Waste Cooked Oil as an Alternative Feed Stock for Bio-Diesel Production in Indian Railways.
Arvind Lal1, A. Kumar2, A.K. Gupta3 and N.K. Yadav4.
1Indian Railways Institute of Mechanical and Electrical Engineering, (IRIMEE) Jamalpur. Bihar - 811214
2 Department of Mechanical Engineering, BIT,Mesra Ranchi. Jharkhand
3 University Department of Chemistry, L. N. M. University, Darbhanga, Bihar
4 P. G. Department of Chemistry, T. M. Bhagalpur University, Bhagalpur, Bihar
*Corresponding Author E-mail: lalarvind2@gmail.com
ABSTRACT:
Knowing the enormous potentialities of bio-diesels, Indian Railways has taken up challenge to produce it from plantation of Bio-fuel plants (Jatropha) on a large scale in the vast vacant lands throughout the country including the track sides, and decided to run its Diesel locomotives, road vehicles and even generator sets on it to minimise the air pollution extent in the IR premises. But due to non-availability of regular feedstock (Non-edible oils), it is difficult to continue the same. In this work ,bio-diesel was prepared through the transesterification from waste cooked oils(WCO), collected from Star hotels in and around new Delhi and from the canteen of Queen’s Road Hostel, E. Railway Jamalpur. Methyl alcohol with KOH as a catalyst was used for the process. The best result was found at the temperature of 650C with a reaction time of 1 hour. The biodiesel was characterized by its physical and fuel properties including viscosity, flash point, carbon residue, water and sediments content according to ASTM Standards and found to be comparable as per IS: 15607/05.Production of biodiesel from waste cooked oils for the diesel substitute is particularly important because of the decreasing trend of the economical oil reserves, environmental problems caused due to fossil fuel use and the high price of petroleum products in the international markets.
KEYWORDS: IR (Indian Railways), HSD oil (High speed diesel), waste cooked oil (WCO), Transesterification, free fatty acid (FFA) etc.
1. INTRODUCTION:
IR (Indian Railways) has one of the largest and busiest rail networks in the world, transporting over 18 million passengers and more than 2 million tonnes of freight daily[1]. Traditionally, IR has been accorded priority for supply of energy for traction purpose. But due to power cuts, IR has an adverse effect on the overall performance of the entire system. So, IR has taken a decision to adopt alternative source of energy (BIO-DIESEL) to meet its fuel requirements as well as to overcome the air pollution problems. Biodiesel fuel has become more attractive because of its environmental benefits [2], due to the fact that plants and vegetable oils are renewable biomass source.
Compared to petroleum diesel, biodiesel has lower emission of pollutants, it is biodegradable and enhance the engine lubricity and contributes to sustainability[3,4] Biodiesel has a higher cetane number than diesel fuel, no aromatics, no sulphur, and contains 10-11% oxygen by weight[5]. Hence a considerable work has been done by Indian Railways at Research Design and Standards Organization (RDSO) and IRIMEE to assess the suitability of Bio-diesel for the Indian Railways application as an alternative to power the Diesel locomotives as well as road vehicles.[6]. The price of edible plant and vegetable oils is usually higher than petrodiesel. The use of waste cooked oil as biodiesel feed stock in Indian Railways reduces the cost of biodiesel production, since the feedstock cost constitutes approximately 70-95% of the overall cost of the biodiesel production[7]. Hence, the use of waste cooked oils and non-edible oils should be given higher priority over the other oils as biodiesel feedstock.
The objective of the paper is both to develop self-sufficiency as well as to develop an energy source that is non-polluting, environment friendly and cost effective. The properties of Biodiesel are very similar to those of existing diesel (HSD oils IS: 1460/2005) and it can be blended in various proportion to the diesel.
1.1 Potential of waste cooked oil as a feed stock for bio-diesel source.
Huge quantities of waste cooked oil (WCO) and animal fats are available throughout the world, especially in the developed countries as pointed out by Arjun B. Chhetri[8,9] as mentioned in the table No-1. Though some of this waste oil is used for the soap industry, but large amounts of waste cooked oils are illegally dumped into rivers and landfills, causing environmental pollution. Hence the use of WCO to produce biodiesel offers a significant advantage, due to the reduction in environmental pollution. Klass[10] along other researchers pointed out that HSD oil is also the major source of the emission of NOx, SOx, CO, particulate matters and volatile organic compounds (VOCs).Emission of such pollutants not only has negative impacts on the global environment but also has severe impacts on human health due to their persistence in the environment. Hence WCO, which is otherwise wasted, would be one of the most economical choices to produce biodiesel.
