Dairy industry is a major food processing industry. The waste water from dairy industries are mainly produced in the receiving station, starting, stopping and washing any of the processing units, using the processes pasteurization, homogenization of fluid milk and the production of dairy products. It is estimated that dairy industries generate 2.5 to 10L of wastewater per L of milk processed. Major pollutants found in dairy waste water are organic components like dissolved sugars, carbohydrates, proteins and fat, Suspended Solid, Total Dissolved Solid, Sulfur, Phosphorous and Nitrogen. So the dairy wastewater is considered as high concentration of organic matter and high BOD. Disposal of the waste water is a major challenge for dairy industries. As it produced pungent odor it should be treated before disposal to keep environment free from various problems. In this work, the synthetic dairy waste water was prepared and was treated with activated carbon prepared from waste dried coconut shell. The activated carbon prepared from Coconut shell CGAC could be able to remove COD and BOD of the used water up to satisfactory level at different bed height and contact time. This paper shows the removal efficiency of COD and BOD using the activated carbon. In the experiment, the maximum removal efficiency of COD and BOD from the dairy wastewater was found in bed height 10cm with contact time 2hours.
Introduction
I. INTRODUCTION
Industrialization is an essential part for economical growth of country, [1]. Due to industrialization, pollution is the major problem throughout the world. Among various industries, the food industries are one of the highest consumers of water and are one of the biggest producers of effluent. The dairy industry is an example of food industries. India is the largest producer of milk and dairy products in world and ranked first among the milk producing countries. Every year, the growth rate of dairy industry is expected to 4-5%, [2]. In dairy industries, large amount of fresh water is used throughout all the steps of processing starting from milk receiving station to packaging station. It is estimated that dairy industries generate 2.5 to 10 L of wastewater per L of milk processed, [3]. Effluent production and disposal remain a big issue for the dairy industry. Dairy waste water is identified having high COD, BOD due to high organic contents, and TDS, TSS contents, [4]. Hence, Suitable disposal of effluents in wastewater has been a major challenging issue for the dairy industry in India. In this work, the adsorption method is used for removal of the effluent from the dairy waste water, [5].The adsorbent is prepared from solid waste. The solid waste is the coconut shell collected from temple side.
Table 1: Minimum standards maintained for discharge of effluents from the dairy industry
Parameter
Maximum Value (mg/L)
World Bank Report CPCB, India
pH
6-9
6.5-8.5
BOD5
50
100
COD
250
-
TSS
50
150
Oil & Grease
10
10
Total Nitrogen
10
-
Total Phosphorus
2
-
Temperature Increase
< = 30 C
-
Coliform Bacteria
400 Most Probable Number / 100 ml
-
II. MATERIAL AND METHODS
A. Materials
Synthetic dairy waste water Preparation:
The synthetic dairy waste water was prepared by mixing different chemicals in 1L of tap water, [7, 8]. The ratio is given in table 2.
Table 2: Quantity of chemicals added in 1L tap water
Sl No.
Name of Chemicals
Quantity (gm)
1
Milk powder
5
2
glucose
2
3
Sodium Nitrate
1
4
Potassium Phosphate
1
5
Calcium Chloride
1
The synthetic waste water of above composition of 10L was prepared to carry out the experimental work.
2. CGAC Preparation
The granular activated carbon was prepared from solid waste of coconut shell. Coconut shell was collected from temple and was dried for 15 days in sunlight. It was heated in furnace at 4000C for 2hours, [9]. After that, it was allowed to cool, ground and sieved to get a particle size of 1mm.Then it was acid washed using Hydrochloric acid to activate its surface, [10]. Its activated characteristic was checked. Coconut shell-based activated carbons are the less dust, predominantly micro porous. So they are well-suited for organic chemical adsorption. This activated carbon has the highest hardness compared to other types of activated carbons, which makes it the ideal carbon for water purification.
B. Methods
Experimental Set up
The set up was done in the laboratory. The freshly prepared CGAC was used in this experiment. Five different bed heights 2cm, 4cm, 6cm, 8cm and 10cm of adsorbent CGAC maintained in five cylindrical beds of diameter 3cm. Dairy waste water was allowed to flow through the beds from the top. The particle size for CGAC was taken as 2mm.
The contact time was maintained for 30minutes, 60minutes, 90minutes and 120minutes, respectively. The dairy waste water at inlet and water after passing through the bed was collected from different bed height and taken for COD and BOD analysis.
2. Analytical method for COD
The COD test was carried out using a standard procedure. 50ml of samples were carried out in six flasks, out of which one flask having the untreated water and rest five flasks having treated water by CGAC. Potassium dichromate solution was added to each flask with stirring gently. Solutions were heated in water bath at 1000C for 1hour. Then samples were removed and cooled. Then potassium iodide & sulphuric acid were added to samples. The samples were titrated with sodium thiosulphate. The COD values were determined.
3. Analytical method for BOD
The BOD tests were done using BOD bottles and BOD incubator. The samples were taken in six BOD bottles, out of which one bottle was filled with untreated water and rest five bottles with treated water by CGAC. The bottles were kept in the incubator maintaining temperature 200C for 5 days. After 5days, BOD values were observed.
III.. RESULTS AND DISCUSSION
A. Analysis
The initial COD and BOD of the Dairy waste water were obtained as 735.33mg/L and 438.67 mg/L respectively. Experimental results obtained for different bed height of cylindrical beds using freshly prepared CGAC were reported in table 3.
IV. ACKNOWLEDGEMENTS
The authors would like to thank the management of GIET University for their kind support for the novel work. The authors would like to thank HOD and the supportive staffs of Chemical Engineering department for their whole hearten support.
Conclusion
CGAC has the highest hardness compared to other types of activated carbons, which makes it the ideal carbon for water purification.
It is observed from the experiment that by increasing the bed height of adsorbent in the bed and the contact time, the removal efficiency of BOD and COD is gradually increasing. CGAC has the highest hardness compared to other types of activated carbons, which makes it the ideal carbon for water purification.
The experiment can be carried out in continuous manner for industrial application with slight change in the experimental setup.
References
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