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    Solar energy, since it is available every day, is seen as one of the most valuable renewable energy resources. Thus, the energy of sun should be efficiently used in various applications. The most known applications that use solar energy are heating water and spaces. High efficiency solar collectors need appropriate selective surfaces to absorb the heat. Selective surfaces (Selektif-Sera) used in this study are applied to flat collectors, which are produced by a roll to roll cost effective coating of nano nickel layers, developed in Selektif Teknoloji Co. Inc. Efficiency of flat collectors using Selektif-Sera absorbers are calculated in collaboration with Institute for Solar Technik Rapperswil, Switzerland. The main cause of high energy consumption in industry is mostly caused from low temperature level processes. There is considerable effort in research to minimize the energy use by renewable energy sources such as solar energy. A feasibility study will be presented to obtain the potential of solar thermal energy utilization in the textile industry using these solar collectors. For the feasibility calculations presented in this study, textile dyeing and finishing factory located at Kahramanmaras is selected since the geographic location was an important factor. Kahramanmaras is located in the south east part of Turkey thus has a great potential to have solar illumination much longer. It was observed that, the collector area is limited by the available area in the factory, thus a hybrid heating generating system (lignite/solar thermal) was preferred in the calculations of this study to be more realistic. During the feasibility work, the calculations took into account the preheating process, where well waters heated from 15 °C to 30-40 °C by using the hot waters in heat exchangers. Then the preheated water was heated again by high efficiency solar collectors. Economic comparison between the lignite use and solar thermal collector use was provided to determine the optimal system that can be used efficiently. The optimum design of solar thermal systems was studied depending on the optimum collector area. It was found that the solar thermal system is more economic and efficient than the merely lignite use. Return on investment time is calculated as 5.15 years. {"references": ["http://www.aee-intec.at/0uploads/dateien561.pdf, Accessed on 18/05/2016.", "http://www.solarthermalworld.org/sites/gstec/files/SoPro_Leaflet_en.pdfAccessed on 18/05/2016.", "Kalogirou S. \"The potential of solar industrial process heat applications\", Applied Energy, 2003, vol. 76, no. 4, pp. 337-361.", "S Mekhilef, R Saidur, A Safari, \"A review on solar energy use in industries\", Renewable and Sustainable Energy, 2011, vol. 15, no. 4 pp. 1777-1790.", "Taibi, E, Gielen D, Bazilian M. \"Measuring energy poverty: Focusing on what matters\", Renewable and Sustainable Energy, 2012, vol.16, no.1, pp. 735-744", "Faninger, G., \"The potential of Solar Heat in the future energy system\", IFF-University of Klagenfurt, Austria; www.uni-klu.ac.at/iff/ikn/downloads/Potential_of_Solar_Heat.pdf, Accessed on 18/05/2016", "Vannoni, C., Battisti, R., Drigo, S., Potential for Solar Heat in Industrial Processes, Task 33, 2008. Solar Cooling and Heating Committee of the International Energy Agency (IEA).", "TMMOB Mechanical Engineering Chamber Report, \"T\u00fcrkiye'nin Enerji G\u00f6r\u00fcn\u00fcm\u00fc\", 2012, pp. 1588", "Kad\u0131rgan F., Roll to roll manufacturing of solar selective sheets, PCT patent, PCT/IB2010/055006, WO/2012/059789 \n[10]\thttp://www.estif.org/fileadmin/estif/content/policies/downloads/D23-solar-industrial-process-heat.pdf, Accessed on 20/05/2016"]}

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  • Authors: M. de Wild-Scholten; V. Cassagne; T. Huld;

    The 2011 world average carbon footprint of PV system manufacturing is estimated as 1798 kg CO2- eq/kWp using technology shares (multi, mono, film Si, CdTe, CIGS) as weighting factors. The electricity mixes of all production countries of poly-Si, wafer, cell and modules was taken into account. New yearly irradiation data (kWh/m2) and PV energy output (kWh/kWp) are calculated for different regions in Europe on NUTS level 1 and 2 for horizontal, optimum and vertical angle. The world average carbon footprint of PV electricity generation is estimated as 55 g CO2- eq/kWh with cumulative installations as weighting factors. Lowest value of 38 g CO2-eq/kWh is for Cyprus which has a high irradiation and the highest value of 89 g CO2-eq/kWh is for Iceland which has a low irradiation. It is assumed that the PV modules are installed at optimal angle to the sun and end-of-life treatment is excluded. The majority of countries can decrease the greenhouse gas emission of electricity generation by increasing the share of photovoltaics. 29th European Photovoltaic Solar Energy Conference and Exhibition; 3421-3430