1.2 HSD oil consumption and uses of biodiesel in IR.
Approximately two billion liters of diesel fuel are consumed annually by the 4,000 freight and passenger locomotives in the Indian railway fleet. The prime mover in all but a few of these locomotives is the medium-speed diesel engine, having power levels ranging up to 4000 horsepower. The expenditure of Indian Railways on diesel fuel is Rs 4400 crores. Diesel fuel is approximately 18 percent of railways’ total operating expenses.[11]. A blend of B20 (20% biodiesel and 80% petro diesel) has been found most suitable to IR and climatic conditions. A B20 blends equates to an overall annual railway market potential of 400 million liters of neat biodiesel.[11]. By the year, IR has planted more than 12 millions of Jatropha plants on the vacant lands especially along the track sides and the figures are increasing by leaps and bounds. Already 4 (four) esterification plants for manufacturing of Biodiesel have been set up in different locations and some more are in pipeline [11]. But due to shortage of these feed stocks, waste vegetable or cooked oil has taken as a feedstock for making bio-diesel in IR application.
2. MATERIALS AND METHODS:
2.1 MATERIALS AND OPTIMISATION OF BIODIESEL PRODUCTION FROM WCO.
Waste Vegetable oil or cooked oil is collected from the star hotels in and around Delhi and stored at Sakurbasti Diesel shed as a feedstock, in the Nothern Railway applications. Some used cooked oils are also collected from the canteen of Queens Road hostel of Eastern Railways, Jamalpur (Bihar) for the experiment.
It is well recognized that the waste cooked oil is a result of the frying temperature, length of the use as well as the material used for the frying. The oil used for the cooking was not single oil but mostly refined soybeans and other blended ones. The used oil sample was taken from the frying potatoes, fish, chickens and other vegetable based food items. Before going to the actual transesterification, the oil was first conditioned to remove sediments and moisture etc. The oil sample was heated in a beaker to 1100C to evaporate off the water and after cooling, was filtered using a cloth (75 micron) to separate any particles. The percentage of free fatty acid (FFA) was then measured from titration method. (N/10NaOH solution using phenophthein as indicator) and accordingly, the next steps were taken.[12] If the FFA is less than 4 to 5, single step process is sufficient but if it is more than 5 (Five) then acid treatment process is to be done to reduce it below Four (4).In this case FFA was found to be less than four hence ,single step process was used. From the titration, the total amount of catalyst per liter of waste cooked oil was determined to be 14 grams of KOH per liter of waste cooked oil. This amount was confirmed to be correct by actual experiments.
First of all a mixture of 180 ml of methanol and 14 gram of KOH (both L.R grade from MERCK) was prepared and it was then poured into 1 liter of oil placed in the reaction vessel. The oil was kept in a thermostat at 65±5°C with a stirring of 250-300 rpm. On addition of the alcohol and base mixture the stirring was increased to around 600 rpm, for 20 to 30 minutes for getting better collision of reactants.
The reaction mixture was then allowed to settle in a separating funnel for about 12 hours. When the two phases of glycerol and Biodiesel became clearly distinct, they were separated out.
The upper phase of Bio-diesel was washed 3 to 4 times with distilled water to remove excess of unreacted oil, catalyst and methanol until it become completely translucent and was finally dried at 100±10°C in oven to remove the water or moisture.
The best result with more yield ( 90%) and minimum time ( 1 hour) was obtained with oil: alcohol: KOH ratio of 1 liter: 180.43 ml: 14 gram as mention in table no-2. The so recovered biodiesel was then subjected to various tests as mention in table - 3 at Diesel Shed Laboratory, Eastern Railways as per IS: 1460/05 or IS: 15607 for comparison.
Table No-1.Feedstock of waste cooking oil
|
Sl. No |
Country |
Availability |
|
1 |
USA |
100millions gallons/day |
|
2 |
Canada |
135,000tons/year. |
|
3 |
E.U. |
700,000-1,000,000 tons/year |
|
4. |
U.K |
200,000 tons/year. |
|
5 |
India |
Figure not available. |
Table No-2 Optimized parameters for biodiesel production.
|
Sl. No. |
Parameters affecting Reactions Single stage process. |
Waste cooked oil ( WCO) |
|
1 |
Esterification |
Alkaline |
|
2 |
Alcohal used |
Methanol |
|
3 |
Alcohal to oil molar ratio |
6:1 |
|
4. |
Catalyst used |
Potassium hydroxide ( KOH) |
|
5 |
Catalyst amount % |
14g/liter of MeOH |
|
6 |
Reaction temperature0C |
65 |
|
7 |
Reaction time minutes. |
60 |
|
8 |
Stirring speed rpm |
600 ( both clock wise and anti clock wise) |
|
9. |
Settling time hours |
12 |
|
10 |
Methyl ester wash |
Distilled water till clear. |
Table No-3 Comparision of properties of biodiesel with diesel fuel.
