Bubbling up for major energy savings
Aeration is the most energy-hungry operation in sewage treatment, but a technology new to the UK market has the potential to deliver a step change in aeration efficiency, says Paul Barter, principal process engineer at Hydro International
Aeration can consume between 54 and 97% of total energy, depending on the configuration of the plant, according to a recent study (1). Energy costs account for 15-30% of large, and 30-40% of small WwTP's operating and maintenance budgets (2). So increasing the efficiency of the activated sludge system will significantly reduce operating costs.
Good aeration is all about maximising the contact of oxygen from air with the wastewater. There are various processes used for aeration, the most common being the fine bubble diffused air (FBDA) process; other systems such as surface aeration or jet aeration are still used, but are less popular.
The FBDA process is based on perforated rubber disk membranes placed at the bottom of the ditch, through which air is blown to create the bubbles that rise and aerate the mixture. The most efficient process up until now, the FBDA process still only achieves a moderate standard oxygen transfer efficiency (SOTE) and some of the opportunity to transfer oxygen is missed. Nevertheless, FBDA systems remain a major energy drain on operation & maintenance budgets. One new technology - ultra-fine bubble aeration (UFBA) - claims to achieve up to 30% higher SOTE than conventional fine bubble diffusers. UFBA uses rectangular diffusers to deliver many more smaller bubbles over a much larger floor area.
Increasing the contact area of the air to the wastewater provides a greater opportunity for oxygen transfer. For a submerged system, this usually relates to having a smaller bubble.
The smaller the bubble, the larger the ratio between the bubble's surface area and its volume. In UFBA, the 1mm bubble has three times the surface area of a 3mm bubble typical of FBDA systems, leading to a significant improvement in the opportunities for oxygen transfer. Increasing the time that the bubble is in contact with the wastewater will also improve the transfer process. Of course, the easiest solution would simply be to have a deeper tank, but in most cases it's not a practical solution.
A simple bit of classroom science can point us to a clever alternative: buoyancy is a function of the difference between the volume and density of the fluid displaced. Therefore small bubbles have much lower buoyancy and will rise through the wastewater more slowly.
A 1mm bubble has four times less buoyancy force than a 2mm bubble and nine times less than a 3mm bubble. The bubble has a slower ascent through the wastewater, and therefore increased contact time for oxygen transfer.
It is also important to decrease the resistance to transfer. There are many constituents of wastewater that restrict the transfer of oxygen from the air to the wastewater, loosely collected together and applied as the alpha and beta factors for oxygen transfer, converting the actual oxygen requirement (AOR) into a standard oxygen requirement (SOR).
If these constituents can be mitigated, then the alpha and beta factors could rise, meaning less resistance to oxygen transfer. In this respect, both FBDA systems and UFBA systems perform the same. Increasing the partial pressure of oxygen in the air bubbles would also achieve higher transfer of oxygen to the wastewater, as with enriched oxygen and pure oxygen activated sludge systems.
This is an opportunity to increase SOTE, but enriching oxygen is an expense in capital equipment and operation, so any efficiency gains would need to be balanced against the additional costs.
Operators of activated sludge plants will understand the importance of minimising the amount of dissolved oxygen (DO) in the wastewater and maximising the difference in the transfer.
They achieve the lowest possible measures through good plant control, but problems can occur where plant is not calibrated correctly, or where operators do not want to risk pushing the DO levels too close to zero and closing down the process altogether.
Reducing the amount of DO through good plant maintenance and control should be an objective for any activated sludge process, but even in well-run plants, there can still be localised areas where the DO levels are too high.
Disk diffuser systems have only 10% floor coverage, and therefore all the air available for oxygen transfer travels through 10% of the volume of the tank. The more air per area, the more likely that any individual bubble will adversely affect the transfer properties of an adjacent bubble.
Because they have a far greater floor area, ultrafine bubble diffusers lower the flux rate, where flux is the volume of air per membrane surface area. The higher the flux, the more air is being applied to each square metre of membrane areas. The lower the flux rate, the higher the efficiency.
One such UFBA system is the HiOx activated sludge aeration system. Already a proven technology since the 1990s, Hydro International is introducing the technology to the UK for the first time. HiOx promises improved aeration performance and increased capacity as well as reducing energy demands.
As an example of its effectiveness, in a recent installation at Hidalgo, Mexico, a retrofitted HiOx system achieved 46% reduction in energy use and increased plant capacity by 140%, achieved 96% BOD removal. The system continues to save between £9,000 and £25,000 per month.
HiOx is suitable for both retrofitting and new installations and increases transfer efficiency by 20-30% leading to reduced power demands. The system offers lower installation costs, because each diffuser covers a large area equivalent to 100 conventional 22cm disc diffusers.
Due to its innovative design with high-strength perforated polyurethane, HiOx achieves lower maintenance costs as well as a longer life than conventional systems and lower through-life costs.