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    Authors: A. Mathieu; B. Aubry; E. Chhim; M. Jobe; +1 Authors

    {"references": ["T Gopinathan, K P Arul Shri: Simulation of Recharging Battery of the\nPacemaker using Piezoelectric Crystal from the Pulse in Aorta, Thesis,\nDec 2011.", "H.W. Ko: US Patent 3456134A: Piezoelectric Energy Converter for\nElectronic Implants, 1969.", "A. Badel: R\u00e9cup\u00e9ration d'Energie et Contr\u00f4le Vibratoire par El\u00e9ments\nPi\u00e9zo\u00e9lectriques Suivant une Approche Non Lin\u00e9aire, Ph.D. Thesis,\nUniversit\u00e9 de Savoie, 2008.", "M. Deterre: Toward an Energy Harvester for Leadless Pacemakers,\nPh.D. Thesis, Paris-Sud Univ. 2013.", "N. Andrew: Redington,CardiacDept, Brompton Hospital, Fulham Road,\nLondon SW3 6HP, in press.", "R. White, G. Savage, M. Zdeblick: US Patent 7729768 B2: Implantable\nCardiac Motion Powered Piezoelectric Energy Source.", "S. Priya, D.J. Inman: Energy Harvesting Technologies.", "N. Bassiri-Gharb : Piezoelectric Mems: Materials and Devices,\nPiezoelectric and Acoustic Materials for Transducer Applications, A.\nSafari, E.K. Akdogan, eds., Springer US, 2008, pp. 413\u2013430.", "W. Clark, C. Mo : Energy Harvesting Technologies, Ch.16, pp.405-430,\nS. Priya, D.J. Inman eds., Springer, 2009.\n[10] M. Deterre, E. Lefeuvre, E. Dufour-Gergam : An Active Piezoelectric\nEnergy Extraction Method for Pressure Energy Harvesting, Smart\nMaterials and Structures, Vol.21(8), 085004, 2012.\n[11] M.A. Karami, D.J. Inman: Powering Pacemakers from Heartbeat\nVibrations Using Linear and Nonlinear Energy Harvesters, Appl. Phys.\nLett. 100, 042901 (2012), in press.\n[12] S.R Anton, H.A Sodano : A Review of Power Harvesting Using\nPiezoelectric Materials (2003\u20132006), Smart Materials and Structures,\nVol.16(3), R1, 2007."]} Present project consists in a study and a development of piezoelectric devices for supplying power to new generation pacemakers. They are miniaturized leadless implants without battery placed directly in right ventricle. Amongst different acceptable energy sources in cardiac environment, we choose the solution of a device based on conversion of the energy produced by pressure variation inside the heart into electrical energy. The proposed energy harvesters can meet the power requirements of pacemakers, and can be a good solution to solve the problem of regular surgical operation. With further development, proposed device should provide enough energy to allow pacemakers autonomy, and could be good candidate for next pacemaker generation.

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    Authors: Stephan Silvestre; Octavio Escobar; Ulises Neri;

    The concept of energy transition can be interpreted in different ways depending on the nature of the agent involved. However, practitioners and existing literature agree that a country’s energy transition is the variation of fossil fuel share in the total primary energy supply (TPES). Public policies mostly focus on changing the energy mix directly or indirectly. However, the production of fossil fuels depends mostly on market-related determinants, including prices and investment in the means of production. But what is the contribution of global energy transition? The objective of this paper is to estimate to which extent public policies related to energy transition affect fossil fuel production in producing countries. For this purpose, we consider as a proxy of energy transition the evolution over 40 years of the TPES of a large panel of fossil fuel–exporting countries, which we compare to its total primary energy production (TPEP). Moreover, we analyze these effects to determine if they differ according to country characteristics, such as its level of development or its membership in OPEC. Finally, we describe the long-run and short-run effects by studying separately the effects of production investments and those of R&D investments in RES technologies. The European Journal of Comparative Economics, Vol 17. no. 1, p. 5-30

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  • Authors: Robert Scharler; Ingwald Obernberger; Claudia Benesch; Christoph Mandl;

