Laboratory of biofuels
Contact: Timo Kikas Tel.: +372 731 3163 e-mail: timo.kikas@emu.ee
Address: Chair of Biosystems Engineering Institute of Forestry and Engineering
Estonian University of Life Sciences56 Fr. R. Kreutzwald Str. 51006 Tartu, ESTONIA |
Our People:
Timo Kikas, PhD Chair Professor, Biosystems Engineering |
Merlin Raud, PhD
Researcher, Bioenergy and Biofuels |
Lisandra Meneses, PhD
Senior Researcher |
Tharaka Rama Krishna Chowdary Doddapaneni, PhD
Marie Curie Research Fellow |
Sabarathinam Shanmugam, PhD |
Renu Geetha Bai, PhD |
Vahur Rooni, PhD |
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Lara Podkuiko, MSc Doctoral student |
Margareta Novian Cahyanti, MSc Doctoral Student, Junior Research Fellow |
Nikki Sjulander, MSc Doctoral student, Junior Research Fellow |
Sharib Khan, MSc Doctoral Student, Junior Research Fellow |
Salini Chandrasekharan Nair, MSc Doctoral Student, Junior Research Fellow |
Anjana Hari, MSc Doctoral Student, |
Damaris Okafor, MSc Doctoral student |
Kaie Ritslaid, BSc (science) Lecturer/Analyst |
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Main Research Fields:
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Reсent Publications: (last 5 years) Rocha-Meneses, Lisandra; Zannerni, Rawan; Inayat, Abrar; Abdallah, Mohamed; Shanableh, Abdallah; Ghenai, Chaouki; Kamil, Mohammed; Kikas, Timo (2022). Current progress in anaerobic digestion reactors and parameters optimization. Biomass Conversion and Biorefinery. DOI: 10.1007/s13399-021-02224-z. Raud, M.; Krennhuber, K.; Jäger, A.; Kikas, T. (2019). Nitrogen explosive decompression pre-treatment: an alternative to steam explosion. Energy, 177, 175−182.10.1016/j.energy.2019.04.071.
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In order to prepare specialists in the field of bioenergy and biofuels who have knowledge and experience in the topics of biofuel production, technology involved, regulations, standards and analysis, we are offering following lectures: TE.0940 Industrial processes and machines in bioenergetics, |
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Analytical Capability In the Biofuels laboratory we are able to perform following analysis: |
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Density measurements with petroleum density meter; hydrometric method Standard Test Method for Density, Relative Density (Specific Gravity), or API Gravity of Crude Petroleum and Liquid Petroleum Products by Hydrometer Method. EN ISO 3675; ASTM D1298 Density measurements with digital density meter Analysis of Active Sulphur Species Analysis of Fractional composition |
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Measurements of Kinematic viscosity Standard Test Method for Kinematic Viscosity of Transparent and Opaque Liquids (and the Calculation of Dynamic Viscosity). EN ISO 3104; ASTMD 445. Measurements of Vapour Pressure Standard Test Method for Vapour Pressure of Petroleum. EN 13016-1; EN 13016-2; ASTM D5191. Measurements of Vapour Lock Index, VLI (VLI=10VP+7E70) Vapour Lock Index VLI (VLI = 10VP + 7E70) Products (Mini Method). EVS-EN 228:2002. Arvutuslik metoodika. Measurements of Existent Gum in Fuels Standard Test Method for Existent Gum in Fuels by Jet Evaporation. EN ISO 6246; ASTMD 381. Measurements of Corrosion Standard Method for Detection of Copper Corrosion from Petroleum Products by the Copper Strip Tarnish Test.; EN ISO 2160; ASTMD 130. |
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Measurements of Water and Particulates Standard method for Free Water and Partiulate Contamination in Distillate Fuels (Fuels Inspection Procedures). ASTMD1319. Measurements of Cetane Index Standard Test Method for Calculated Cetane Index by Four Variable Equation. EN ISO 4264; ASTMD 4737. Measurements of Cetane Index of distillate fuels. Standard Test Method for Calculated Cetane Index of Distillate Fuels. (Fuels Inspection Procedures). ASTMD 4176. |
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Measurements of Flash Point. Cleveland Open cuvette Standard Test Method for Flash and Fire Points by Cleveland Open Cu. EN 22592; ASTMD 92. Measurements of Flash Point. Pensky-Martens method Standard Test Method for Flash Point by Pensky-Martens Closed Tester*. EN ISO 2719; ASTM D93. Measruements of carbon residue Standard Test Method for Conradson Carbon Residue of Gasolineeum Products (on 10% distillation), Micro Method. EN ISO 10370; ASTM D4530. |
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Analysis of Acid and Base number. Titration Standard Test Method for Acid and Base Number and pH by Color-Indicator Titration. EN ISO 6618; ASTM D974. Determination of water Coulometric Karl Fischer titration method EN ISO 12937; ASTM D4928. Determination of water Volumetric Karl Fischer titration method ASTM D4377. Determination of contamination in middle distillates. EN 12662; ASTM D4807. |
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Determination of Carbon Residue by Conradson Determination of carbon residue – Conradson method. ASTM D189; EN ISO 6615. Determination of Water and Sediment Standard Method of Test for Water and Sediment in Fuel Oil and Crude Oil by Centrifuge Method. ISO 3734. ASTM D1796. Determination of Water Standard Method of Test for Water in Petroleum Products, and Bituminous Materials by Distillation. ISO 3733; ASTM D 95. |
