A dispersed-ozone flotation(DOF) separator for tertiary wastewater treatment P.K.Jin, X C Wang and G. Hu School of Environmental and Municipal Engineering, Xi'an University of Architecture and Technology, No 13 Yanta Road, Xi'an 710055, China(E-mail: pkjin @xauat edu cn; rcwang @xauat edu cn) Abstract A dispersed-ozone flotation(DOF)separator was devised for a pilot study of tertiary wastewater treatment for re-use purposes. As a compact device combining coagulation, ozonation and flotation in an integrated unit, the DOF separator achieved a very high removal of SS, ToC, Uv254 and colour, as well as effective inactivation of coliform and total bacteria within a short hydraulic retention time of 30 min. The finished water quality is comparable to or better than that by a conventional tertiary treatment process using coagulation, sedimentation, filtration and chlorine disinfection, and meets the quality standards for non- drinkable domestic reuse Keywords Dispersed-ozone flotation; tertiary treatment; water reuse A typical process for tertiary treatment of the secondary effuent usually consists of oagulation, solid/liquid separation and disinfection units for a removal of residual Ss. organic matter, colour, offensive odour and microorganisms to meet the requirement of water re-use. Regarding solid/liquid separation, sedimentation/filtration and flotation/ filtration are common options, and regarding disinfection, chlorine and ozone are among the disinfectants widely applied. For onsite or decentralised wastewater treatment and re-use, systems with compact configuration and ease of control and operation are expected (Lens et al., 2001) Comparing with sedimentation, dissolved or dispersed air flotation is often considered be more suitable for the separation of pollutants with densities similar to or smaller than water. Many studies have shown the advantages of flotation for the treatment of algal rich reservoir stored lowland water(Bauer et aL, 1998), low turbidity surface water (Johnson et aL., 1995), and taste and odour control(Hargesheimer and Watson, 1996). To enhance pollutants removal by flotation, pre-ozonation has been widely used (Yu et aL., 1994 Schmidt et aL., 1995). There have also been practices of ozone-induced flotation for water and wastewater treatment(Betzer et al. 1980: Rashid et al., 1990) Generally speaking, the residual pollutants in the secondary effluent are composed of low concentration suspended solids and organic substances which are less biodegradable and usually cause the problems of colour and offensive odour( Gogate and Pandit, 2004). One idea for effective removal of these pollutants is to seek a combination of coagu- lation, ozonation and flotation in one treatment unit. This leads to the development of a dispersed-ozone flotation(DOF) separator as is introduced in this paper. Materials and methods Dispersed-ozone flotation system Figure I shows the schematic flow chart of the DOF separator for the pilot study at Beishiqiao Wastewater Purification Centre, Xi'an, China. The main body of the DOF doi:10.2166/wst2006.263
A dispersed-ozone flotation (DOF) separator for tertiary wastewater treatment P.K. Jin, X.C. Wang and G. Hu School of Environmental and Municipal Engineering, Xi’an University of Architecture and Technology, No 13 Yanta Road, Xi’an 710055, China (E-mail: pkjin@xauat.edu.cn; xcwang@xauat.edu.cn) Abstract A dispersed-ozone flotation (DOF) separator was devised for a pilot study of tertiary wastewater treatment for re-use purposes. As a compact device combining coagulation, ozonation and flotation in an integrated unit, the DOF separator achieved a very high removal of SS, TOC, UV254 and colour, as well as effective inactivation of coliform and total bacteria within a short hydraulic retention time of 30 min. The finished water quality is comparable to or better than that by a conventional tertiary treatment process using coagulation, sedimentation, filtration and chlorine disinfection, and meets the quality standards for nondrinkable domestic reuse. Keywords Dispersed-ozone