issues caused by grit are the effects present if the grit is not captured. Left free to enter the plant, grit ends up filling space in the bottom of clarifiers, aeration basins, and digesters. The abrasive quality of grit also prematurely wears down pumps and valves, adding to operations and maintenance overhead.

The actual makeup of typical grit extracted out of a grit basin can have over 50% water and organics. That volume can be reduced and the capture of actual grit optimized with the use of a grit classifier washer. By classifying and washing the grit, water and organics are returned to the process without losing the grit, making it possible to cut the grit disposal volume in half. 

In certain cases this technique allows the cleaned and classified grit to be used as landfill capping material. An installation in Wisconsin was able to optimize volume of the grit for disposal as well as the classification of the material resulting in a 79% tipping fee decrease, with the leftover material being able to be used as a landfill cap. 

Small Changes Add Up

It seems that a majority of the discussion is focusing on volume reduction of sludge. Rightfully so. The handling and disposal of sludge is right up there and second in line regarding major overhead considerations for a WWTP. But sometimes giving a closer look at related processes, small changes can add up to big savings through process optimization. The combination of these improvements can really add up. As it has been said before: “Small changes, big results…”