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EFFECT OF ORGANIC LOADING RATE ON DAIRY WASTEWATER USING ANAEROBIC BIO-FILM REACTOR

M.S. Sivakumar* and B. Asha

Depatrment of Civil Engineering, Annamalai University, Annamalai Nagar 608 002, T.N., India India

*Corresponding Author:
M.S. Sivakumar
Depatrment of Civil Engineering, Annamalai University, Annamalai Nagar 608 002, T.N., India India
E-mail: siva.ms75@yahoo.in

Received: 24 August 2011 Accepted: 15 November 2011

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Abstract

A short term solution for the treatment of dairy wastewater is discussed with an average COD values of 3620, 4060, 4300, 4570 and 5200mg/L with varying OLR of 0.1502, 0.1706, 0.1798, 0.1912, 0.2166 and kg COD/m3/day. The performance of model was evaluated in terms of % COD removal and biogas conversion.

Keywords

Organic Loading Rate, Hydraulic Retention Time, Chemically Oxidation Demand, Biogas, Bio film

Introduction

India is a large producer of milk and dairy product in the world with annual milk production crossing 85 million tones in the year 2002 and growing at the rate of 2.8% per annum (Ramasamy et al., 2004). The dairy wastewater consists of high organic matters, mainly Lactose, fat and protein. The enriched nutrients in cheese whey have created a suitable environment for Lactobacillus species to convert organic sources into methane via anaerobic process. Anaerobic treatment process is an ideal technique for the bioconversion of dairy wastewater into biogas. In this study, anaerobic bio film reactor, which is a time-tested proven technology to remove COD up to 84% for dairy wastewater is evaluated with an experimental model for the performance and detailed experiment study was conducted.

In this anaerobic treatment process no require-ments for aeration, low amount of excess sludge production and low area demand are the additional advantages of anaerobic treatment process (Deminel et al., 2005). Dairy Industries produce wastewater with a high Organic Loading Rate fluctuation resulting by seasonal products and products variations such as Yogart, Ice cream, milk, cheese whey and other relevant products (Healy et al., 2007; Broushton et al., 2007).

The methods of handling, treating and disposing of the farm wastes may adversely affect air, water and soil condition, and may be a nuisance to those who dwell nearby (Coker et al., 2001). Large scale dairy production system generates great quantities of wastewater.

Materials and Methods

The experimental setup consist of an anaerobic biofilm reactor having effective volume of 13 liters. The physical features and process parameters are presented in Table 1 . The schematic of the experimental set up is shown in the Figure 1.

icontrolpollution-Physical-features

Table 1. Physical features and process parameters experimental models:

icontrolpollution-anaerobic-bio

Fig. 1 Experimental setup for an anaerobic bio film reactor

The experiment was commissioned using domestic wastewater collected from the sewage treatment facility of our university. The reactor was acclimatized and attained a steady state condition after 90 days with an average COD removal of 66% to 84%.

The samples were collected from M/S. Aavin chilling plant Ltd., Villupuram, Tamil Nadu and analyzed for critical parameters. The characteristics of the parameters and their values are presented in Table 2.

icontrolpollution-Dairy-wastewater

Table 2. Characteristics of Dairy wastewater

icontrolpollution-Gas-Generation

Fig. 2 OLR Vs Gas Generation

The wastewater was introduced initially in the reactor with an overall average OLR of 0.1816 KgCOD/ m3/d and in stages mixed with domestic wastewater in proportion of 20%, 40%, 60% and 100%. The process stabilization and acclimatization was attained with an average COD reduction of 76% after 30 days.

After attained the steady state condition the experiment was run continuously for different combinations of influent COD of 3620, 4060, 4300, 4570 and 5200 (mg/L). The operating conditions are interpreted for the parameters of Organic Loading Rates (OLR), 0.1502, 0.1706, 0.1798, 0.1912, 0.2166, kg COD/m3/d and Hydraulic Retention Times (HRT) of 72, 36, 24, 18, 14.4 hrs.

Result and Discussion

Figure 1 shows five different concentration of dairy wastewater was investigated. The maximum removal of COD attain at 84% for 0.0726, kg COD/m3/d OLR. Figure 2 shows the biogas collection from the reactor was found in the range from 0.016 to 0.048 of gas / kg COD removed.

Conclusion

The present investigation reveals that the biogas production and % of COD removal efficiency of dairy wastewater using an anaerobic bio-film reactor as a noval film anaerobic bio reactor with high performance for handling the high organic load was successfully achieved. The reactor was very efficient in the treatment of diluted high strength dairy wastewater at a maximum COD removal efficiency of 84% with an OLR of 0.0726 kg COD m3/d.

The maximum yield of biogas production was achieved at influent COD 4500mg/L with OLR of 0.0623kg COD/m3/d.

Acknowledgement

The authors are thankful to the authorities of Annamalai University for having provided the Laboratory facilities.

References

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