flotation; tertiary treatment; water reuse Introduction A typical process for tertiary treatment of the secondary effluent usually consists of coagulation, solid/liquid separation and disinfection units for a removal of residual SS, organic matter, colour, offensive odour and microorganisms to meet the requirement of water re-use. Regarding solid/liquid separation, sedimentation/filtration and flotation/ filtration are common options, and regarding disinfection, chlorine and ozone are among the disinfectants widely applied. For onsite or decentralised wastewater treatment and re-use, systems with compact configuration and ease of control and operation are expected (Lens et al., 2001). Comparing with sedimentation, dissolved or dispersed air flotation is often considered to be more suitable for the separation of pollutants with densities similar to or smaller than water. Many studies have shown the advantages of flotation for the treatment of algal rich reservoir stored lowland water (Bauer et al., 1998), low turbidity surface water (Johnson et al., 1995), and taste and odour control (Hargesheimer and Watson, 1996). To enhance pollutants removal by flotation, pre-ozonation has been widely used (Yu et al., 1994; Schmidt et al., 1995). There have also been practices of ozone-induced flotation for water and wastewater treatment (Betzer et al., 1980; Rashid et al., 1990). Generally speaking, the residual pollutants in the secondary effluent are composed of low concentration suspended solids and organic substances which are less biodegradable and usually cause the problems of colour and offensive odour (Gogate and Pandit, 2004). One idea for effective removal of these pollutants is to seek a combination of coagulation, ozonation and flotation in one treatment unit. This leads to the development of a dispersed-ozone flotation (DOF) separator as is introduced in this paper. Materials and methods Dispersed-ozone flotation system Figure 1 shows the schematic flow chart of the DOF separator for the pilot study at Beishiqiao Wastewater Purification Centre, Xi’an, China. The main body of the DOF Water Science & Technology Vol 53 No 9 pp 151–157 Q IWA Publishing 2006 doi: 10.2166/wst.2006.263 151
买 Scum Discharge ator water Raw water tank Air Pressur stabilizer dispersio Figure 1 Dispersed-ozone flotation system eparator is a closed cylindrical compartment with an inner column at the centre, thus dividing the cylindrical space into a contact zone and a separation zone. On top of the compartment there is an inversely placed circular cone forming a scum chamber. There are two inlets at the bottom of the separator, one as the entrance for the raw water. the secondary effluent, after coagulant(polyaluminium chloride, PAC) dosing and mixing through the raw water pump and online hydraulic mixer, another as the entrance for the return flow mixed with dispersed ozone. The two flows are well mixed hydraulically as they enter the contact zone at its bottom. By the ozone dispersion pump, gaseous ozone from an ozone generator is dispersed in water(return flow from the treated water)as micro bubbles. Therefore, a contact reaction of ozone with pollutants and attachment of pollutants onto micro ozone bubbles occurs at the same time in the contact zone. In the separation zone, floated scum accumulates on the top and treated water is collected through the perforated annular pipe at the bottom. A magnetic valve is installed on the treated water pipe. It is automatically controlled by a time controller so that it can be switched"open"and"closed"at prescribed time intervals. As the valve is opened, treated water flows out of the dOF separator at a regular rate and the water level is kept constant in the separator; as the valve is closed, the treated water flow is shut down and the water level begins to rise in the DOF separator(Figure 2a). In this way, scum accumulated AA JA ated scum through the top outlet of the DOF separator: (a)water es to the outlet;( c) scum being discharged through the outle