    This paper presents experimental results derived from test runs performed with a laboratory-scale updraft fixed-bed gasifier coupled to a combustion chamber to produce data for the investigation of the release behaviour and the conversion of fuel-bound nitrogen during gasification and subsequent staged combustion of the producer gas using softwood pellets. The concentrations of relevant nitrogenous gas species including tars have been measured in the producer gas and at different positions in the combustion chamber. Based on the experimental measurements and results derived from the test runs, the pathway of the fuel-bound nitrogen could be described. Results show that during updraft fixed-bed gasification the fuel-bound nitrogen is mainly released as N bound in tars from the packed bed and is then subsequently released as HCN, NO, NH3 and N2 as a result of tar cracking during combustion. This strong N-fixation in the tars was not expected. It is of great relevance for the understanding of the behaviour of the fuel-bound nitrogen as a basis for a low-NOx combustion of the producer gas. Proceedings of the 19th European Biomass Conference and Exhibition, 6-10 June 2011, Berlin, Germany, pp. 996-1001

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  • Authors: T. Willner; A. Sievers; E. Baldauf;

    A high pressure/high temperature reactor was used in semi­continuous mode for hydroprocessing of Cracked Vegetable Oil (CVO). Therefore, hydrogen with a partial pressure of 50 bar was conveyed continuously through the pilot plant. The reaction temperature was 350 °C. This temperature was hold for 3 h in each experiment. CVO was provided in the reactor for treatment with a molybdenum catalyst with traces of heavy metals in a ratio of 1 wt.­% corresponding to the mass of CVO in the reactor at the beginning of the test. Deoxygenation (DO) reactions were found in all experiments and Hydrogenated Cracked Vegetable Oil (HCVO) was obtained. Acid number and calorific value measurement as well as selectively gas chromatography/mass spectrometry (GCMS) was performed for proving DO. CVO used in this study was made from rapeseed oil. The aim of the project is the transfer of those findings to CVO which is based on used frying oil. Conventional raw materials suffer on a lack of sustainability and high cost. CVO removes these drawbacks and provides a high quality product with high energy density at the same time. Proceedings of the 22nd European Biomass Conference and Exhibition, 23-26 June 2014, Hamburg, Germany, pp. 1034-1037

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    {"references": ["Ministry of energy and mineral resources. Annual Report 2007.\nAmman", "W Durisch , J Keller , W Bulgheroni , LKeller , H Fricker, Solar\nirradiation measurements in Jordan and comparisons with California\nand Alpine data, Applied Energy, 52(2-3),1995,111-124.", "O Badran, Study in industrial applications of solar energy and the range\nof its utilization in Jordan. Renewable Energy, 24(3-4), 2001, 485-90.", "E Hrayshat , M Al-Soud, Potentials of solar energy development for\nwater pumping in Jordan. Renew Energy 29, 2004,1393-1399.", "Jordan Meteorological Department: Jordan Annual Climate Bulletin,\nJMD, Amman, Jordan, 2000.", "Jordan Meteorological Department: Jordan Annual Climate Bulletin,\nJMD, Amman, Jordan, 1999.", "Duffie and Beckman, Solar Engineering of Thermal Processes, 2nd\nedition, Wiley and Sons, Toronto."]} The purpose of this work is to present the potential of solar energy in Zarqa region. The solar radiation along year 2009 was obtained from Pyranometer which measures the global radiation over horizontal surfaces. Solar data in several different forms, over period of 5 minutes, hour-by-hour, daily and monthly data radiation have been presented. Briefly, the yearly global solar radiation in Zarqa is 7297.5 MJ/m2 (2027 kWh/m²) and the average annual solar radiation per day is 20 MJ/m2 (5.5 Kwh/m2). More specifically, the average annual solar radiation per day is 12.9 MJ/m2 (3.57 Kwh/m2) in winter and 25 MJ/m2 (7 Kwh/m2) in summer.

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    Authors: Er.T.B.Shaikh; Er.A.B.Kolekar; Er.N.N.Shinde;

    Globally it is estimated that 84% of produced grains are wasted. In India 20-40% of food grains are spoiled, due to conventional preservation technique. The preservation tech like canning, freezing, drying etc are used in order to avoid the food wastage. Renewable hybrid drying system may be optimum for food preservations at low cost and will exploit at large in the present scenario. Proposed system of hybrid drying system is an integration of solar thermal air heating system coupled with air heating using suitable heating system based on biomass burning to maintain continuous drying process. Experiments are carried out for sun drying, oven drying, solar drying using air heaters and solar- biomass thermal drying. It is observed that solar hybrid system using biomass as a fuel for heating has reduced time of drying maize. For only solar system hot air drying time reduced from 72 to 33 hours and for solar hybrid drying time reduced from 72 to 15 hours. https://journalnx.com/journal-article/20150072

