Academic literature on the topic 'Solid biomass'
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Journal articles on the topic "Solid biomass"
HONJO, Takako. "Biomass Solid Fuel." Journal of High Temperature Society 34, no. 4 (2008): 146–52. http://dx.doi.org/10.7791/jhts.34.146.
Full textYeremenko, O. I. "Research of advanced crusher wood biomass for solid fuel production." Naukovij žurnal «Tehnìka ta energetika» 11, no. 1 (January 30, 2020): 105–13. http://dx.doi.org/10.31548/machenergy2020.01.105.
Full textWu, M. R., D. L. Schott, and G. Lodewijks. "Physical properties of solid biomass." Biomass and Bioenergy 35, no. 5 (May 2011): 2093–105. http://dx.doi.org/10.1016/j.biombioe.2011.02.020.
Full textPestaño, Lola Domnina Bote, and Wilfredo I. Jose. "Production of Solid Fuel by Torrefaction Using Coconut Leaves As Renewable Biomass." International Journal of Renewable Energy Development 5, no. 3 (November 4, 2016): 187–97. http://dx.doi.org/10.14710/ijred.5.3.187-197.
Full textMiljkovic, Biljana, Branislava Nikolovski, Dejan Mitrović, and Jelena Janevski. "Modeling for Pyrolysis of Solid Biomass." Periodica Polytechnica Chemical Engineering 64, no. 2 (October 11, 2019): 192–204. http://dx.doi.org/10.3311/ppch.14039.
Full textCastaldi, Marco J. "D201 SOLID CARBON FEEDSTOCK GASIFICATION USING CO_2 SIMULATION AND EXPERIMENT(Biomass-4)." Proceedings of the International Conference on Power Engineering (ICOPE) 2009.2 (2009): _2–277_—_2–282_. http://dx.doi.org/10.1299/jsmeicope.2009.2._2-277_.
Full textIDA, Tamio. "A Study Outcome for Biomass Project and Solid Biomass Conversion Technology." Journal of Smart Processing 3, no. 1 (2014): 40–46. http://dx.doi.org/10.7791/jspmee.3.40.
Full textMa, Long Bo. "Empirical Analysis on Peasant Households' Willingness of Using Solid Biomass Fuel." Applied Mechanics and Materials 548-549 (April 2014): 617–21. http://dx.doi.org/10.4028/www.scientific.net/amm.548-549.617.
Full textAbdulyekeen, Kabir Abogunde, Ahmad Abulfathi Umar, Muhamad Fazly Abdul Patah, and Wan Mohd Ashri Wan Daud. "Torrefaction of biomass: Production of enhanced solid biofuel from municipal solid waste and other types of biomass." Renewable and Sustainable Energy Reviews 150 (October 2021): 111436. http://dx.doi.org/10.1016/j.rser.2021.111436.
Full textJoseph, Ben, Frank Hensgen, Lutz Bühle, and Michael Wachendorf. "Solid Fuel Production from Semi-Natural Grassland Biomass—Results from a Commercial-Scale IFBB Plant." Energies 11, no. 11 (November 1, 2018): 3011. http://dx.doi.org/10.3390/en11113011.
Full textDissertations / Theses on the topic "Solid biomass"
Schimming, Sarah McNew. "Design of solid catalysts for biomass upgrading." Diss., Georgia Institute of Technology, 2014. http://hdl.handle.net/1853/54265.
Full textLaryea-Goldsmith, Rene. "Concurrent combustion of biomass and municipal solid waste." Thesis, Cranfield University, 2010. http://dspace.lib.cranfield.ac.uk/handle/1826/5580.
Full textBecidan, Michaël. "Experimental Studies on Municipal Solid Waste and Biomass Pyrolysis." Doctoral thesis, Norwegian University of Science and Technology, Department of Energy and Process Engineering, 2007. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-1723.
Full textThe introduction of this thesis (Chapters 1-9) presents the broader picture of waste management and thermal treatments (situation, trends and novel concepts) with a strong focus on nitrogen (N) in Chapter 6 (a summary of this chapter can be found on page 42). A new insight on N-functionalities is presented, mostly based on plant physiology publications widely ignored by the bioenergy world. N in biomass is found in a variety of chemical compounds and not only in protein compounds. An extensive literature survey concerning N-chemistry during pyrolysis of model compounds and biomass has also been done. A critical light is cast on these studies.
