Assessing the potential of enhanced primary clarification to manage fats, oils and grease (FOG) at wastewater treatment works

• Published in: The Science of the total environment 2020-08, Vol.728, p.138415-138415, Article 138415
• Main Authors: Collin, Thomas Denis, Cunningham, Rachel, Asghar, Mohammed Qasim, Villa, Raffaella, MacAdam, Jitka, Jefferson, Bruce
• Format: Article
• Language: English
• Subjects: Dissolved air flotation (DAF); Hexane extractable material (HEM); Primary sedimentation tanks (PSTs); Sewage treatment works (STWs)
• ISSN: 0048-9697; 1879-1026
• DOI: 10.1016/j.scitotenv.2020.138415

Daily, sewage treatment works (STWs) receive large volumes of fats, oils and greases (FOG), by-products of food preparation. To increase FOG removal at STW, conventional primary sedimentation tanks (PSTs) can be enhanced using chemical coagulant or through dissolved air flotation (DAF) techniques. This work aimed to assess the potential benefits of enhanced primary treatment for FOG removal through an energy and costs analysis. To achieve this, a five-year sampling programme was conducted monthly at 15 STWs measuring FOG concentrations in crude and settled sewage (i.e. after primary treatment). In addition, two DAF pilot systems were trialled for four months and their performance, in terms of FOG removal, was assessed and compared to that of a control primary clarifier. Across the 15 STWs, influent FOG concentrations were found at 57 ± 11 mg.L−1. Chemical coagulants dosed prior to PSTs increased FOG removal rates on average to 71% whilst traditional sedimentation only achieved 50% removal. Effluent FOG concentrations were found between 12–22 mg.L−1 and 19–36 mg.L−1 respectively. By contrast, DAF achieved FOG effluent concentrations on average at 10 ± 4 mg.L−1 corresponding to 74% removal from a relatively low influent concentration of 40 ± 30 mg.L−1. Thus, enhanced primary treatments have the potential to reduce organic load to secondary treatment and increase energy generation through anaerobic digestion. The overall net energy balance was estimated at 2269 MWh.year−1 for the DAF compared to 3445 MWh.year−1 for the chemically-enhanced PST making it a less financially attractive alternative. Yet, in the case where the works require upgrading to accommodate flow or load increases, DAF appeared as a sensible option over sedimentation offering significantly lower capital costs and footprint. In relation to FOG management, upgrading all STWs is not realistic and will require understanding where the benefits would be the highest. [Display omitted] •FOG occurred at concentrations of 57 ± 11 mg.L−1 in crude sewage.•Conventional sedimentation removed between 33 and 64% of FOG.•Chemically-assisted clarification increased FOG removal between 64 and 76%.•Removal efficiency was 74 ± 10% for DAF with effluents as low as 10 ± 4 mg.L−1.•DAF is a sensible option over sedimentation if the works require upgrading.