|
Properties and Units. |
IS: 15607/05 specification. |
HSD oil (High speed diesel) IS: 1460/05 |
Waste Cooked oil biodiesel (WCOBD) |
Test methods. |
|
Density@150C g/cm3 |
0.87-0.90 |
0.850 |
0.885 |
IS: 1448 |
|
Kinematic Viscosity @400C cst |
2.5-6.0 |
2.0-5.0 |
5.80 |
ASTM D 445 |
|
Flash point 0C (PMCC) Min |
120 |
350C by Abel apparatus |
162 |
ASTM D 93 |
|
Carbon residue % wt |
0.05 Max |
0.015 Max |
0.140 |
ASTM D 4530 |
|
Calorific value MJ/Kg |
---- |
44.0 |
38.6 |
Bomb calorimeter |
|
Cetane value min |
51 |
52 |
53 |
ASTM D 613 |
|
Moisture content, (mg/kg) max |
0.05% |
---- |
nil |
ASTM D 2709 Karl fisher Titrator |
|
Acid Value Mg KOH/g Max |
0.5 |
<1 |
0.35 |
ASTM D 974 |
|
Ester content % Mass min |
96.5 |
---- |
90 |
EN 14110 GC method. |
2.2 BIO-DIESEL PROCESSING UNITS AND TRANSESTERIFICATION REACTION:-
One pilot plant of capacity 5(five) litre made of glass having three separators, reaction vessel, alcohol recovery and auto temperature controlling device was set up at IRIMEE, Jamalpur. More than 20 batches of biodiesel (3.5 Litre) were made and it was used in IRIMEE generator as B10 without any adverse effect.
Biodiesel, fatty acid of methyl esters used, is obtained by the alkali- catalyzed transesterification reaction of the waste or cooked vegetable oils with alcohols.

Where, R’, R’’ and R’’’ are the different types of fatty acid chains associated with the oil which are largely palmitic, stearic, oleic and linoleic acids ( from 16 to 18 carbon chain). For shifting the equilibrium to the right side the molar concentration ratios of alcohol: oil is kept more than 3:1.
3. RESULTS AND DISCUSSION:
3.1 Fuel characterization:
The sample was tested to determine the fuel characteristics according to ASTM biodiesel fuel quality assurance standard test. Table -3 shows the summary of the test method used, the standard limit as recommended by IS: 15607/05.
(1) Though the Biodiesel are to be tested for impurities associated with it coming through the transestrification process, yet no sedimentation no. water content and clear appearance and other physical properties mentioned in the chart coming within the prescribed limit tell much about their purity.
(2) Biodiesel and its blends are susceptible to growing microbes when water is present in them. The solvency property of Biodiesel can cause microbial slime to detach and clog fuel filters. In our findings all the Biodiesel are completely free from water content.
(3) The yield of Biodiesel obtained in this method is about 90%. The least yield from waste cooked oil indicates a higher percentage of FFA in the oil and a percentage of it going under saponification.
(4) The acid value can be used to guide in quality control of fuels. Acid value of WCO Biodiesel as obtained was found well within the standard of 0.5, which shows that FFA coming from the mother oil is minimum and would not come in the way of performance of IC Engine.
(5) The viscosity of liquid is an important characteristic as it determines the ease of flow through pipeline, injector nozzle and orifices and formation of fuel in the cylinder. The kinematic viscosity of Biodiesel and its blends were within the prescribed standard limit.
(6) Specific gravity specification is needed in India to check for any contamination or adulteration. It was found within the prescribed limit for all the case.
(7) Flash point measures the tendency of the sample to form a flammability mixture with air and as per Indian standard it must be of minimum 120°C. In this case, this point was 162oC which is not only beyond the prescribed limit and above the HSD but it will also be easier for storage for their less inflammability.
(8) Carbon residue of the fuel is indicative of carbon depositing tendency of fuel. In case of Biodiesel, it shows a high correlation with presence of free fatty acids, glycerides, soaps, polymers, higher unsaturated fatty acids and inorganic impurities. Carbon residue for WCO biodiesel was found higher than the prescribed limit. It shows the presence of any of the above mentioned substances.
9. The calorific value of WCO biodiesel was found to be 38.60 MJ/kg and is less than the calorific value of diesel (44.0 MJ/kg) but greater than that of pure oil. As the percentage of bio-diesel in the blends increased, the calorific value decreased.
(10) Rinsed water of Biodiesel may be utilized as irrigation purposes for plants after treatment of water as per norms of Central Pollution control Board (CPCB). (BOD 6.6 mg/l, TDS-453mg/l, pH 9.3).
4. CONCLUSION:
From the results and discussions it can safely be said that waste cooked oil can be an important source for biodiesel production. WCO biodiesel and its blends may prove suitable for Indian Railways application as there is large quantity of waste cooked oil available. The star hotels supply these oil free of cost to Indian Railways specially at sakurbasti diesel shed to maintain its own reputation and at the same time it also helps to improve the biodiesel economics in Indian railways.
5. ACKNOWLEDGEMENT:
The author would like to acknowledge Director, IRIMEE to grant for conducting research at IRIMEE, Jamalpur and also thankful to Incharge of Diesel shed Laboratory, Eastern Railway Jamalpur for providing test reports in due time.
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