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Littérature scientifique sur le sujet « Bio-oil »

Auteur : Grafiati
Publié le 4 juin 2021
Mis à jour le 8 juin 2024

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Articles de revues sur le sujet "Bio-oil"

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Comyns, Alan. « Treating bio-oil ». Focus on Catalysts 2014, no 7 (juillet 2014) : 1. http://dx.doi.org/10.1016/s1351-4180(14)70218-1.

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Zhu, Jiu‐fang, Ji‐cong Wang et Quan‐xin Li. « Transformation of Bio‐oil into BTX by Bio‐oil Catalytic Cracking ». Chinese Journal of Chemical Physics 26, no 4 (août 2013) : 477–83. http://dx.doi.org/10.1063/1674-0068/26/04/477-483.

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Singh, Kaushlendra, L. Mark Risse, K. C. Das, John Worley et Sidney Thompson. « Pyrolysis of Poultry Litter Fractions for Bio-Char and Bio-Oil Production ». Journal of Agricultural Science and Applications 01, no 02 (30 juin 2012) : 37–44. http://dx.doi.org/10.14511/jasa.2012.010201.

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Ahmed, Abu Saleh. « Microwave Assisted Pyrolysis of Moringa Seed and Karanja for Bio-Oil Production ». International Journal of Renewable Energy Resources 13, no 1 (6 mai 2023) : 14–24. http://dx.doi.org/10.22452/ijrer.vol13no1.2.

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Microwave-assisted pyrolysis is an alternative technique of conventional heating which undergo thermochemical process to convert biomass to bio oil, bio char and biogas. Microwave-assisted pyrolysis is more rapid and efficient to produce product compared to conventional heating. A modified household microwave oven with 800W was used to pyrolyze Moringa seed and Karanja to become bio oil and bio char. This experiment was repeated in different parameters such as time, temperature and power to obtain maximum bio oil yield. Bio oil yield of Moringa seed increased from 7.2 wt% at 300°C in 5 minutes to 10.6 wt% at 450°C in 13 minutes. Bio oil of both raw materials showed maximum yield when pyrolysis time is 13 minutes in 800W but after 13 minutes, the bio oil yield of Moringa decrease of 2.4% and bio oil yield of Karanja decrease of 4.7%. The calorific value of Moringa bio oil is 25.08MJ/kg whereas Karanja bio oil is 20.36 MJ/kg. Functional group of both bio oil mainly include alcohol, ketones, aldehydes and carboxylic acid. The pH value of Moringa bio oil and Karanja bio oil are 4.38 and 5.86 respectively.
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Lindfors, Christian, Eeva Kuoppala, Anja Oasmaa, Yrjö Solantausta et Vesa Arpiainen. « Fractionation of Bio-Oil ». Energy & ; Fuels 28, no 9 (7 septembre 2014) : 5785–91. http://dx.doi.org/10.1021/ef500754d.

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Meng, Jiajia, Andrew Moore, David Tilotta, Stephen Kelley et Sunkyu Park. « Toward Understanding of Bio-Oil Aging : Accelerated Aging of Bio-Oil Fractions ». ACS Sustainable Chemistry & ; Engineering 2, no 8 (16 juillet 2014) : 2011–18. http://dx.doi.org/10.1021/sc500223e.

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Zhuang, Xiaozhuang, Ziyu Gan, Dengyu Chen, Kehui Cen, Yuping Ba et Dongxia Jia. « An approach for upgrading bio-oil by using heavy bio-oil co-pyrolyzed with bamboo leached with light bio-oil ». Fuel 331 (janvier 2023) : 125931. http://dx.doi.org/10.1016/j.fuel.2022.125931.