separator is a closed cylindrical compartment with an inner column at the centre, thus dividing the cylindrical space into a contact zone and a separation zone. On top of the compartment there is an inversely placed circular cone forming a scum chamber. There are two inlets at the bottom of the separator, one as the entrance for the raw water, i.e. the secondary effluent, after coagulant (polyaluminium chloride, PAC) dosing and mixing through the raw water pump and online hydraulic mixer, another as the entrance for the return flow mixed with dispersed ozone. The two flows are well mixed hydraulically as they enter the contact zone at its bottom. By the ozone dispersion pump, gaseous ozone from an ozone generator is dispersed in water (return flow from the treated water) as micro bubbles. Therefore, a contact reaction of ozone with pollutants and attachment of pollutants onto micro ozone bubbles occurs at the same time in the contact zone. In the separation zone, floated scum accumulates on the top and treated water is collected through the perforated annular pipe at the bottom. A magnetic valve is installed on the treated water pipe. It is automatically controlled by a time controller so that it can be switched “open” and “closed” at prescribed time intervals. As the valve is opened, treated water flows out of the DOF separator at a regular rate and the water level is kept constant in the separator; as the valve is closed, the treated water flow is shut down and the water level begins to rise in the DOF separator (Figure 2a). In this way, scum accumulated on Effluent Con Time Co Raw water tank r Coagulant Pump Ozone Ozone Generator El Magnetic Valve with Time Controller 1 waste water PAC 2 3 4 4 Online mixer Air Pressure stabilizer Contact zone Scum chamber Separation Zone Scum Discharge Ozone dispersion pump DOF Separator Return flow Treated water Figure 1 Dispersed-ozone flotation system (a) (b) (c) Figure 2 Automatic discharge of accumulated scum through the top outlet of the DOF separator: (a) water level rises as the magnetic valve is closed; (b) water level rises to the outlet; (c) scum being discharged through the outlet P.K. Jin et al. 152
the top is driven to the narrow end of the circular cone(Figure 2b) where it finally flows out through the discharge pipe(Figure 2c). As discharge is finished, the valve is switched open again and the next cycle of operation automatically starts. The time interval is set according to the conditions of scum accumulation Table I summarises the standard operational condition of the DOF separator. The ozone dispersion pump drew both a return water flow from the treated water pipe and an air stream from the ozone generator. The air stream was kept constant but ozone concen- tration was adjustable. The micro air bubbles (with an average size of approximately 10 um) were found to be well dispersed throughout the central column(contact zone)of the DOF separator In the separation zone, there was a clear boundary between a upper layer of milky dispersion(water with micro air bubble) and a lower layer of transparent water, indicating a very good condition of air bubble flotation Raw water The raw water for this study is the secondary effluent from the sewage treatment plant Its quality is shown in Table 2, based on the monitoring record during the study Analytical methods Chemical analysis. Chemical analysis in this study was conducted regarding turbidity colour, TOC and UV254 of the raw water and treated water. Methods utilised include the Turbidity: Nephelometic method using a SZD-2 turbidimeter: Colour: platinum-cobalt method using a Hitachi 2000 spectrophotometer at 420 nm; TOC: Catalytic combustion method using a Shimadzu ToC-5050 analyser; UV254: USing a Hitachi 2000 spectrophotometer at 254 nm(cell length I cm) Total bacteria and coliform analysis. Total bacteria and coliform were analysed by membrane filter technique and the results were recorded in terms of colony forming unit (cfu) Results and discussion Pollutants removal by the DOF separator Turbidity removaL. In the raw water, i.e. the secondary effluent, turbidity varied between 2 and 5 NTU. After coagulation, most of the turbid matter was coagulated with organic matter and other pollutants forming micro flocs which were removed by the dOF Table 1 Standard operational condition Parameter Value Raw water flow rate 1 m/hr aseous ozone flow rate HRT in the DOF separator Stabilised air pressure 0.3 MPa Recycle flow rate Table 2 Raw water quality(th Parameter 7.0-7.9 10.8-41.2mg/L Turbidity 4-20NTU 5-35cL. 0.106-0.163cm 30.000 DOC 4.25-9.43mg/L Total coliform 600 cfu/100 mL