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  • Authors: Hermann Hofbauer; Friedrich Kirnbauer; Matthias Kuba; F. Havlik;

    An innovative process to produce synthesis gas from a solid feedstock is dual fluidbed (DFB) steam gasification of biomass. The principle of this technology is the separation of the fluidized bed into a gasification and a combustion zone. Bed material, nowadays olivine, is circulating, between them, which has two functions. Firstly, it acts as heat carrier from the combustion to the gasification zone. Secondly, it has the role of a catalyst regarding the reduction of hydrocarbons. In this work, the catalytic activity of different fresh and also used bed materials, such as olivine and silica sand was tested regarding their ability to enhance the water-gas-shift reaction and also reduce hydrocarbons. Calcite is known as active material in this respect and, therefore, used as reference substance. Experiments showed a correlation between the enhancement of the water-gas-shift reaction and the reduction of lighter and heavier hydrocarbons by steam reforming. Results show that as long as a bed material particle has built up a calcium-rich layer, satisfying conversion of carbon monoxide and the hydrocarbons can be achieved. As model substances for hydrocarbons ethane and toluene were used. These results are the basis for further research of catalytic characteristics of potential bed materials for the dual fluidized bed steam gasification of biomass. Proceedings of the 23rd European Biomass Conference and Exhibition, 1-4 June 2015, Vienna, Austria, pp. 562-567

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    Authors: Wenyuan Ye; Jiuyang Lin; Luis, Patricia; Bruggen, Bart Van Der;

    {"references": ["", "M. Meinshausen, N. Meinshausen, W. Hare, S. C. B. Raper, K. Frieler, R.\nKnutti, D. J. Frame, M. R. Allen, \"Greenhouse-gas Emission Targets for\nLimiting Global Warming to 2\u00b0C\" Nature J., vol. 458, pp. 1158-1162,\n2009.", "P. Luis, T. Van Gerven, and B. Van der Bruggen, \"Recent Developments\nin Membrane-based Technologies for CO2 Capture\" Prog. Energy\nCombust. Sci. J., vol. 38, pp. 419-448, 2012.", "W. Ye, J. Lin, J. Shen, P. Luis, B. Van der Bruggen, \"Membrane\nCrystallization of Sodium Carbonate for Carbon Dioxide Recovery:\nEffect of Impurities on the Crystal Morphology\" Cryst. Growth Des.J.,\nvol. 13, pp. 2362\u20132372, 2013.", "P. Luis, D Van Aubel, B Van der Bruggen, \"Technical viability and\nexergy analysis of membrane crystallization: Closing the loop of CO2\nsequestration\" Int. J. Greenh. Gas Con. J., vol. 12, pp. 450-459, 2013.", "T. Ring, \"Kinetic effects on particle morphology and size distribution\nduring batch precipitation\" Powder Technol. J., vol. 65, pp. 195-206,\n1991.", "M. A. Bialik, H. Theliander, P. Sedin, C. L. Verrill, N. DeMartini,\n\" Solubility and solid-phase composition in Na2CO3-Na2SO4 solutions at\nboiling temperature: A modeling approach\" Ind. Eng. Chem. Res. J., vol.\n47, pp. 3233-3238, 2008.", "D. Weckesser, A. K\u00f6nig, \"Particle shape and purity in membrane based\ncrystallization\" Chem. Eng. Technol. J. vol. 31, pp. 157-162, 2008.", "B. Shi, W. J. Frederick Jr., R. W. Rousseau, \"Nucleation, growth, and\ncomposition of crystals obtained from solutions of Na2CO3 and Na2SO4\"\nInd. Eng. Chem. Res. J., vol. 42, pp. 6343-6347, 2003.", "A. P. Soemardji, C. L. Verrill, W. J. Jr. Frederick, H. Theliander,\n\"Prediction of Crystal Species Transition in Aqueous Solutions of\nNa2CO3 and Na2SO4 and Kraft Black Liquor\" Tappi J. vol. 3, pp. 27-32 ,\n2004."]} This study addresses the effect of impurities on the crystallization of Na2CO3 produced within a strategy for capturing CO2 from flue gases by alkaline absorption. A novel technology - membrane assisted crystallization - is proposed for Na2CO3 crystallization from mother liquors containing impurities. High purity of Na2CO3•10H2O crystals was obtained without impacting the performance of the mass transfer of water vapor through membranes during crystallization.