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Qarizada, Deana, Erfan Mohammadian, Azil Bahari Alis, Suriatie Mat Yusuf, Aqilah Dollah, Humapar Azhar Rahimi, Ahmad Shah Nazari et Muzhda Azizi. « Thermo Distillation and Characterization of Bio Oil from Fast Pyrolysis of Palm Kernel Shell (PKS) ». Key Engineering Materials 797 (mars 2019) : 359–64. http://dx.doi.org/10.4028/www.scientific.net/kem.797.359.

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Thermo distillation of palm kernel shell in a column reactor was studied in this paper. The objective of this research was to characterize the bio oil and bio oil fractions. The maximum yield was around 70 wt% at 120 °C. The bio oil fractions were collected in ten columns at different temperature ranging between 75- 105°C. HHV of bio oil was 26MJ/Kg. The bio oil moisture, volatility, fixed carbon, and ash were determined and found to be around 6.44wt%, 52.72wt%, 24.39wt%, 16.45wt%, respectively. It can be seen that the PKS bio oil can be considered as an alternative fuel. . HHV of bio oil fraction was between 20- 21MJ/Kg, The density of bio oil fraction was 976.54 g/ mL, and pH of bio oil fraction were around of 2.16.
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Jamil, Farrukh, Murni Melati Ahmad et Suzana Yusup. « Comparative Study for Catalytic Cracking of Model Bio-Oil and Palm Kernel Shell Derived Bio-Oil ». Advanced Materials Research 781-784 (septembre 2013) : 2476–79. http://dx.doi.org/10.4028/www.scientific.net/amr.781-784.2476.

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This work investigates the comparison between upgraded product from model bio-oil and bio-oil from PKS. The process is carried out in the presence of HZSM-5 at temperature of 500oC, 3bar pressure and oil/catalyst ratio of 15. It is observed that the properties such as pH, density, calorific value and elemental value of products are improved. The calorific value for upgraded bio-oil is 31.65 MJ/kg while for model bio-oil the value is 30.32 MJ/kg at same operating conditions. The degree of deoxygenation of the upgraded bio-oil and upgraded model bio-oil is 43.74% and 45.56% respectively. The study showed that the model bio-oil can be used to represent the bio-oil.
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Zainab, H., N. Nurfatirah, A. Norfaezah et H. Othman. « Green bio-oil extraction for oil crops ». IOP Conference Series : Materials Science and Engineering 133 (juin 2016) : 012053. http://dx.doi.org/10.1088/1757-899x/133/1/012053.

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Thèses sur le sujet "Bio-oil"

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Sakaguchi, Masakazu. « Gasification of bio-oil and bio-oil/char slurry ». Thesis, University of British Columbia, 2010. http://hdl.handle.net/2429/23347.

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Economic utilization of biomass as a fuel has been limited by transportation cost. One suggested remedy to address the problems of processing biomass on a large scale is to pyrolyze solid biomass at numerous local sites and transport the resulting liquid or liquid/char slurry to a large centralized conversion plant. This research involves the gasification of biomass fast pyrolysis oil, so called bio-oil, and a slurry mixture of bio-oil and fast pyrolysis char into synthesis gas. Kinetics of the reaction of steam with chars was studied using a thermo-gravimetric analyzer. Slurry Char was produced by pyrolysis of an 80 wt% bio-oil/20 wt% char mixture at nominal heating rates of 100–10,000°C/s. The resulting Slurry Char was subjected to steam gasification with 10–50 mol% steam at 800–1200°C. Reactivity of the Slurry Chars increased with the pyrolysis heating rate, but was lower than that of Original Chars. Kinetic parameters were established for a power-law rate model. Some measurements were initially done of gasification in CO₂. A fluidized bed reactor, equipped with an atomization system, was constructed for gasification of bio-oil and slurry. The reactor contained either sand, or Ni-based catalyst. Experiments included gasification with pure steam and air. Effects of bed temperatures in the range 720–850°C, steam-to-carbon molar ratios of 2.0–7.5, and air ratios of 0–0.5 on gas composition and yields were tested. The carbon conversion of bio-oil to gas was found to be greater than that of slurry. The product gas composition was affected significantly by catalysis of the water-gas shift and the steam gasification. Greater yields of hydrogen and lesser yields of CO and hydrocarbons were found when catalyst was used. On a dry, inert-free basis, gases of up to 61% H₂ were obtained. The data were compared with a thermodynamic equilibrium model. The product gas yield was reasonably predictable by the model. A mass and energy balance model of steam gasification in a dual-bed gasifier-combustor revealed that energy requirements are sensitive to the steam/carbon ratio and to the recovery of latent heat in the produced gas.
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Zhang, Mingming. « Properties of bio-oil based fuel mixtures : biochar/bio-oil slurry fuels and glycerol/bio-oil fuel blends ». Thesis, Curtin University, 2015. http://hdl.handle.net/20.500.11937/1825.