the top is driven to the narrow end of the circular cone (Figure 2b) where it finally flows out through the discharge pipe (Figure 2c). As discharge is finished, the valve is switched open again and the next cycle of operation automatically starts. The time interval is set according to the conditions of scum accumulation. Table 1 summarises the standard operational condition of the DOF separator. The ozone dispersion pump drew both a return water flow from the treated water pipe and an air stream from the ozone generator. The air stream was kept constant but ozone concentration was adjustable. The micro air bubbles (with an average size of approximately 10mm) were found to be well dispersed throughout the central column (contact zone) of the DOF separator. In the separation zone, there was a clear boundary between a upper layer of milky dispersion (water with micro air bubble) and a lower layer of transparent water, indicating a very good condition of air bubble flotation. Raw water The raw water for this study is the secondary effluent from the sewage treatment plant. Its quality is shown in Table 2, based on the monitoring record during the study. Analytical methods Chemical analysis. Chemical analysis in this study was conducted regarding turbidity, colour, TOC and UV254 of the raw water and treated water. Methods utilised include the following: † Turbidity: Nephelometic method using a SZD-2 turbidimeter; † Colour: platinum-cobalt method using a Hitachi 2000 spectrophotometer at 420 nm; † TOC: Catalytic combustion method using a Shimadzu TOC-5050 analyser; † UV254: Using a Hitachi 2000 spectrophotometer at 254 nm (cell length 1 cm). Total bacteria and coliform analysis. Total bacteria and coliform were analysed by membrane filter technique and the results were recorded in terms of colony forming unit (cfu). Results and discussion Pollutants removal by the DOF separator Turbidity removal. In the raw water, i.e. the secondary effluent, turbidity varied between 2 and 5 NTU. After coagulation, most of the turbid matter was coagulated with organic matter and other pollutants forming micro flocs which were removed by the DOF Table 1 Standard operational condition Parameter Value Parameter Value Raw water flow rate 1 m3 /hr. Online mixing time 30 s Air and gaseous ozone flow rate 0.2 m3 /h (at 1 atm) HRT in the DOF separator 30 min. Stabilised air pressure 0.3 MPa Recycle flow rate 0.5 m3 /h Table 2 Raw water quality (the secondary effluent) Parameter Analysis Parameter Analysis pH 7.0–7.9 COD 10.8–41.2 mg/L Turbidity 4–20 NTU BOD5 6.0–12.0 mg/L Colour 25–35 c.u. NH3-N 0.7–2.0 mg/L UV254 0.106–0.163 cm21 Total coliform 30,000 cfu/mL DOC 4.25–9.43 mg/L Total coliform 600 cfu/100 mL P.K. Jin et al. 153
separator. As shown in Figure 3, under the standard operational condition specified in Table 1, the residual turbidity in the treated water was below 1.0NTU in the month experimental period(average 3-0. NTU) Colour removal. Figure 4 shows the variation of colour in the raw water and the treated water. It can be seen that the DOF separator performed well in colour removal from the 买 raw water under the above mentioned operational conditions. The average colour in the raw water, i. e. the secondary effuent, was 92.4c.u. in the experimental period, and he average colour in the treated water was 14. 4 c.u. An average colour removal of 84. 49 was achieved Organic removal. Figure 5 shows the treatment results of organic removal (represented by TOC and UV254)by the DOF separator under the operational conditions as mentioned above. The average TOC and UV254 were 11.3 mg/L and 0. 