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Determination of Water Standard Method of Test for Water in Petroleum Products, and Bituminous Materials by Distillation. ISO 3733; ASTM D 95. Water Reaction (Water Reaction Interface; Water Reaction separation). Metoodika ASTM D 1094- Water Reaction of Aviation Fuels. Determination of water soluble acids and bases Standard Test Method for Acidity of Hydrocarbon Liquids and their Distillation Residues. ASTM D1093. |
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Calculation of Viscosity Index Standard Practice for Calculating Viscosity Index From Kinematic viscosity at 100 °C and at 4°oC. ISO 2909; ASTM D2270. |
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Determination of acid value of FAME’s Oil and fat derivates.Fatty Acid Methyl Esters(FAME). Determination acid value. EVS-EN 14104. Determination of iodine value of FAME’s Oil and fat derivates.Fatty Acid Methyl Esters(FAME). Determination iodine value. EVS EN 14111. Fibre analysis Fibre analysis from biomass (Crude Fiber, ADF and NDF determinations). Measurements of glucose and ethanol content in liquids Determination of glucose and ethanol concentration with Analox GL6 device. |
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Determination of structural sugars from the biomass Determination of Structural Carbohydrates and Lignin in Biomass by HPLC – NREL/TP-510-42618. |
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Intellectual Property: 1. Double walled cylindrical rotating photobioreactor with inner light source (link) |
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Double walled cylindrical rotating biophotoreactor with inner light source, that includes closed vessel, which is formed by two horizontal double walled cylinders on the common rotational axes with a potential to rotate, outer and inner walls, endplates, and the fixed section that joins both rotating cylinders and is filled with microalgal solution. In the middle of the double walled cylinders inner light source is placed. The excess heat produced by the light source is dissipated using ventilator. Turning the light source on and off the switching mechanism is used. To the upper part of the fixed section the outtake of residual gases and input of nutrient solution with filters and valves are fixed. To the lower part of the fixed section the outtake of excess biomass and input of carbon dioxide (CO2) and/or air with filters and valves are fixed. The open ends of rotating cylinders are furnished with seals that make contact with the sliding surfaces of the fixed section. The closed ends are furnished with rolling-braces that prevent axial displacement. | |
2. Nitrogen explosion pretreatment method for disruption of biomass structure (link) |
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The invention belongs to the field of instrumentation for production of non-fossil biofuels, more specifically instrumentation for production of bioethanol, biobuthanol and biodiesel and is applicable in biofuel production process from lignocellulosic biomass. In nitrogen explosion method for disrupting cell structure, dry milled biomass is mixed with water to achieve creamy consistency (biomass to water ration from 1:5 to 1:15), pressure is increased using nitrogen gas (N2) to a range of 10 to 60 bars, temperature in the pressure vessel is raised to a range of 125 to 190 degrees of Celsius and is kept thus for the incubation period of 10 to 120 minutes. The mixture is then cooled to a temperature range of 25 to 90 degrees of Celsius, while the total time of biomass heating, incubation and cooling is in the range of 1 to 4 hours. After reaching the final temperature, the pressure is suddenly released to achieve explosive decompression and the pretreated biomass is used in further processing. | |
3. Integrated flow-through apparatus for ethanol production from lignocellulosic biomass (link) |
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The invention falls in the category of non-fossil fuel production technology, bioethanol production in particular, and is applicable in the production of bioethanol from lignocellulosic biomass. Integrated flow-through apparatus for ethanol production from lignocellulosic biomass contains of interconnected pre-treatment, hydrolysis, fermentation, and distillation units. The pre-treatment, hydrolysis, and distillation units are incorporated into a single integrated reactor, where pre-treatment and hydrolysis units are made of two-levelled coil of tubing that is wound around the distillation unit. The tube size in both levels is different and the reactor has a heat exchange system. The pre-treatment unit is placed in the inner part of the two-levelled tubing and the hydrolysis unit in the outer part. The tube size decreases from inner part to outer. Different parts of the tubing are immersed in the heat carrier and separated from each other by insulating walls. The fermentation unit of the apparatus is an upright container that includes an upright winding channel. The inlet of the channel is at the bottom and outlet at the top of the container. Apparatus is furnished with sensors and a control panel to control the processes in the apparatus. |