Paper I (or P-I) ([Becidan 2004]) presents preliminary results using the experimental set-up and shows its potential in thermal studies. The study of N-release was twofold: NOx release during combustion of biomass and NOx precursors (NH3 and HCN) release during pyrolysis of sewage sludge. The main results confirm known trends: N-release during combustion decreases with increasing fuel-N content; N-release as NH3 and HCN during pyrolysis is clearly dependent on temperature with increasing release with increasing temperature and NH3 as the main component at all conditions.
Paper II (or P-II) ([Skreiberg 2004]) presents modelling work realised to assess the potential for reduction of NOx emission formed from fuel-N by implementing staged air combustion. The results obtained from these chemical analysis of ideal reactors (Plug Flow Reactor and Perfectly Stirred Reactor) can be seen as a simplified CFD approach. The reduction potential is depending on a variety of factors and will therefore have to be assessed on a case-to-case basis. However, some conclusions can be drawn: (1) PSR mixing conditions are more favourable than PFR flow; (2) increasing fuel-N content will increase the relative NOx reduction potential; (3) increasing fuel-N fraction of NH3, or HNCO, compared to HCN will increase the NOx reduction potential; (4) increasing amounts of CO, and H2, will increase the NOx reduction potential, but it depends also on the fuel-N compounds; (5) one primary air stage is sufficient, unless also the fuel supply is staged. It is possible to further increase the NOx reduction with more primary air stages at some conditions, but the increase is limited; (6) increasing overall excess air ratio will decrease the NOx reduction potential; (7) increasing residence time will only significantly increase the NOx reduction potential until the main chemistry is completed. However, the time for completion of the main chemistry is significantly longer in a PSR compared to a PFR, and the effect of an increasing residence time is much more pronounced at optimum conditions in a PSR; (8) temperature is an important parameter. However, for a specific set of other parameters there exists an optimum temperature. The temperature in the primary air stage should be high enough to complete the main chemistry. The temperature needed to complete the main chemistry, and the fuel-N chemistry, in a PSR is higher than in a PFR for the same residence time. The temperature in the secondary air stage should be as low as possible, but high enough to ensure complete combustion.
Paper III (or P-III) ([Becidan 2007a]) looks at the products distribution and the main pyrolysis products of thermally thick and scarcely studied biomass residues samples. For all fuels, higher temperatures favour gas yield at the expense of char and liquid yields. High heating rate also promotes gas yield. The main gas components were CO2, CO, CH4, H2, C2H2, C2H6 and C2H4. An increase in temperature and heating rate leads to increasing yields for all the gases up to 825-900°C where CO2 and hydrocarbons yields show a clear tendency to stabilise, increase slightly or decrease slightly depending on the fuel. The gas release dynamics reveal important information about the thermal behaviour of the various components (cellulose, hemicellulose and lignin) of the biomass and are consistent with studies using TGA. The gross calorific value of the gas produced increases with increasing temperature reaching a plateau at 750-900ºC. This study provides valuable data of the thermal behaviour of thermally thick biomass samples which is of interest for further work in the area of combustion, gasification and pyrolysis in fixed beds. The study confirms the potential of those unexploited residues for production of energy carriers through pyrolysis.
Paper IV (or P-IV) ([Becidan 2007b]) proposes a more extensive study of N-release from 3 biomass residues (coffee waste, brewer spent grains, fibreboard). This study of N-behaviour during biomass pyrolysis of thermally thick samples provided several findings. At high heating rate, NH3 and HCN are the two N-containing compounds, NH3 being the main one at all conditions; NH3 release increases with increasing heating rate and temperature to reach a maximum at 825-900°C while HCN yield increases sharply with temperature without reaching a plateau in the temperature range studied. N-selectivity, N release pattern and N-compounds thermal behaviour are affected by the fuel properties, in all probability including N-functionalities. While the total N-conversion levels to (HCN+NH3) are similar for all fuels at high heating rate, the differences are very significant at low heating rate (more than 2-fold for NH3 and 3-fold for HCN). This can be related to the different fuel properties including N-functionalities. Several attempts have been made previously to correlate N-functionalities and N-release during pyrolysis. However no clear dependence has ever been established for biomass. Furthermore, the intricate and versatile nature of N in biomass samples and its interactions with emicellulose, cellulose and lignin prior to and during pyrolysis are difficult to elucidate.