219cm, respectively, resulting in a SUVA(specific UV absorbance) ratio of 0.0194, which is slightly lower than the SUva ratio of organics in natural water (usually with humic substances as the main component) as >0.02(Jin and Wang, 2004), and indicating the characteristics of the secondary effluent. The DOF separator achieved almost identical removals of ToC and UV254(53.5 and 55.7%0, respectively) with the SUVA ratio slightly decreased (SUVA=0.0183). Many studies have shown that one of the important roles ozone plays is to alter the structure of organic matter and result in a decrease of the SUVa ratio (Owen et al, 1995; Goel et al., 1995). The low decrease of SUVa is considered due to 5.0 A Raw water: Average 3.1 NTU z与 Treated water. Average 0.7 NTU Date of sampling (in 200 Figure 3 Turbidity removal by DOF separator Date of sampling(in 2004
separator. As shown in Figure 3, under the standard operational condition specified in Table 1, the residual turbidity in the treated water was below 1.0 NTU in the month experimental period (average 3– 0.7 NTU). Colour removal. Figure 4 shows the variation of colour in the raw water and the treated water. It can be seen that the DOF separator performed well in colour removal from the raw water under the above mentioned operational conditions. The average colour in the raw water, i.e. the secondary effluent, was 92.4 c.u. in the experimental period, and the average colour in the treated water was 14.4 c.u. An average colour removal of 84.4% was achieved. Organic removal. Figure 5 shows the treatment results of organic removal (represented by TOC and UV254) by the DOF separator under the operational conditions as mentioned above. The average TOC and UV254 were 11.3 mg/L and 0.219 cm21 , respectively, resulting in a SUVA (specific UV absorbance) ratio of 0.0194, which is slightly lower than the SUVA ratio of organics in natural water (usually with humic substances as the main component) as .0.02 (Jin and Wang, 2004), and indicating the characteristics of the secondary effluent. The DOF separator achieved almost identical removals of TOC and UV254 (53.5 and 55.7%, respectively) with the SUVA ratio slightly decreased (SUVA = 0.0183). Many studies have shown that one of the important roles ozone plays is to alter the structure of organic matter and result in a decrease of the SUVA ratio (Owen et al., 1995; Goel et al., 1995). The low decrease of SUVA is considered due to 0.0 1.0 2.0 3.0 4.0 5.0 5-Oct 10-Oct 15-Oct 20-Oct 25-Oct 30-Oct 4-Nov 9-Nov 14-Nov 19-Nov 24-Nov 29-Nov 4-Dec 9-Dec 14-Dec 19-Dec 24-Dec Date of sampling (in 2004) Turbidity (NTU) Raw water: Average 3.1 NTU Treated water: Average 0.7 NTU Figure 3 Turbidity removal by DOF separator 0 50 100 150 5-Oct 10-Oct 15-Oct 20-Oct 25-Oct 30-Oct 4-Nov 9-Nov 14-Nov 19-Nov 24-Nov 29-Nov 4-Dec 9-Dec 14-Dec 19-Dec 24-Dec Date of sampling (in 2004) Colour (c. u.) Raw water: Average 92.4 c.u. Treated water: Average 14.4 c.u. Figure 4 Colour removal by DOF separator P.K. Jin et al. 154
15.0 10.0 5.0 Treated water: Average 5.3 mg/L 0.0 U天与 502 Raw water. Average 0.219 cm reated water: Average 0.097 cm 强强 Date of sampling(in 2004) Figure 5 TOC and UV254 removal by DOF separator both the low aromaticity of the raw water and the low ozone dose, 1. 6 mg/L, which may not be enough to decompose organic matter. The organic removal was mainly achieved by coagulation and flotation. Bacteria and coliform inactivation. Figure 6 shows the total bacteria and total coliform counts in the treated water. The dof achieved a 3-log removal of total bacteria and 2.3- log removal of total coliform in comparison with the bacteria counts shown in Table 1 Due to the limitation of ozone supply capacity of the experimental system, investigation could not be conducted for bacteria and coliform removal at an ozone dose higher than 1.6 mg/L. However, the DOF separator showed its advantage in fulfilling simultaneous disinfection and removal of other pollutants, even at an insufficient ozone dose of 1. 6 mg/L Effect of ozone dose. In the DOF separation process, ozone-rich air is the air source for flotation and ozone also plays the function of oxidation. Figure 7 shows the influence of 口 Total bacteria (mL Total colifom《100mL) Sample number Figure 6 Inactivation of microorganisms by dOF separator
