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IRJET- Experimental Investigation of Biodiesel (Caster-RICINUS COMMUNIS) using Variable Compression CI Engine
1.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 6977 Experimental Investigation of Biodiesel (Caster-RICINUS COMMUNIS) using Variable Compression CI Engine Nitin H. Umale1, Prof. P. B. Ingle2, Prof. V. Gore3 1M.Tech student, Mechanical Engineering, P. R Pote College of Engineering, Amravati, India. 2Assistant Professor, Department of Mechanical Engineering P. R Pote College of Engineering, Amravati, India. 3Assistant Professor, Department of Mechanical Engineering P. R Pote College of Engineering, Amravati, India. ---------------------------------------------------------------------***---------------------------------------------------------------------- Abstract – In order to meet the energy requirements ,there has been growing interest in alternative fuels like vegetable oils, biodiesels, biogas, LPG, CNG to provide asuitablediesel oil substitute for internal combustion (IC) engine. Vegetable oils, because of their agricultural origin, may be due to less carbon content compared to mineral diesels are producing less CO2 emissions to the atmosphere. It also reduces import of petroleum products. In these experimental studyiscarried out on an IC engine laboratorysinglecylinder, four-strokevariable compression ratio (VCR), direct injection diesel engine to analyze the performance and emission characteristics of pure diesel and waste cooking oil (WCO) – diesel blended fuels with various blended rate. Experiments have been carried out to estimate the performance, emission and combustion characteristics of a single cylinder, four-stroke VCR multi fuel engine fuelled with biodiesel land its blends with standard diesel. Key Words: Biodiesel, Diesel Engine, Emission, HC, CO NOx, Performance 1. INTRODUCTION To meet the growing energy needs resulting from spiralling demand and diminishing supply, alternative energy sources “mostly biofuels” are receiving more attention. In addition, the increasing global concern has caused to focus on the oxygenated diesel fuels because of the environmental pollution from internal combustion engines. These issues have triggeredvariousresearchstudiestoreplacepetroleum- based diesel fuel with the biofuel. 1.1 Methodology In Methodology weare dealing with theactualworkingof our project there are two main working process in our project these are as follow 1. Biodiesel production 2. Trail on Engine Why CASTOR? Caster (RICINUS COMMUNIS) is in very abundant form and it can be easily found in our area . Castordoesnotrequire any special atmosphere and irrigation land. India is a largest producer of castor in the world and its production rate is 3 times in ayaer as compare to other resources. In this seed oil contents is about 50% of the total weight . Biodieselobtained from castor has a very low cloud and pour point which make this biodiesel a goodalternativeinwinterconditionCastoroil biodiesel could be used as petroleum diesel additive for improving both environmental and flow behavior of the mineral fuel 1.2 Biodiesel Production Experimentation First Process under the methodology section is of biodiesel production consist of following three process 1. Pre Process ( Heating of oil and esterification) 2. Main Process (Transesterification ) 3. Post Pocess ( water wash) 4. Biodiesel Blending 1.3 Extraction of oil The castor oil was extracted by using a sorbet About 500ml of hexane was poured in a round bottom flask and 100g of ground castor beans was packed in a filter paper placed in the thimble and fixed with a round bottom flask which was connected with a condenser the fitted apparatus then heated in a heating mantle to biol the solvent . Whenthe solvent boiled the vapour rose through the vertical tube into condenser to the top and the vapor condensed dripped into the thimble in the center the extractor seeped through the pore of the thimble and filled siphon tube where it flowed back down into the round bottom flask . The extraction prolonged to eight hours after which the resulting mixturein the round bottom flask was concentrated in rotator evaporator to recover the solvent from the extracted oil.The weight of the extracted oil was recorded . The crude oil was refined by degumming , neutralization and bleaching process . In degumming process the crude oil was treated with hot water to remove gums , hydrates, FFA and soap . Finally it was bleached with activated clay to remove colour odour impurities and residual soap. 1.4 Transesterification Process (Main Process) Is a reaction of an alcohol with an Easter to form different types of alcohols and ester in the presence or absence of a
2.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 6978 catalyst . in the production of biodiesel vegetable oil is in the form of triglyceride which reacts with a small chain alcohol ( methanol ethanol propanol and so on) in the presence of homogeneous catalyst such as base (KOH Naoh CH3OH (CH3O)2Ca CaO ) or acid (HCL H2sO4 H3PO4) or heterogeneous catalyst as zeolites or biocatalyst as enzymes hence the process is also known as alcoholysis for methonal methanolysis and for ethanol ethanolysis . The esters that formed in methonolysis are called as fatty acid methyl estera(FAMEs) and esters that formed in ethnolysis are fatty acid ethyl ester (FAEEs) about 25 ml of oil was kept in three necked round bottom flask and heated to 65C (thisisthePre- Process) then calculated amount of methanol and catalyst (KOH or H2sO4) were added with stirring system. The experiment prolonged for three hours Chemical Reaction which govern this process is given as 1.5 Seperation And Purification Of Biodiesel After the completionofthereaction,theproductwasallowed to cool and equilibrate which resulted in separating of two phases . the upper phase consisted of methyl esterwithsmall amount of impurities such as residual alcohol