A mechanism of cross-linking between a protein side group and cellulose during pyrolysis was proposed. Further work should focus on the use of the data obtained for improved modelling of biomass pyrolysis. In order to obtain more mechanistic insights the study of model compounds seems more appropriate but may have limited validity because of the intricate structure of “real” biomass. These two types of studies are therefore complementary to obtain a good overview of N-release.
Paper V (or P-V) ([Becidan 2007c]) presents the kinetics of decomposition of the three afore-mentioned biomass residues. The results can be summarised as such:
(1) The samples were studied at five different T(t) temperature programs. The temperature programs covered a wide range of experimental conditions: the experiments exhibited 10 – 14 times variation in time span, mean reaction rate and peak reaction rate.
The experiments on a given sample were described by the same set of model parameters. The optimal parameters were determined by the method of least squares. Three models were proposed that described equally well the behavior of the samples in the range of observations.
(2) A model built from three distributed activation energy reactions was suitable to describe the devolatilisation at the highly different T(t) functions of our study with only 12 adjustable parameters. The other two models contained simpler mathematical equations (first order and nth order partial reactions, respectively), accordingly their use may be more convenient when the coupling of kinetic and transport equations are needed. On the other hand, the simpler models needed higher numbers of parameters to describe the complexity of these wastes
(3) The reliability of the proposed models was tested in three ways: (i) the models provided good fits for all the five experiments of a sample; (ii) the evaluation of a narrower subset of the experiments (the three slowest experiments) provided approximately the same parameters as the evaluation of the whole series of experiments; (iii) the models proved to be suitable to predict the behavior of the samples outside of those experimental conditions at which the model parameters were determined. Check (iii) corresponded to an extrapolation to ca. four-time higher reaction rates from the domain of the three slowest experiments.
(4) The evaluated experiments included “constant reaction rate” (CRR) measurements. This type of temperature control involves a continuously changing heating rate. The simultaneous evaluation of linear, stepwise and CRR experiments proved to be advantageous in the determination of reliable kinetic models. (5) The samples had very different chemical compositions. Nevertheless, the same models described them equally well. Accordingly, the models and the strategies for their evaluation and validation can be recommended for a wider range of biomass studies.
Paper VI (or P-VI) ([Becidan 2007d]), this study on thermally thick biomass samples pyrolysis has investigated (1) temperature field, (2) weight loss at two scales (TGA and macro-TGA). The main findings are:
(a) Qualitative evaluation of the thermal history: three temperature regimes have been identified: (1) exponentially increasing temperature, (2) linearly increasing temperature (3) 2-slope increasing temperature with a flattening period. The regime at a given point will depend on the sample weight, the reactor temperature and the location in the sample.
(b) Quantitative evaluation of the thermal history: significant temperature gradients were measured, with a maximum radial gradient of 167°C/cm for coffee waste at a reactor temperature of 900°C. This will affect the pyrolysis process.
(c) The step-by-step pyrolysis chemistry was described and discussed (10°C/min heating rate). By use of a novel concept, i.e. intra-sample heating rate, the exothermic step of pyrolysis was shown. It is related to char and/or char-forming reactions.
(d) The comparative study of weight loss in TGA and macro-TGA (10°C/min heating rate, never done before to our knowledge) was performed to investigate the “scaling effect”. Pyrolysis time and pyrolysis rate differences were characterised and quantified.
Paper III reprinted with kind permission of Elsevier, sciencedirect. com
González, Martínez María. "Woody and agricultural biomass torrefaction : experimental study and modelling of solid conversion and volatile species release based on biomass extracted macromolecular components." Thesis, Toulouse, INPT, 2018. http://oatao.univ-toulouse.fr/24326/1/gonzalez_martinez.pdf.
Full textLiew, Lo Niee. "Solid-state Anaerobic Digestion of Lignocellulosic Biomass for Biogas Production." The Ohio State University, 2011. http://rave.ohiolink.edu/etdc/view?acc_num=osu1306870552.
Full textRamadhan, Omar M. "Biomass derived oil : production, fractionation and structural investigation." Thesis, University of Manchester, 1986. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.326043.