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    Solar energy, since it is available every day, is seen as one of the most valuable renewable energy resources. Thus, the energy of sun should be efficiently used in various applications. The most known applications that use solar energy are heating water and spaces. High efficiency solar collectors need appropriate selective surfaces to absorb the heat. Selective surfaces (Selektif-Sera) used in this study are applied to flat collectors, which are produced by a roll to roll cost effective coating of nano nickel layers, developed in Selektif Teknoloji Co. Inc. Efficiency of flat collectors using Selektif-Sera absorbers are calculated in collaboration with Institute for Solar Technik Rapperswil, Switzerland. The main cause of high energy consumption in industry is mostly caused from low temperature level processes. There is considerable effort in research to minimize the energy use by renewable energy sources such as solar energy. A feasibility study will be presented to obtain the potential of solar thermal energy utilization in the textile industry using these solar collectors. For the feasibility calculations presented in this study, textile dyeing and finishing factory located at Kahramanmaras is selected since the geographic location was an important factor. Kahramanmaras is located in the south east part of Turkey thus has a great potential to have solar illumination much longer. It was observed that, the collector area is limited by the available area in the factory, thus a hybrid heating generating system (lignite/solar thermal) was preferred in the calculations of this study to be more realistic. During the feasibility work, the calculations took into account the preheating process, where well waters heated from 15 °C to 30-40 °C by using the hot waters in heat exchangers. Then the preheated water was heated again by high efficiency solar collectors. Economic comparison between the lignite use and solar thermal collector use was provided to determine the optimal system that can be used efficiently. The optimum design of solar thermal systems was studied depending on the optimum collector area. It was found that the solar thermal system is more economic and efficient than the merely lignite use. Return on investment time is calculated as 5.15 years. {"references": ["http://www.aee-intec.at/0uploads/dateien561.pdf, Accessed on 18/05/2016.", "http://www.solarthermalworld.org/sites/gstec/files/SoPro_Leaflet_en.pdfAccessed on 18/05/2016.", "Kalogirou S. \"The potential of solar industrial process heat applications\", Applied Energy, 2003, vol. 76, no. 4, pp. 337-361.", "S Mekhilef, R Saidur, A Safari, \"A review on solar energy use in industries\", Renewable and Sustainable Energy, 2011, vol. 15, no. 4 pp. 1777-1790.", "Taibi, E, Gielen D, Bazilian M. \"Measuring energy poverty: Focusing on what matters\", Renewable and Sustainable Energy, 2012, vol.16, no.1, pp. 735-744", "Faninger, G., \"The potential of Solar Heat in the future energy system\", IFF-University of Klagenfurt, Austria; www.uni-klu.ac.at/iff/ikn/downloads/Potential_of_Solar_Heat.pdf, Accessed on 18/05/2016", "Vannoni, C., Battisti, R., Drigo, S., Potential for Solar Heat in Industrial Processes, Task 33, 2008. Solar Cooling and Heating Committee of the International Energy Agency (IEA).", "TMMOB Mechanical Engineering Chamber Report, \"T\u00fcrkiye'nin Enerji G\u00f6r\u00fcn\u00fcm\u00fc\", 2012, pp. 1588", "Kad\u0131rgan F., Roll to roll manufacturing of solar selective sheets, PCT patent, PCT/IB2010/055006, WO/2012/059789 \n[10]\thttp://www.estif.org/fileadmin/estif/content/policies/downloads/D23-solar-industrial-process-heat.pdf, Accessed on 20/05/2016"]}

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  • Authors: M. de Wild-Scholten; V. Cassagne; T. Huld;

    The 2011 world average carbon footprint of PV system manufacturing is estimated as 1798 kg CO2- eq/kWp using technology shares (multi, mono, film Si, CdTe, CIGS) as weighting factors. The electricity mixes of all production countries of poly-Si, wafer, cell and modules was taken into account. New yearly irradiation data (kWh/m2) and PV energy output (kWh/kWp) are calculated for different regions in Europe on NUTS level 1 and 2 for horizontal, optimum and vertical angle. The world average carbon footprint of PV electricity generation is estimated as 55 g CO2- eq/kWh with cumulative installations as weighting factors. Lowest value of 38 g CO2-eq/kWh is for Cyprus which has a high irradiation and the highest value of 89 g CO2-eq/kWh is for Iceland which has a low irradiation. It is assumed that the PV modules are installed at optimal angle to the sun and end-of-life treatment is excluded. The majority of countries can decrease the greenhouse gas emission of electricity generation by increasing the share of photovoltaics. 29th European Photovoltaic Solar Energy Conference and Exhibition; 3421-3430