both the low aromaticity of the raw water and the low ozone dose, 1.6 mg/L, which may not be enough to decompose organic matter. The organic removal was mainly achieved by coagulation and flotation. Bacteria and coliform inactivation. Figure 6 shows the total bacteria and total coliform counts in the treated water. The DOF achieved a 3-log removal of total bacteria and 2.3- log removal of total coliform in comparison with the bacteria counts shown in Table 1. Due to the limitation of ozone supply capacity of the experimental system, investigation could not be conducted for bacteria and coliform removal at an ozone dose higher than 1.6 mg/L. However, the DOF separator showed its advantage in fulfilling simultaneous disinfection and removal of other pollutants, even at an insufficient ozone dose of 1.6 mg/L. Evaluation of the DOF separation process Effect of ozone dose. In the DOF separation process, ozone-rich air is the air source for flotation and ozone also plays the function of oxidation. Figure 7 shows the influence of 0.0 5.0 10.0 15.0 TOC (mg/L) Raw water: Average 11.3 mg/L Treated water: Average 5.3 mg/L 0.0 0.1 0.2 0.3 5-Oct 10-Oct 15-Oct 20-Oct 25-Oct 30-Oct 4-Nov 9-Nov 14-Nov 19-Nov 24-Nov 29-Nov 4-Dec 9-Dec 14-Dec 19-Dec 24-Dec Date of sampling (in 2004) UV254 (cm–1) Raw water: Average 0.219 cm–1 Treated water: Average 0.097 cm–1 Figure 5 TOC and UV254 removal by DOF separator 0 10 20 30 40 50 12 34 Sample number cfu Total bacteria (/mL) Total coliform (/100mL) Figure 6 Inactivation of microorganisms by DOF separator P.K. Jin et al. 155
DTOC(mg/L) nu(0.01/cm) §50 Turbidity∝0.1NTU a Total bacteria(×1000)口 Colifom(10) 买 10 Ozone dose(mg/L) Figure 7 Effect of ozone dose on treated water quality zone dose on the quality of treated water. With no ozone dose(equivalent to pressured air flotation), the DOF separator could achieve a good removal of turbidity and certain removal of colour, organic matter and bacteria. As the ozone dose increased, the efficiency of colour, organic and bacteria removal was improved. For a further higher removal of coliform bacteria, a higher ozone dose would be needed Treated water quality. Table 3 compares the water quality of the DOF separator and the current conventional treatment process(coagulation sedimentation filtration chlorine disinfection)applied in Beishiqiao Wastewater Purification Centre for tertiary wastewater treatment for re-use. It can be seen that the DOF separator process can achieve the very high water quality. Regarding colour, odour and total bacteria, the treated water quality by the doF separator is better than that by conventional tertiary treatment. The treated water quality meets the Chinese Standard for Domestic Re-use(SAC, 2002). Moreover, the total hrt of the doF separation process is only 30min, in comparison with that for the conventional tertiary treatment 2-3h. High treatment efficiency is one of the important features of the DOF parasol Summary and conclusion This paper introduced a compact device for tertiary wastewater treatment utilising a dispersed ozone flotation technique. The DOF separator combines coagulation, ozonation and dispersed air flotation in one treatment unit within a total hydraulic retention time of approximately only 30 min. The following conclusions can be drawn from the current Table 3 Comparison of the water quality of the treated water between DOF separator and conventional DOF separator Conventional treatment Standard for non-drinkable domestic reus Colour (unit) 5-10 15-30 Slight uncomfortable sell No offensive odour Turbidity(NTU》 5-10 Ss(mg/L) 10-15 BOD(mg/L) 0-20 Coliform(cfu/100 mL) 3 HRT 30 min