glycerol and partial glyceridewhilethelowerphasecontainedtheglycerol with other material ( excess methanol catalyst soap formed during reaction and some entrained esters and partial glycerides)The upper layer was methyl ester ( Biodiesel ) while the lower layer was glycerol the obtained methyl ester was purified by successive rinse with 2.5% (w/w)sulphuric acid and distilled water . To avoid emulsion during washing process NaCl solution was used . Then the washed methyl ester was treatedwithanhydroussodiumsulphatetoremove excess water . It was then filtered and dried by heating atlow temperature ( 60) for 30min 1.6 Biodiesel Blending In biodiesel blending the castor biodiesel ( B100) is blended with the Diesel (B00) at 40 c and kept it for homogenization for 20min with agitation upto 300 rpm after this kept the solution upto 2 hours and we get the biodiesel blend (B 5 , B10, B 15, B20 etc) B5 means 5% of pure biodiesel with the 95% of Diesel . For solution of 1 litre of B5 we have to Blend 50ml of pure biodiesel with 950 ml of Diesel 2. TRAIL ON ENGINE The setup consists of single cylinder, four stroke, VCR (Variable Compression Ratio) Diesel engine connected to eddy current type dynamometer for loading. The compression ratio can be changed without stopping the engine and without altering the combustion chamber geometry by specially designed tilting cylinder block arrangement. Setup is provided with necessary instruments for combustion pressure and crank-angle measurements. These signals are interfaced to computer through engine interfacing airflow, fuel flow, temperatures and load measurement. The set up has stand-alone panel box consisting of air box, two fuel tanks for duel fuel test, manometer, fuel measuring unit, transmittersforairandfuel flow measurements, process indicator and engine indicator. Rotameters are provided for cooling water and calorimeter water flow measurement. The setup enables study of VCR engine performance for brake power, indicated power, frictional power, BMEP, IMEP, brake thermal efficiency, indicated thermal efficiency, Mechanical efficiency, volumetric efficiency, specific fuel consumption, A/F ratio and heat balance. Lab view based Engine Performance Analysis software package “EnginesoftLV”isprovidedforon line performance evaluation.AcomputerizedDieselinjection pressure measurement is optionally provided. Fig -1: Schematic arrangement Basic technical specification of the test engine Product VCR Engine test setup 1 cylinder, 4 stroke, Diesel (Computerized) Engine Make Kirloskar, Type 1 cylinder, 4 stroke Diesel, water cooled, power 3.5 kW at 1500 rpm, stroke 110 mm, bore 87.5 mm. 661 cc, CR 17.5, Modified to VCR engine CR range 12 to 18bria / 10 pt Dynamometer Type eddy current, water cooled, with loading unit Propeller shaft With universal joints Air box M S fabricated with orifice meter
3.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 6979 and manometer Fuel tank Capacity 15 lit with glass fuel metering column Calorimeter Type Pipe in pipe Piezo sensor Range 5000 PSI, with low noise cable Crank angle sensor Resolution 1 Deg, Speed 5500 RPM with TDC pulse. Data acquisition device NI USB-6210, 16-bit, 250kS/s. Piezo powering unit Make-Cuadra, Model AX-409. Digital millivolt meter Range 0-200mV, panel mounted Temperature sensor Type RTD, PT100 and Thermocouple, Type K Temperature transmitter Type two wire, Input RTD PT100, Range 0–100 Deg C, Output 4–20 mA and Type twowire, Input Thermocouple, Range 0–1200 Deg C, Output 4–20 mA Load indicator Digital, Range 0-50 Kg, Supply 230VAC Load sensor Load cell, type strain gauge, range 0-50 Kg Fuel flow transmitter DP transmitter, Range 0-500 mm WC Air flow transmitter Pressure transmitter, Range (-) 250 mm WC Software “Engine soft LV” Engine performance analysis software Rotameter Engine cooling 40-400 LPH; Calorimeter 25-250 LPH Pump Type Monoblock Overall dimensions W 2000 x D 2500 x H 1500 mm Optional Computerized Diesel injection pressure measurement Table -1: Basic technical specification of the test engine 3. PERFORMANCE OF CASTOR BIODIESEL BLENDS IN DIESEL ENGINE:- 3.1 For Compression Ratio 16.5 Chart -1 : Load Vs Break Power Chart -2: Load vs BSFC Chart -3: Load vs Break Thermal Eff
4.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 6980 Chart -4 : Load Vs Vol eff (%) 3.2 For Compression Ratio 17.5 Chart -1 : Load Vs Break Power Chart -2: Load vs BSFC Chart -3: Load vs Break Thermal Eff Chart -4 : Load Vs Vol eff (%) 4. EMISSION CHARACTERISTICS:- 4.1 For Compression Ratio 16.5 Chart -1 : Load Vs NOx Concentration (ppm)
5.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 05 | May 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.211 | ISO 9001:2008 Certified Journal | Page 6981 Chart -2 : Load Vs HC Concentration (ppm) Chart -3 : Load Vs CO Concentration (ppm) 4.2 For Compression Ratio 17.5 Chart -1 : Load Vs NOx Concentration (ppm) Chart -2 : Load Vs HC Concentration (ppm) Chart -3 : Load Vs CO Concentration (ppm) 5. CONCLUSIONS Biodiesel obtained by Castor oil has good inherent properties and most of its properties resembles to that of diesel. The performanceof biodiesel canbefurtherimproved by blending 1. When B20 castor biodiesel Blend used in engine at CR 16.5 has Lower BSFC than the B10 castor Biodiesel Blends but has higher Break thermal eff. And lower CO, HC emission and comparatively higher NOX emission but it can be controlled by several methods 2. When B10 castor biodiesel Blend used in engine at CR 17.5 has Lower BSFC than the B20 castor Biodiesel Blends but has higher Break thermal eff. And lower NOX, and comparatively higher CO , HC emission but it can be controlled by several methods REFERENCES [1] Aydin H, BayindirH.Performanceand emissionanalysis of cottonseed oil methyl ester in a diesel engine. Renew Energ 2010;35:588–92.
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International Research Journal
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