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    Authors: A. Mathieu; B. Aubry; E. Chhim; M. Jobe; +1 Authors

    {"references": ["T Gopinathan, K P Arul Shri: Simulation of Recharging Battery of the\nPacemaker using Piezoelectric Crystal from the Pulse in Aorta, Thesis,\nDec 2011.", "H.W. Ko: US Patent 3456134A: Piezoelectric Energy Converter for\nElectronic Implants, 1969.", "A. Badel: R\u00e9cup\u00e9ration d'Energie et Contr\u00f4le Vibratoire par El\u00e9ments\nPi\u00e9zo\u00e9lectriques Suivant une Approche Non Lin\u00e9aire, Ph.D. Thesis,\nUniversit\u00e9 de Savoie, 2008.", "M. Deterre: Toward an Energy Harvester for Leadless Pacemakers,\nPh.D. Thesis, Paris-Sud Univ. 2013.", "N. Andrew: Redington,CardiacDept, Brompton Hospital, Fulham Road,\nLondon SW3 6HP, in press.", "R. White, G. Savage, M. Zdeblick: US Patent 7729768 B2: Implantable\nCardiac Motion Powered Piezoelectric Energy Source.", "S. Priya, D.J. Inman: Energy Harvesting Technologies.", "N. Bassiri-Gharb : Piezoelectric Mems: Materials and Devices,\nPiezoelectric and Acoustic Materials for Transducer Applications, A.\nSafari, E.K. Akdogan, eds., Springer US, 2008, pp. 413\u2013430.", "W. Clark, C. Mo : Energy Harvesting Technologies, Ch.16, pp.405-430,\nS. Priya, D.J. Inman eds., Springer, 2009.\n[10] M. Deterre, E. Lefeuvre, E. Dufour-Gergam : An Active Piezoelectric\nEnergy Extraction Method for Pressure Energy Harvesting, Smart\nMaterials and Structures, Vol.21(8), 085004, 2012.\n[11] M.A. Karami, D.J. Inman: Powering Pacemakers from Heartbeat\nVibrations Using Linear and Nonlinear Energy Harvesters, Appl. Phys.\nLett. 100, 042901 (2012), in press.\n[12] S.R Anton, H.A Sodano : A Review of Power Harvesting Using\nPiezoelectric Materials (2003\u20132006), Smart Materials and Structures,\nVol.16(3), R1, 2007."]} Present project consists in a study and a development of piezoelectric devices for supplying power to new generation pacemakers. They are miniaturized leadless implants without battery placed directly in right ventricle. Amongst different acceptable energy sources in cardiac environment, we choose the solution of a device based on conversion of the energy produced by pressure variation inside the heart into electrical energy. The proposed energy harvesters can meet the power requirements of pacemakers, and can be a good solution to solve the problem of regular surgical operation. With further development, proposed device should provide enough energy to allow pacemakers autonomy, and could be good candidate for next pacemaker generation.

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    Authors: Stephan Silvestre; Octavio Escobar; Ulises Neri;

    The concept of energy transition can be interpreted in different ways depending on the nature of the agent involved. However, practitioners and existing literature agree that a country’s energy transition is the variation of fossil fuel share in the total primary energy supply (TPES). Public policies mostly focus on changing the energy mix directly or indirectly. However, the production of fossil fuels depends mostly on market-related determinants, including prices and investment in the means of production. But what is the contribution of global energy transition? The objective of this paper is to estimate to which extent public policies related to energy transition affect fossil fuel production in producing countries. For this purpose, we consider as a proxy of energy transition the evolution over 40 years of the TPES of a large panel of fossil fuel–exporting countries, which we compare to its total primary energy production (TPEP). Moreover, we analyze these effects to determine if they differ according to country characteristics, such as its level of development or its membership in OPEC. Finally, we describe the long-run and short-run effects by studying separately the effects of production investments and those of R&D investments in RES technologies. The European Journal of Comparative Economics, Vol 17. no. 1, p. 5-30

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  • Authors: Robert Scharler; Ingwald Obernberger; Claudia Benesch; Christoph Mandl;