Full textSattar, Anwar. "Hydrogen production from biomass for use in solid oxide fuel cells." Thesis, University of Birmingham, 2015. http://etheses.bham.ac.uk//id/eprint/6335/.
Full textRecari, Ansa Javier. "Gasification of biomass and solid recovered fuels (SRFs) for the synthesis of liquid fuels." Doctoral thesis, Universitat Rovira i Virgili, 2017. http://hdl.handle.net/10803/450856.
Full textLa gasificación es una tecnología prometedora para el aprovechamiento energético de biomasa y residuos ya que permite convertir los combustibles sólidos en un gas de síntesis (syngas) con múltiples aplicaciones. Sin embargo, ciertas limitaciones todavía impiden la completa implementación de esta tecnología a escala industrial, en particular para la producción de combustibles líquidos a partir del proceso Fischer Tropsch (FT). Los principales inconvenientes están relacionados con la calidad del syngas, por ejemplo una baja relación H2/CO y la presencia de impurezas (tar y contaminantes menores), y dependen de la naturaleza del material y de las condiciones de operación del proceso de gasificación. Esta tesis se centra en la mejora de la calidad del syngas de gasificación de biomasa y combustibles sólidos recuperados (CSRs) para la producción de combustibles líquidos. El trabajo se divide en dos partes principales. La primera parte consiste en estudios experimentales de gasificación de biomasa y CSRs en un reactor de lecho fluidizado a escala de laboratorio para evaluar la influencia de las condiciones de operación (temperatura, materiales de lecho, agentes de gasificación, etc.) en el rendimiento del proceso y la composición del gas. Debido a que los CSRs contienen mayores cantidades de precursores de contaminantes que la biomasa, se ha desarrollado un método para determinar la concentración de HCl, H2S, HCN y NH3 en el syngas mediante potenciometría de ion selectivo. Además, se propone la aplicación de un pretratamiento térmico (torrefacción) a los materiales de gasificación como un método para mejorar las propiedades de los materiales y disminuir la emisión de contaminantes en el syngas. Por último, la segunda parte consiste en un estudio tecno-económico para estimar los costes de inversión y de operación de plantas de combustibles líquidos FT a partir de la gasificación de biomasa y residuos, partiendo de los resultados obtenidos experimentalmente.
Gasification is a promising technology for energy exploitation of biomass and waste, converting carbonaceous fuels into a synthesis gas (syngas) with multiple applications. However, technical obstacles hinder the full implementation of this technology at industrial scale, particularly for the production of liquid fuels through Fischer-Tropsch (FT) synthesis. Those challenges are mainly related to the syngas quality, such as a low H2/CO ratio and the presence of impurities (tar and minor contaminants), strongly influenced by the nature of the feedstock and the operating conditions of the gasification process. This thesis focuses on the improvement of the syngas quality from gasification of biomass and solid recovered fuels (SRFs) aiming to produce liquid fuels. The present work is divided in two main blocks. The first block corresponds to biomass and SRFs gasification experiments in a lab-scale fluidized bed reactor in order to study the influence of key operating conditions (temperature, bed materials, gasification agents, etc.) on the gasification performance and gas composition. Since SRF materials contain higher amounts of contaminants precursors than biomass, a method to assess the concentration of HCl, H2S, HCN and NH3 in the syngas by means of ion-selective potentiometry was developed. The application of a thermal pretreatment (torrefaction) to the gasification feedstocks is proposed as a way to upgrade the feedstock properties and abate the release of contaminants in the syngas. The second part of this work consists in a techno-economic analysis that estimates capital and production costs of FT liquid fuel plants based on biomass and waste gasification, using as input the experimental results.
Risnes, Håvar. "High Temperature Filtration in Biomass Combustion and Gasification Processes." Doctoral thesis, Norwegian University of Science and Technology, Faculty of Engineering Science and Technology, 2002. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-1485.
Full textHigh temperature filtration in combustion and gasification processes is a highly interdisciplinary field. Thus, particle technology in general has to be supported by elements of physics, chemistry, thermodynamics and heat and mass transfer processes. This topic can be addressed in many ways, phenomenological, based on the up stream processes (i.e. dust/aerosol formation and characterisation) or apparatus oriented.
The efficiency of the thermochemical conversion process and the subsequent emission control are major important areas in the development of environmentally sound and sustainable technology. Both are highly important for combustion and gasification plant design, operation and economy.