zone dose on the quality of treated water. With no ozone dose (equivalent to pressured air flotation), the DOF separator could achieve a good removal of turbidity and certain removal of colour, organic matter and bacteria. As the ozone dose increased, the efficiency of colour, organic and bacteria removal was improved. For a further higher removal of coliform bacteria, a higher ozone dose would be needed. Treated water quality. Table 3 compares the water quality of the DOF separator and the current conventional treatment process (coagulation þ sedimentation þ filtration þ chlorine disinfection) applied in Beishiqiao Wastewater Purification Centre for tertiary wastewater treatment for re-use. It can be seen that the DOF separator process can achieve the very high water quality. Regarding colour, odour and total bacteria, the treated water quality by the DOF separator is better than that by conventional tertiary treatment. The treated water quality meets the Chinese Standard for Domestic Re-use (SAC, 2002). Moreover, the total HRT of the DOF separation process is only 30 min, in comparison with that for the conventional tertiary treatment 2–3 h. High treatment efficiency is one of the important features of the DOF separator. Summary and conclusion This paper introduced a compact device for tertiary wastewater treatment utilising a dispersed ozone flotation technique. The DOF separator combines coagulation, ozonation and dispersed air flotation in one treatment unit within a total hydraulic retention time of approximately only 30 min. The following conclusions can be drawn from the current study: 0 10 20 30 40 50 60 70 Concentration TOC (mg/L) UV (× 0.01/cm) Colour (c.u.) Turbidity (× 0.1 NTU) Total bacteria (× 1000) Coliform (× 10) Raw water 0 0.4 0.8 1.2 1.6 Ozone dose (mg/L) Figure 7 Effect of ozone dose on treated water quality Table 3 Comparison of the water quality of the treated water between DOF separator and conventional process Parameter DOF separator Conventional treatment Standard for non-drinkable domestic reuse Colour (unit) 5–10 15–30 30 Odour None Slight uncomfortable sell No offensive odour Turbidity (NTU) ,0.5 ,0.5 5–10 SS (mg/L) ,10 ,10 10–15 BOD (mg/L) ,10 ,10 10–20 COD (mg/L) ,30 ,30 50–60 Total bacterial(cfu/mL) 25 30 – Coliform (cfu/100 mL) 3 3 5 HRT 30 min 2 – 3 h – P.K. Jin et al. 156
(1) At an ozone dose of 1.6 mg/L with a PAC dose of 50 mg/L, the DOF separator can achieve very good removals of turbidity, colour, organic matter, total bacteria and aliform bacteria from the secondary effluent. The treated water quality is compar able to, or better than, that by a conventional tertiary treatment process and meets the standard for domestic re-use (2) Generation of micro bubbles of ozone-rich air and creation of well dispersed onditions are considered to be the main reason for the high efficiency of disinfed tion and separation in the DOF separator. () With its compact structure, low HRT and high efficiency of pollutant removal, the DOF separator is recommendable to be used as a treatment unit in an onsite or decentralised system for tertiary wastewater treatment and reuse. Acknowledgements This study was supported by the National Natural Science Foundation of China(Grant No.50138020). References Bauer, M. et al. (1998). Enhanced rapid gravity filtration and dissolved air flotation for pre-treatment of river Thames reservoir water. Water Sci. TechnoL., 37(2). 35-42 Betzer, N, Argaman, Y and Kott, Y.(1980). Effluent treatment and algae recovery by ozone-induced flotation. Water Res, 14(8). 1003-1009 Goel, S et al. (1995). Biodegradation of NOM: effect of NOM source and ozone dose. J. AWWA, 87(1) 90-105. Gogate, P.R. and Pandit, A B(2004). A review of imperative technologies for wastewater treatment 1: oxidation technologies at ambient conditions. Adv. Environ. Res, 8. 501-551 Hargesheimer, EE. and Watson. S.B.(1996). Drinking water treatment options for taste and odor control. Warer res,30(6,1423-1430. Jin, P K. and Wang, X C.(2004). Effect of ozonation and hydroxyl peroxide oxidation on the structure of mic acids and their removal. /WA 4th Water Congress, Marrakech. 