    This paper presents experimental results derived from test runs performed with a laboratory-scale updraft fixed-bed gasifier coupled to a combustion chamber to produce data for the investigation of the release behaviour and the conversion of fuel-bound nitrogen during gasification and subsequent staged combustion of the producer gas using softwood pellets. The concentrations of relevant nitrogenous gas species including tars have been measured in the producer gas and at different positions in the combustion chamber. Based on the experimental measurements and results derived from the test runs, the pathway of the fuel-bound nitrogen could be described. Results show that during updraft fixed-bed gasification the fuel-bound nitrogen is mainly released as N bound in tars from the packed bed and is then subsequently released as HCN, NO, NH3 and N2 as a result of tar cracking during combustion. This strong N-fixation in the tars was not expected. It is of great relevance for the understanding of the behaviour of the fuel-bound nitrogen as a basis for a low-NOx combustion of the producer gas. Proceedings of the 19th European Biomass Conference and Exhibition, 6-10 June 2011, Berlin, Germany, pp. 996-1001

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  • Authors: T. Willner; A. Sievers; E. Baldauf;

    A high pressure/high temperature reactor was used in semi­continuous mode for hydroprocessing of Cracked Vegetable Oil (CVO). Therefore, hydrogen with a partial pressure of 50 bar was conveyed continuously through the pilot plant. The reaction temperature was 350 °C. This temperature was hold for 3 h in each experiment. CVO was provided in the reactor for treatment with a molybdenum catalyst with traces of heavy metals in a ratio of 1 wt.­% corresponding to the mass of CVO in the reactor at the beginning of the test. Deoxygenation (DO) reactions were found in all experiments and Hydrogenated Cracked Vegetable Oil (HCVO) was obtained. Acid number and calorific value measurement as well as selectively gas chromatography/mass spectrometry (GCMS) was performed for proving DO. CVO used in this study was made from rapeseed oil. The aim of the project is the transfer of those findings to CVO which is based on used frying oil. Conventional raw materials suffer on a lack of sustainability and high cost. CVO removes these drawbacks and provides a high quality product with high energy density at the same time. Proceedings of the 22nd European Biomass Conference and Exhibition, 23-26 June 2014, Hamburg, Germany, pp. 1034-1037

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    {"references": ["Ministry of energy and mineral resources. Annual Report 2007.\nAmman", "W Durisch , J Keller , W Bulgheroni , LKeller , H Fricker, Solar\nirradiation measurements in Jordan and comparisons with California\nand Alpine data, Applied Energy, 52(2-3),1995,111-124.", "O Badran, Study in industrial applications of solar energy and the range\nof its utilization in Jordan. Renewable Energy, 24(3-4), 2001, 485-90.", "E Hrayshat , M Al-Soud, Potentials of solar energy development for\nwater pumping in Jordan. Renew Energy 29, 2004,1393-1399.", "Jordan Meteorological Department: Jordan Annual Climate Bulletin,\nJMD, Amman, Jordan, 2000.", "Jordan Meteorological Department: Jordan Annual Climate Bulletin,\nJMD, Amman, Jordan, 1999.", "Duffie and Beckman, Solar Engineering of Thermal Processes, 2nd\nedition, Wiley and Sons, Toronto."]} The purpose of this work is to present the potential of solar energy in Zarqa region. The solar radiation along year 2009 was obtained from Pyranometer which measures the global radiation over horizontal surfaces. Solar data in several different forms, over period of 5 minutes, hour-by-hour, daily and monthly data radiation have been presented. Briefly, the yearly global solar radiation in Zarqa is 7297.5 MJ/m2 (2027 kWh/m²) and the average annual solar radiation per day is 20 MJ/m2 (5.5 Kwh/m2). More specifically, the average annual solar radiation per day is 12.9 MJ/m2 (3.57 Kwh/m2) in winter and 25 MJ/m2 (7 Kwh/m2) in summer.

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  • image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Authors: Er.T.B.Shaikh; Er.A.B.Kolekar; Er.N.N.Shinde;

    Globally it is estimated that 84% of produced grains are wasted. In India 20-40% of food grains are spoiled, due to conventional preservation technique. The preservation tech like canning, freezing, drying etc are used in order to avoid the food wastage. Renewable hybrid drying system may be optimum for food preservations at low cost and will exploit at large in the present scenario. Proposed system of hybrid drying system is an integration of solar thermal air heating system coupled with air heating using suitable heating system based on biomass burning to maintain continuous drying process. Experiments are carried out for sun drying, oven drying, solar drying using air heaters and solar- biomass thermal drying. It is observed that solar hybrid system using biomass as a fuel for heating has reduced time of drying maize. For only solar system hot air drying time reduced from 72 to 33 hours and for solar hybrid drying time reduced from 72 to 15 hours. https://journalnx.com/journal-article/20150072