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This thesis reports the properties of bio-oil-based fuel mixtures. For bioslurry fuels, the interaction between biochar and bio-oil results in changes in fuel properties and the redistribution of inorganic species. For glycerol/methanol/bio-oil (GMB) fuel blends, the solubility and fuel properties are improved upon methanol addition but other impurities in crude glycerol worsen the solubility with limited impact on properties. It is also possible to integrate the GMB blends production into the biodiesel production process.
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Ortiz-Toral, Pedro J. « Steam reforming of bio-oil effect of bio-oil composition and stability / ». [Ames, Iowa : Iowa State University], 2008.

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Pollard, Anthony Joseph Sherwood. « Comparison of bio-oil produced in a fractionated bio-oil collection system ». [Ames, Iowa : Iowa State University], 2009. http://gateway.proquest.com/openurl?url_ver=Z39.88-2004&rft_val_fmt=info:ofi/fmt:kev:mtx:dissertation&res_dat=xri:pqdiss&rft_dat=xri:pqdiss:1474690.

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Atiku, Farooq Abubakar. « Combustion of bio-oil and heavy fuel oil ». Thesis, University of Leeds, 2015. http://etheses.whiterose.ac.uk/12179/.

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The use of combustion parameters to predict what happens to fuel during burning and its effect on living systems is important. This work is directed towards understanding the fundamental chemistry of soot generated from burning biomass-pyrolysis liquid fuels and its mechanism of formation. In this study, fuels such as eugenol, anisole, furfural and some hydrocarbon fuels are subjected to combustion using a wick burner which allowed the burning rate, smoke point and emission factor to be investigated. Reaction zone analysis of flames by direct photography and by using optical filters for further investigation of C2* and CH* species, was conducted. Additionally, detailed characterization of the soot generated was performed, and comparisons were made with soot from petroleum products and from biomass combustion system. The key aim was to generate experimental data and to capture detailed information regarding sooting tendencies with a view to utilize the information which would eventually allow the formation of a comprehensive bio-oil combustion model. This could provide accurate predictions of the combustion characteristics and pollutant formation. Studies are reported on the significant role of high temperature pyrolysis products in soot formation and acquiring further mechanistic insight. This work has been extended to consider heavy petroleum fuel oils (residual oil) during combustion and the effect of composition on combustion products and on the effect on health and the global environment. Heavy fuel oil, such as Bunker C and vacuum residue, are commonly used as fuel for industrial boilers, power generation, and as transport fuels in, for example, in large marine engines. The combustion of these fuels gives rise to carbonaceous particulate emissions including fine soot (Black Carbon or BC) which, along with associated polynuclear aromatic hydrocarbons (PAH): The structure and thermal reactions of petroleum asphaltene have been studied by analytical pyrolysis. Additionally, related combustion characteristics of the asphaltene extracted from bio-oil have been investigated by pyrolysis gas chromatography-mass spectrometry. The results showed the difference between bio-asphaltene and the petroleum asphaltene and the different tendency to form smoke. They also showed the presence of markers for the bio-asphaltene structure.
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Chan, Jacky. « Ethanol production from bio-oil ». Thesis, University of British Columbia, 2009. http://hdl.handle.net/2429/14730.