This thesis is divided into four parts:
I. High temperature cleaning in combustion processes.
II. Design evaluations of the Panel Bed Filter technology.
III. Biomass gasification
IV. High temperature cleaning of biomass gasification product gas
The first part validates the filter performance through field experiments on a full scale filter element employed to a biomass combustion process and relates the results to state of the art within comparable technologies (i.e. based on surface filtration). The derived field experience led to new incentives in the search for a simplified design featuring increased capacity. Thus, enabling both high efficiency and simplified production and maintenance. A thorough examination of design fundamentals leading to the development of a new filter geometry is presented.
It is evident that the up-stream process has significant influence upon the operation conditions of a filter unit. This has lead to a detailed investigation of some selected aspects related to the thermochemical conversion. Furthermore, the influence of fuel characteristics upon conversion and product gas quality is discussed.
The last part discusses the quality of biomass gasification product gas and requirements put upon the utilisation of this gas in turbines, diesel engines or other high temperature applications. Filtration experiments conducted on product gas derived from wood gasification are reported and discussed.
Josephson, Alexander Jon. "Modeling Soot Formation Derived from Solid Fuels." BYU ScholarsArchive, 2018. https://scholarsarchive.byu.edu/etd/7020.
Full textBooks on the topic "Solid biomass"
Birdsall, Jaquelyn. Repowering solid fuel biomass electricity generation. Sacramento, California]: [California Energy Commission], 2012.
Find full textJones, Jenny M., Amanda R. Lea-Langton, Lin Ma, Mohamed Pourkashanian, and Alan Williams. Pollutants Generated by the Combustion of Solid Biomass Fuels. London: Springer London, 2014. http://dx.doi.org/10.1007/978-1-4471-6437-1.
Full textMatolcsy, G. A. Development of a moisture resistant densified solid fuel from forest biomass. Ottawa: The Dept., 1986.
Find full textCompany, RAM Mutual Insurance. Fire safety in solid fuel burning systems. Esko, Minn: RAM Mutual Insurance Co., 2002.
Find full textLind, Terttaliisa. Ash formation in circulating fluidised bed combustion of coal and solid biomass. Espoo, Finland: VTT, Technical Research Centre of Finland, 1999.
Find full textGrammelis, Panagiotis. Solid biofuels for energy: A lower greenhouse gas alternative. London: Springer, 2011.
Find full textTillman, David A. Solid fuel blending: Principles, practices, and problems. Oxford: Elsevier, Butterworth-Heinemann, 2012.
Find full textInternational Workshop on Thermal Solid Waste Utilisation in Regular and Industrial Facilities (1999 Kazimierz Dolny, Poland). Thermal solid waste utilisation in regular and industrial facilities: [proceedings of the International Workshop on Thermal Solid Waste Utilisation in Regular and Industrial Facilities, held November 28-30, 1999, in Kazimierz Dolny, Poland]. New York: Kluwer Academic, 2000.
Find full textEuropean Forum on Electricity Production from Biomass and Solid Wastes by Advanced Technologies (1st 1991 Florence). Electricity production from biomass and solid wastes by advanced technologies: Proceedings of the 1st European forum on electricity production from biomass and solid wastes by advanced technologies, Florence, Italy, 27-29 November 1991. [Luxembourg]: [Office for Official Publications of the European Communities], 1992.
Find full textDuong, Dao (Dao N.B.) and Harding N. S, eds. Solid fuel blending: Principles, practices, and problems. Oxford: Elsevier, Butterworth-Heinemann, 2012.
Find full textBook chapters on the topic "Solid biomass"
Christoforou, Elias, and Paris A. Fokaides. "Biomass Raw Material." In Advances in Solid Biofuels, 5–24. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-030-00862-8_2.
Full textChristoforou, Elias, and Paris A. Fokaides. "Solid Biomass Pretreatment Processes." In Advances in Solid Biofuels, 25–56. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-030-00862-8_3.
Full textPels, J. R., and A. J. Sarabèr. "Utilization of Biomass Ashes." In Solid Biofuels for Energy, 219–35. London: Springer London, 2011. http://dx.doi.org/10.1007/978-1-84996-393-0_10.
Full textWebster, David J. "Municipal Solid Waste as a Biomass Feedstock." In Plant Biomass Conversion, 109–27. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2011. http://dx.doi.org/10.1002/9780470959138.ch5.