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  • Authors: Hermann Hofbauer; Friedrich Kirnbauer; Matthias Kuba; F. Havlik;

    An innovative process to produce synthesis gas from a solid feedstock is dual fluidbed (DFB) steam gasification of biomass. The principle of this technology is the separation of the fluidized bed into a gasification and a combustion zone. Bed material, nowadays olivine, is circulating, between them, which has two functions. Firstly, it acts as heat carrier from the combustion to the gasification zone. Secondly, it has the role of a catalyst regarding the reduction of hydrocarbons. In this work, the catalytic activity of different fresh and also used bed materials, such as olivine and silica sand was tested regarding their ability to enhance the water-gas-shift reaction and also reduce hydrocarbons. Calcite is known as active material in this respect and, therefore, used as reference substance. Experiments showed a correlation between the enhancement of the water-gas-shift reaction and the reduction of lighter and heavier hydrocarbons by steam reforming. Results show that as long as a bed material particle has built up a calcium-rich layer, satisfying conversion of carbon monoxide and the hydrocarbons can be achieved. As model substances for hydrocarbons ethane and toluene were used. These results are the basis for further research of catalytic characteristics of potential bed materials for the dual fluidized bed steam gasification of biomass. Proceedings of the 23rd European Biomass Conference and Exhibition, 1-4 June 2015, Vienna, Austria, pp. 562-567

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    Authors: Wenyuan Ye; Jiuyang Lin; Luis, Patricia; Bruggen, Bart Van Der;

    {"references": ["", "M. Meinshausen, N. Meinshausen, W. Hare, S. C. B. Raper, K. Frieler, R.\nKnutti, D. J. Frame, M. R. Allen, \"Greenhouse-gas Emission Targets for\nLimiting Global Warming to 2\u00b0C\" Nature J., vol. 458, pp. 1158-1162,\n2009.", "P. Luis, T. Van Gerven, and B. Van der Bruggen, \"Recent Developments\nin Membrane-based Technologies for CO2 Capture\" Prog. Energy\nCombust. Sci. J., vol. 38, pp. 419-448, 2012.", "W. Ye, J. Lin, J. Shen, P. Luis, B. Van der Bruggen, \"Membrane\nCrystallization of Sodium Carbonate for Carbon Dioxide Recovery:\nEffect of Impurities on the Crystal Morphology\" Cryst. Growth Des.J.,\nvol. 13, pp. 2362\u20132372, 2013.", "P. Luis, D Van Aubel, B Van der Bruggen, \"Technical viability and\nexergy analysis of membrane crystallization: Closing the loop of CO2\nsequestration\" Int. J. Greenh. Gas Con. J., vol. 12, pp. 450-459, 2013.", "T. Ring, \"Kinetic effects on particle morphology and size distribution\nduring batch precipitation\" Powder Technol. J., vol. 65, pp. 195-206,\n1991.", "M. A. Bialik, H. Theliander, P. Sedin, C. L. Verrill, N. DeMartini,\n\" Solubility and solid-phase composition in Na2CO3-Na2SO4 solutions at\nboiling temperature: A modeling approach\" Ind. Eng. Chem. Res. J., vol.\n47, pp. 3233-3238, 2008.", "D. Weckesser, A. K\u00f6nig, \"Particle shape and purity in membrane based\ncrystallization\" Chem. Eng. Technol. J. vol. 31, pp. 157-162, 2008.", "B. Shi, W. J. Frederick Jr., R. W. Rousseau, \"Nucleation, growth, and\ncomposition of crystals obtained from solutions of Na2CO3 and Na2SO4\"\nInd. Eng. Chem. Res. J., vol. 42, pp. 6343-6347, 2003.", "A. P. Soemardji, C. L. Verrill, W. J. Jr. Frederick, H. Theliander,\n\"Prediction of Crystal Species Transition in Aqueous Solutions of\nNa2CO3 and Na2SO4 and Kraft Black Liquor\" Tappi J. vol. 3, pp. 27-32 ,\n2004."]} This study addresses the effect of impurities on the crystallization of Na2CO3 produced within a strategy for capturing CO2 from flue gases by alkaline absorption. A novel technology - membrane assisted crystallization - is proposed for Na2CO3 crystallization from mother liquors containing impurities. High purity of Na2CO3•10H2O crystals was obtained without impacting the performance of the mass transfer of water vapor through membranes during crystallization.

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