Influence of the characteristics of organic matter on the efficiency of horizontal subsurface-flow constructed wetlands

Resumen

Subsurface-flow constructed wetlands (SSF CWs) constitute a proven technology for treatment of urban wastewater. One of the principal objectives of CW treatment is to remove organic matter, suspended solids and nutrients from the settled wastewater. The organic and mineral matter contained in urban wastewater is composed of a complexity of substances of different sizes and chemical compositions. In conventional treatment systems it has been demonstrated that the particle size-frequency distribution of the influent wastewater can affect treatment efficiency. However, very few studies have been conducted in SSF CW to determine whether factors such as the size-frequency distribution or organic matter characteristics affect treatment efficiency. Thus the initial hypothesis of this work is based on the supposition that in SSF CW systems, the characteristics of the dissolved and particulate organic matter can influence the removal of COD and ammonium of wastewater. The designed studies were conducted in small experimental SSF CW units that were shallow (0.27 and 0.3 m), and with a surface area of 0.54-0.77 m2. The SSF CWs were planted with Phragmites australis and in most of the studies the treatments received wastewater on an intermittent basis. Wastewater used in these studies was either synthetic or settled urban wastewater. The synthetic wastewater was prepared with tap water and composed of glucose (organic matter easily biodegradable), starch (organic matter slowly biodegradable) and nutrients. In Chapters 2 and 3, details are provided to illustrate that shallow SSF CW provided excellent removal of COD, with average removal rates ranging from 70 to 94% irrespective of the type of organic ubstrate (glucose vs starch) or organic loading rates (5-6 g COD/m2.d to 20-22 g COD/m2.d). The ammonium-N removal in these systems was moderate, with the glucose-fed SSF CW providing marginally better removal (45 to 57%) as compared to the starch-fed system (40 to 43%). The hydraulic conductivity was low in the system fed with glucose due to the presence of a greater growth of biofilm. In experimental SSF CW treating urban wastewater, the application of the physico-chemical pretreatment did not improve COD effluent concentrations as compared to the no-pretreatment control (82 vs 88%), but did reduce turbidity and COD concentration in the influent. The removal rates of ammonium-N were similar in both systems and ranged from 63 to 94%. The hydraulic conductivity was higher (28 m/d) in the system with treated wastewater as compared to the control (20 m/d). These results indicate that the pretreatment could possibly help to reduce pervasive solids accummulation in the inlet zone (Chapter 4). Chapter 5 describes a study designed to evaluate treatment efficiency in experimental SSF CW that were operated with either intermittent or continuous feeding. The COD removal rates were relatively high and merely identical in both systems, with an average value of 78%. Ammonium-N removal was significantly higher (P<0.05) in the intermittently fed system as compared to the continuously fed system (87 vs. 69%). The enhanced removal of COD and ammonium-N observed in the present studies were attributed to several factors including shallow wetland beds, macrophyte aboveground biomass, and more oxidizing conditions in the root zone. Chapter 6 provides survey-type information for six full-scale SSF CW. The data indicated that the greatest amount of solids were deposited within the inlet zone (3-57 kg/m2), with significantly less solids near the outlet (2-16 kg/m2). It was apparent that the amount of solids deposited near the inlet was highly variable and was correlated with respective loading rates (3.1-17.5 g COD/m2.d; 2.6-10 g TSS/m2.d). Analyses of the accumulated solids showed them to be approximately 20% organic matter, extremely recalcitrant and difficult to degrade under either aerobic or anaerobic conditions. Hydraulic conductivity values were significantly lower near the inlet zone (0-4 m/d) as compared to the outlet zone (12-200 m/d). Chapter 7 lists the main conclusions for each of the chapters and provides suggestions for future investigations.