Full textKlemm, Marco, Ralf Schmersahl, Claudia Kirsten, Nadja Weller, Annett Pollex, Jan Hari Arti Khalsa, and Thomas Zeng. "Upgraded “New” Solid Biofuels." In Energy from Organic Materials (Biomass), 451–81. New York, NY: Springer New York, 2018. http://dx.doi.org/10.1007/978-1-4939-7813-7_247.
Full textMirowski, Tomasz, and Eugeniusz Mokrzycki. "Thermochemical Processing of Solid Biomass." In Biomass in Small-Scale Energy Applications: Theory and Practice, 1–18. Boca Raton : Taylor & Francis, CRC Press, 2019. | Series: Energy systems : from design to management: CRC Press, 2019. http://dx.doi.org/10.1201/9780429286063-1.
Full textJones, Jenny M., Amanda R. Lea-Langton, Lin Ma, Mohamed Pourkashanian, and Alan Williams. "The Combustion of Solid Biomass." In Pollutants Generated by the Combustion of Solid Biomass Fuels, 25–43. London: Springer London, 2014. http://dx.doi.org/10.1007/978-1-4471-6437-1_3.
Full textHartmann, Hans. "Solid Biofuels and Their Characteristics." In Energy from Organic Materials (Biomass), 415–50. New York, NY: Springer New York, 2018. http://dx.doi.org/10.1007/978-1-4939-7813-7_245.
Full textBhaskaran, Sminu, Saurabh Gupta, and Santanu De. "Dual Fluidized Bed Gasification of Solid Fuels." In Coal and Biomass Gasification, 425–54. Singapore: Springer Singapore, 2017. http://dx.doi.org/10.1007/978-981-10-7335-9_17.
Full textDurand, A., C. Vergoignan, and C. Desgranges. "Biomass estimation in solid state fermentation." In Advances in Solid State Fermentation, 23–37. Dordrecht: Springer Netherlands, 1997. http://dx.doi.org/10.1007/978-94-017-0661-2_3.
Full textConference papers on the topic "Solid biomass"
Barreiros Martins, Luis A., Marco Andre´ Reis, Manuel Eduardo Ferreira, and Jose´ Carlos Teixeira. "Drying Kinetics of Solid Biomass." In ASME 2011 International Mechanical Engineering Congress and Exposition. ASMEDC, 2011. http://dx.doi.org/10.1115/imece2011-64242.
Full textBurra, K. G., and A. K. Gupta. "Role of Catalyst in Solid Biomass Gasification." In ASME 2016 Power Conference collocated with the ASME 2016 10th International Conference on Energy Sustainability and the ASME 2016 14th International Conference on Fuel Cell Science, Engineering and Technology. American Society of Mechanical Engineers, 2016. http://dx.doi.org/10.1115/power2016-59039.
Full textInfiesta, Luciano, Cassius Ferreira, Alam Trovó, Luciana Gonçalves, Washington Martins da Silva Jr., Valério Luiz Borges, and Solidônio Carvalho. "PELLETIZED BIOMASS FROM MUNICIPAL SOLID WASTES FOR USE AS SOLID FUEL." In Brazilian Congress of Thermal Sciences and Engineering. ABCM, 2018. http://dx.doi.org/10.26678/abcm.encit2018.cit18-0015.
Full textShamsuddin, Abd Halim, and Mohd Shahir Liew. "High Quality Solid Biofuel Briquette Production From Palm Oil Milling Solid Wastes." In ASME 2009 3rd International Conference on Energy Sustainability collocated with the Heat Transfer and InterPACK09 Conferences. ASMEDC, 2009. http://dx.doi.org/10.1115/es2009-90122.
Full textApprill, Bob, Logan Coen, Brian Gessler, Jonathan Mattson, and Christopher Depcik. "Fixed Bed Solid Fuel Combustor for the Purpose of Testing Solid Biomass Emissions Properties." In ASME 2014 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/imece2014-36543.
Full textMa, Long-bo, Da-hong Zhang, and Zu-jun Liu. "Way of the Development of Solid biomass fuel Industry." In 2010 2nd International Conference on Information Science and Engineering (ICISE). IEEE, 2010. http://dx.doi.org/10.1109/icise.2010.5690560.