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Bioethanol is often viewed as one of the solutions to the tight gasoline supplies in North America. Although bioethanol is already available in the market, there are a number of problems associated with the current processes for the production of bioethanol. The current bioethanol production processes are often referred as first generation bioethanol production processes. For these first generation processes, the feedstocks for production are usually energy crops. The most common energy crops in North America are corn and wheat. The use of these energy crops has triggered debates on the problems associated with using food sources to create energy and the uptake of agricultural land to produce energy. In this project, an alternative feedstock for bioethanol is investigated. The feedstock used in the project is bio-oil, which can be derived from any biomass waste. An advantage of using bio-oil is that it is not derived from food crops but instead waste material is being converted into energy. The objective of this study was to determine the technical viability of producing bio ethanol using bio-oil as a substrate for fermentation. In order to maximize the ethanol yield, the extraction of levoglucosan with water was optimized and a number of detoxification techniques for inhibitor removal were evaluated. This report provides a technical overview of conditions evaluated for extracting levoglucosan from bio-oil, and methods used for improving the fermentability of bio-oil hydrolysate by detoxification. The techniques used in an attempt to improve the fermentability of bio-oil hydrolysate include: adsorption, overliming, solvent extraction, and hydrogenation. In addition, a biological approach called adaptive evolution was used to aid the yeast to adapt to the inhibitory environment of bio-oil hydrolysate in order to increase their resistance to inhibitors. The optimal condition for aqueous extraction of levoglucosan from bio-oil was found to be 1:1 (mass water to mass bio-oil). It was found that the temperatures examined (25°C and 80°C) had minimal effect on the amount of levoglucosan extracted. Among the detoxification techniques tested, it was found that overliming and solvent extraction were able to improve the fermentability of bio-oil hydrolysates. Overliming was able to increase the yield of ethanol from bio-oil hydrolysate by 0.19±0.01 (g ethanol/g glucose) at 50% strength hydrolysate and 0.45±0.05 (g ethanol/g glucose) at 40% strength hydrolysate. A number of extractants were examined and the three best solvents were 25% volume of tri-n-octylamine with co-solvent 1-octanol, 50% volume of alamine 336 with co-solvent 1-octanol and oleyl alcohol. These three solvents were able to selectively remove at least 84 — 93% of acetic acid, which was the targeted inhibitor in bio-oil hydrolysate. In addition, a technique called adaptive evolution of yeasts was applied, which was capable of increasing the ethanol yield by at least 6% when compared with the unadapted parental strains.
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Lifita, Nguve Tande. « Autothermal reforming of bio-oil model compounds ». Thesis, University of Leeds, 2018. http://etheses.whiterose.ac.uk/20004/.

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Correll, David. « Optimized landscape plans for bio-oil production ». [Ames, Iowa : Iowa State University], 2009. http://gateway.proquest.com/openurl?url_ver=Z39.88-2004&rft_val_fmt=info:ofi/fmt:kev:mtx:dissertation&res_dat=xri:pqdiss&rft_dat=xri:pqdiss:1464191.

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Liu, Kai. « Catalytic hydrodeoxygenation of bio-oil and model compounds ». Thesis, Imperial College London, 2016. http://hdl.handle.net/10044/1/51555.

