Impact of process parameters of thermal alkaline pretreatment on biogas yield and dewaterability of waste activated sludge. (1st September 2021)

• Record Type: Journal Article
• Authors: Toutian, Vahid; Barjenbruch, Matthias; Loderer, Christian; Remy, Christian
• Is Part Of: Water research. Volume 202(2021)
• Publication Date: 2021-09-01
• Subjects: Wastewater treatment plant -- Pondus -- Thermal hydrolysis -- Biodegradability -- Anaerobic digestion -- Dewatering; Water -- Pollution -- Research -- Periodicals; 363.7394
• DOI: 10.1016/j.watres.2021.117465
• Languages: English
• ISSNs: 0043-1354

Abstract

Highlights: Thermal alkaline pretreatment (TAP) of WAS increases biomethane yield (BY) by 22–97%. Higher initial biodegradability of WAS leads to lower increase in BY after TAP. T < 100 °C is as effective as T > 100 °C in terms of BY increase in TAP. Optimum temperature, alkali dose and treatment time for highest BY were determined. Effect of TAP ( T < 100 °C) on dewaterability of digestate needs more research. Abstract: Thermal alkaline pretreatment (TAP) of waste activated sludge (WAS) before anaerobic digestion (AD) was reviewed. Focus of the review was on impact of TAP process parameters on biomethane yield (BY) and kinetics of AD and downstream dewatering. With higher initial biodegradability of untreated WAS, effect of TAP on BY decreases. Depending on initial biodegradability, BY increase of 22–97% is expected. Treatment temperatures below 100 °C showed to be as effective as temperatures higher than 100 °C in terms of BY increase. Alkali dosage and resulting initial pH have a significant effect on BY increase and showed to have an optimum range of 40–60 mg NaOH per g total solids (TS) of sludge. It is advised that alkali is dosed based on solids content in WAS and monitored by pH. Treatment time of 1.5–5 h is sufficient for an effective low temperature TAP ( T < 100 °C), with longer treatment times showing no positive impact on BY increase. Load of sludge liquor with organics and nutrients increases with more intensive TAP conditions. Despite kinetic enhancement of hydrolysis step in AD, more research is needed to clarify if TAP improves kinetics of entire AD process which determines required digester volume. Impact of TAP on dewaterability of digestate is ambiguous and needs more investigation using standardized methods, also with regards to potential effects on polymer demand. Findings of experimental studies were reflected against available data from commercialized TAP process of Pondus®, throughout review. Finally, important process design parameters of TAP such as input TS and point of alkali dosage are discussed and recommendations for future research are presented. Graphical abstract: Image, graphical abstract