Full textDavid Lanning, Christopher Lanning, James Fridley, James Dooley, and Mark DeTray. "Mode of Failure Model for Cutting Solid Section Biomass." In 2008 Providence, Rhode Island, June 29 - July 2, 2008. St. Joseph, MI: American Society of Agricultural and Biological Engineers, 2008. http://dx.doi.org/10.13031/2013.25016.
Full textZhu, Zhe, Saqib Sohail Toor, Lasse Rosendahl, Donghong Yu, and Guanyi Chen. "Experimental Study of Subcritical Water Liquefaction of Biomass: Effects of Catalyst and Biomass Species." In ASME 2014 8th International Conference on Energy Sustainability collocated with the ASME 2014 12th International Conference on Fuel Cell Science, Engineering and Technology. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/es2014-6708.
Full textSiregar, S. R. H., D. Nursani, and A. Surjosatyo. "Influence of Die Temperature on Unit Density and Calorific Value of Municipal Solid Waste Pellets." In International Conference on Sustainable Biomass (ICSB 2019). Paris, France: Atlantis Press, 2021. http://dx.doi.org/10.2991/aer.k.210603.034.
Full textRahim, D. A., M. Yan, R. D. A. Pohan, D. Hantoko, and H. Susanto. "Upgrading of Palm Oil Empty Fruit Bunches to Solid Fuel Using Torrefaction and Hydrothermal Treatment." In International Conference on Sustainable Biomass (ICSB 2019). Paris, France: Atlantis Press, 2021. http://dx.doi.org/10.2991/aer.k.210603.030.
Full textReports on the topic "Solid biomass"
Farzan, Hamid. NEW SOLID FUELS FROM COAL AND BIOMASS WASTE. Office of Scientific and Technical Information (OSTI), September 2001. http://dx.doi.org/10.2172/789505.
Full textAkers, David J., Glenn A. Shirey, Zalman Zitron, and Charles Q. Maney. PRODUCTION OF NEW BIOMASS/WASTE-CONTAINING SOLID FUELS. Office of Scientific and Technical Information (OSTI), April 2001. http://dx.doi.org/10.2172/806994.
Full textGlenn A. Shirey and David J. Akers. Production of New Biomass/Waste-Containing Solid Fuels. Office of Scientific and Technical Information (OSTI), September 2005. http://dx.doi.org/10.2172/861525.
Full textLindberg, Jenny P., and Jukka Tana. Best Available Techniques (BAT) in solid biomass fuel processing, handling, storage and production of pellets from biomass. Nordic Council of Ministers, September 2012. http://dx.doi.org/10.6027/tn2012-550.
Full textHenry Liu and Yadong Li. COMPACTING BIOMASS AND MUNICIPAL SOLID WASTES TO FORM AND UPGRADED FUEL. Office of Scientific and Technical Information (OSTI), November 2000. http://dx.doi.org/10.2172/837464.
Full textKelly, John T., George Miller, and Mehdi Namazian. A LOW COST AND HIGH QUALITY SOLID FUEL FROM BIOMASS AND COAL FINES. Office of Scientific and Technical Information (OSTI), July 2001. http://dx.doi.org/10.2172/795777.
Full textHu, Hongqiang, Michael Clark, Amber Hoover, Kevin Kenney, B. Dutcher, G. Wilson, and V. Sethi. Technical Assessment of Using Biomass from Methyl-bromide Treated Fields in Solid Fuel Boilers. Office of Scientific and Technical Information (OSTI), June 2017. http://dx.doi.org/10.2172/1408506.
Full textJ. Richard Hess, Christopher T. Wright, Kevin L. Kenney, and Erin M. Searcy. Uniform-Format Solid Feedstock Supply System: A Commodity-Scale Design to Produce an Infrastructure-Compatible Bulk Solid from Lignocellulosic Biomass -- Executive Summary. Office of Scientific and Technical Information (OSTI), April 2009. http://dx.doi.org/10.2172/971374.
Full textTao, Greg, G. A Reversible Planar Solid Oxide Fuel-Fed Electrolysis Cell and Solid Oxide Fuel Cell for Hydrogen and Electricity Production Operating on Natural Gas/Biomass Fuels. Office of Scientific and Technical Information (OSTI), March 2007. http://dx.doi.org/10.2172/934689.
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