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The upgrading of the Norwegian spruce derived bio-oil was carried out in a batch reactor with conditions of 50 bar H2 (cold) and 3 to 13 hr of batch time at 175 to 250 ℃. The emphasis was given on the effect of operating conditions on the hydrodeoxygenation (HDO) performance of unsupported NiMo nano sulphide catalysts. It is found that the degree of deoxygenation of the bio-oil increases and that of hydrogenation of the upgraded products declines with increasing the reaction temperature. The addition of sulphur to prevent the nanosulphide catalyst leaching problem is not essential. Extending the batch time produces more saturated products with less oxygen content, but it can be optimised as the deoxygenation reaction rate decreases along the time. As for HDO solvent, dodecane is preferred comparing with tetralin. The HDO of p-cresol over Co/Al2O3 and Ni/Al2O3 catalysts at 250 to 375 ℃ and 50 bar of H2 (hot) in a batch reactor gives 4-methylcyclohexanol, methylcyclohexane and toluene as the major products. Both catalysts are active leading to almost complete conversion (≥98%) of p-cresol at all temperatures. The degree of deoxygenation and the product distribution of toluene increases with temperature. Toluene can be produced by the direct deoxygenation of p-cresol and by the disproportionation of methylcyclohexenes at high temperature (i.e. 375 ℃). Sulphur suppresses the HDO of p-cresol. It deactivates the hydrogenation sites but does not appear to be a poison for the hydrogenolysis sites. Same conditions were used for the HDO of guaiacol, except the H2 pressure being used was 40 bar (cold). Dominant products are cyclohexanol, methoxycyclohexanols and cyclohexane at 300 ℃ and below and those at 325 ℃ and above are cyclohexane, benzene and ring contraction products (i.e. cyclopentane and methylcyclopentane). High temperatures facilitate deoxygenation and benzene production. As the temperature increases, the methoxyl group is firstly removed and then the hydroxyl group. At 350 ℃, reducing the pressure from 40 bar (cold) to 20 bar (cold) increases the benzene product distribution from 2 wt% to 40 wt%. Sulphur has a detrimental effect on the HDO of guaiacol. Catechol is the main product from guaiacol in the presence of sulphur.
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Thanamongkollit, Narin. « Modification of Tung Oil for Bio-Based Coating ». University of Akron / OhioLINK, 2008. http://rave.ohiolink.edu/etdc/view?acc_num=akron1218080747.

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Livres sur le sujet "Bio-oil"

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Gnanasekaran, Dhorali, et Venkata Prasad Chavidi. Vegetable Oil based Bio-lubricants and Transformer Fluids. Singapore : Springer Singapore, 2018. http://dx.doi.org/10.1007/978-981-10-4870-8.

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Malaysia, Lembaga Minyak Sawit, dir. Proceedings of chemistry, processing technology & bio-energy conference : PIPOC 2011 International Palm Oil Congress. Kuala Lumpur, Malaysia : Malaysian Palm Oil Board, Ministry of Plantation Industries and Commodities, Malaysia, 2011.

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Malaysia, Lembaga Minyak Sawit, dir. Proceedings of chemistry, processing technology & bio energy conference : PIPOC 2009 International Palm Oil Congress, palm oil, balancing ecologics with economics. Kuala Lumpur, Malaysia : Malaysian Palm Oil Board, 2009.

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EU-Canada Workshop on Thermal Biomass Processing (2nd 1996). Bio-oil production & utilisation : Proceedings of the 2nd EU-Canada Workshop on Thermal Biomass Processing. Newbury : CPL Press for CANMET Energy, Mines and Resources Canada and European Commission, 1996.

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Ismailov, Nariman. Scientific basis of environmental biotechnology practical. ru : INFRA-M Academic Publishing LLC., 2020. http://dx.doi.org/10.12737/1048434.

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The monograph is devoted to modern biotechnology, which allows to solve urgent environmental problems in all areas of modern society. Described the current use of biotechnological methods for environmental protection. The common assessment of the environment, the analysis bioaccumulating capacity of the biosphere, presented information on bio-ecological potential of human society. Considers the issues of technological bio-energetics, obtaining biodegradable materials, different fields of organic waste, bioremediation of soils contaminated with petroleum products, pesticides, heavy metals, solid waste processing, utilization of oil sludge and drill cuttings, cleaning of soil and groundwater from contamination, the use of biotechnology in the oil industry and others Described the modern problems of organic agriculture and the progress in this area. Discussed microbiological, biochemical and technological fundamentals of these processes. The prospects of the use of biotechnology in integrated environmental protection. Discusses the modern view of ecological culture and ecological civilization in the framework of the problems under consideration. Designed for teachers, students, engineers, ecologists, agricultural workers, civil servants, decision-makers, engaged in the manufacture engaged in the development of programs for socio-ecological sustainable development.
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McNicoll, Dan M. Bio-remediation of petroleum-contaminated soils : An innovative, environmentally friendly technology. Ottawa : Ministry of Supply and Services, 1995.