2004. Johnson, B.A. et aL. (1995). Pilot plant testing of dissolved air flotation for treating Boston,s low-turbidity surface water supply. Water Sci. TechnoL. 31(3-4), 83-92. Lens, P. Zeeman, G and Lettinga, G(2001). Decentralized Sanitation and Reuse- Concepts, Systems and Implementation, IWA Publishing, London, UK. wen, D M. et aL.(1995). NOM characterization and treatability. J AWWA, 87(1). 46-63 Rashid, F, Iqbal, M.S. and Bhatti, MS(1990). Mini ozonizer for instant production of ozone required for oxidation reactions and its application in the foam flotation-separation technique. Anal. Chim. Acta, 238. Schmidt, P D. et aL.(1995). DAF treatment of a reservoir water supply: Comparison with in-line direct filtration and control of organic matter. Water Sci. Technol., 31(3-4). 103-1l Standardization Administration of China(SAC)(2002). Urban Wastewater Reuse: Water Qualiry Standard for Urban Water Consumption(GB/T18920-20 Yu, Q. er al. (1994). The chemistry of ozone conditioning in the selective flotation of macroscopic fossil esin from Utah Wasatch Plateau coal. Coal Prep, 15(1), 35-50
(1) At an ozone dose of 1.6 mg/L with a PAC dose of 50 mg/L, the DOF separator can achieve very good removals of turbidity, colour, organic matter, total bacteria and coliform bacteria from the secondary effluent. The treated water quality is comparable to, or better than, that by a conventional tertiary treatment process and meets the standard for domestic re-use. (2) Generation of micro bubbles of ozone-rich air and creation of well dispersed conditions are considered to be the main reason for the high efficiency of disinfection and separation in the DOF separator. (3) With its compact structure, low HRT and high efficiency of pollutant removal, the DOF separator is recommendable to be used as a treatment unit in an onsite or decentralised system for tertiary wastewater treatment and reuse. Acknowledgements This study was supported by the National Natural Science Foundation of China (Grant No. 50138020). References Bauer, M.J. et al. (1998). Enhanced rapid gravity filtration and dissolved air flotation for pre-treatment of river Thames reservoir water. Water Sci. Technol., 37(2), 35 – 42. Betzer, N., Argaman, Y. and Kott, Y. (1980). Effluent treatment and algae recovery by ozone-induced flotation. Water Res., 14(8), 1003 –1009. Goel, S. et al. (1995). Biodegradation of NOM: effect of NOM source and ozone dose. J. AWWA, 87(1), 90 –105. Gogate, P.R. and Pandit, A.B. (2004). A review of imperative technologies for wastewater treatment I: oxidation technologies at ambient conditions. Adv. Environ. Res., 8, 501 – 551. Hargesheimer, E.E. and Watson, S.B. (1996). Drinking water treatment options for taste and odor control. Water Res., 30(6), 1423– 1430. Jin, P.K. and Wang, X.C. (2004). Effect of ozonation and hydroxyl peroxide oxidation on the structure of humic acids and their removal. IWA 4th Water Congress, Marrakech, 2004. Johnson, B.A. et al. (1995). Pilot plant testing of dissolved air flotation for treating Boston’s low-turbidity surface water supply. Water Sci. Technol., 31(3– 4), 83 – 92. Lens, P., Zeeman, G. and Lettinga, G. (2001). Decentralized Sanitation and Reuse – Concepts, Systems and Implementation, IWA Publishing, London, UK. Owen, D.M. et al. (1995). NOM characterization and treatability. J. AWWA, 87(1), 46 –63. Rashid, F., Iqbal, M.S. and Bhatti, M.S. (1990). Mini ozonizer for instant production of ozone required for oxidation reactions and its application in the foam flotation-separation technique. Anal. Chim. Acta, 238, 427 –430. Schmidt, P.D. et al. (1995). DAF treatment of a reservoir water supply: Comparison with in-line direct filtration and control of organic matter. Water Sci. Technol., 31(3– 4), 103 –111. Standardization Administration of China (SAC) (2002). Urban Wastewater Reuse: Water Quality Standard for Urban Water Consumption (GB/T18920-2002). Yu, Q. et al. (1994). The chemistry of ozone conditioning in the selective flotation of macroscopic fossil resin from Utah Wasatch Plateau coal. Coal Prep, 15(l), 35 –50. P.K. Jin et al. 157