search.noResults

search.searching

dataCollection.invalidEmail
note.createNoteMessage

search.noResults

search.searching

orderForm.title

orderForm.productCode
orderForm.description
orderForm.quantity
orderForm.itemPrice
orderForm.price
orderForm.totalPrice
orderForm.deliveryDetails.billingAddress
orderForm.deliveryDetails.deliveryAddress
orderForm.noItems
TECHNICAL FEATURE


drain TRADER


SAF optimisation data shared at wastewater conference


      


Data from a study to improve optimisation of SAF wastewater treatment systems is the focus of a presentation from WPL taking place at the 2020 European Water & Wastewater Management conference on 13- 14 October. WPL’s technical director Andrew Baird and Ashley Lawrence, PhD student at Portsmouth University, will explain how enhancement of the air and power dynamic associated with ammonia removal in submerged aerated filter (SAF) systems, can deliver significant cost savings.


SAF treatment is traditionally viewed as a high cost process due to the energy requirement in delivering high volumes of air and is generally not considered for larger schemes. Adequate oxygen is essential to ensure that bacteria in the wastewater does not break down odour-free compounds into odorous compounds.


Data featured in the presentation, which takes place on day-two of the virtual event, comes from an ongoing programme of study at Southern Water’s Petersfield wastewater treatment plant. It shows that precise control of the process means SAFs can biologically remove nutrients much more efficiently.


16 drain TRADER | November 2020 | www.draintraderltd.com


Biofilm formation on specific media primarily depends on the mass transport of nutrients across their surfaces and their subsequent conversion to odour-free compounds through aeration.


Varying the aeration rate affects the movement of neutrally buoyant media, oxygen transfer rates, flow conditions and the way biomass adheres to and shears off surfaces. This can significantly reduce power consumption per person equivalent treated.


Excessive or inadequate aeration can lead to operational problems for the treatment process including a high sludge volume index (SVI) resulting from biofilm and floc breakup or


ineffective treatment of ammonia during high loading of the plant.


“These are interim results from our study,” said Baird. “We are seeking to define the actual performance parameters for SAF treatment in various applications, and at different scales, with the aim of determining precise design criteria for SAF nutrient removal.


“There are actually very few papers written on the SAF process and often engineers take information from activated sludge systems and transfer it to SAFs, but the systems are not the same.


“At the heart of WPL’s Hybrid SAFTM technology are unique flow characteristics that have been patented,” Baird explained. “These ensure an even and continuous flow of nutrients up through the submerged, moving bed.


“The slowly circulating media gradually descend due to their increasing specific gravity from hosting growing biomass. Using gravity in this way, opposed to using energy, results in a significant reduction in power consumption, improving overall efficiency and enabling a reduction in site footprint and a deployment of a more compact unit.”


Page 1  |  Page 2  |  Page 3  |  Page 4  |  Page 5  |  Page 6  |  Page 7  |  Page 8  |  Page 9  |  Page 10  |  Page 11  |  Page 12  |  Page 13  |  Page 14  |  Page 15  |  Page 16  |  Page 17  |  Page 18  |  Page 19  |  Page 20  |  Page 21  |  Page 22  |  Page 23  |  Page 24  |  Page 25  |  Page 26  |  Page 27  |  Page 28  |  Page 29  |  Page 30  |  Page 31  |  Page 32  |  Page 33  |  Page 34  |  Page 35  |  Page 36  |  Page 37  |  Page 38  |  Page 39  |  Page 40  |  Page 41  |  Page 42  |  Page 43  |  Page 44  |  Page 45  |  Page 46  |  Page 47  |  Page 48  |  Page 49  |  Page 50  |  Page 51  |  Page 52  |  Page 53  |  Page 54  |  Page 55  |  Page 56  |  Page 57  |  Page 58  |  Page 59  |  Page 60  |  Page 61  |  Page 62  |  Page 63  |  Page 64  |  Page 65  |  Page 66  |  Page 67  |  Page 68  |  Page 69  |  Page 70  |  Page 71  |  Page 72  |  Page 73  |  Page 74  |  Page 75  |  Page 76  |  Page 77  |  Page 78  |  Page 79  |  Page 80