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Koppelaar, Rembrandt, et Willem Middelkoop. The Tesla Revolution. NL Amsterdam : Amsterdam University Press, 2017. http://dx.doi.org/10.5117/9789462982062.

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Though oil prices have been on a downward trajectory in recent months, that doesn't obscure the fact that fossil fuels are finite, and we will eventually have to grapple with the end of their dominance. At the same time, however, skepticism about the alternatives remains: we've never quite achieved the promised 'too cheap to meter' power of the future, be it nuclear, solar, or wind. And hydrogen and bio-based fuels are thus far a disappointment. So what does the future of energy look like? The Tesla Revolution has the answers. In clear, unsensational style, Willem Middelkoop and Rembrandt Koppelaar offer a layman's tour of the energy landscape, now and to come. They show how rapid technological advances in batteries and solar technologies are already driving large-scale transformations in power supply, while economic and geopolitical changes, combined with a growing political awareness that there are alternatives to fossil fuels will combine in the coming years to bring an energy revolution ever closer. Within in our lifetimes, the authors argue, we will see changes that will reshape economics, the balance of political power, and even the most mundane aspects of our daily lives. Determinedly forward-looking and optimistic, though never straying from hard facts, The Tesla Revolution paints a striking picture of our global energy future.
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Bridgwater, A. V. Bio-oil Production and Utilisation. CPL Press, 1996.

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Bio-Based Plant Oil Polymers and Composites. Elsevier, 2016. http://dx.doi.org/10.1016/c2014-0-02157-0.

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Zhang, Chaoqun, Michael R. Kessler et Samy Madbouly. Bio-Based Plant Oil Polymers and Composites. Elsevier Science & Technology Books, 2015.

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Chapitres de livres sur le sujet "Bio-oil"

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No, Soo-Young. « Bio-Oil and Pyrolytic Oil ». Dans Application of Liquid Biofuels to Internal Combustion Engines, 181–219. Singapore : Springer Singapore, 2019. http://dx.doi.org/10.1007/978-981-13-6737-3_5.

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Sanna, Aimaro, et Nur Adilah Abd Rahman. « Conversion of Microalgae Bio-oil into Bio-diesel ». Dans Algal Biorefineries, 493–510. Cham : Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-20200-6_16.

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Kedir, Miftah F. « Pyrolysis Bio-oil and Bio-char Production from Firewood Tree Species for Energy and Carbon Storage in Rural Wooden Houses of Southern Ethiopia ». Dans African Handbook of Climate Change Adaptation, 1313–29. Cham : Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-45106-6_183.

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AbstractThe need for emission reduction for climate management had triggered the application of pyrolysis technology on firewood that yield bio-oil, bio-char, and syngas. The purpose of present study was to select the best bio-oil and bio-char producing plants from 17 firewood tree species and to quantify the amount of carbon storage. A dried and 1 mm sieved sample of 150 g biomass of each species was pyrolyzed in assembled setup of tubular furnace using standard laboratory techniques. The bio-oil and bio-char yields were 21.1–42.87% (w/w) and 23.23–36.40% (w/w), respectively. The bio-oil yield of Acacia seyal, Dodonea angustifolia, Euclea schimperi, Eucalyptus globulus, Casuarina equisetifolia, and Grevillea robusta were over 36% (w/w), which make the total yield of bio-oil and bio-char over 62% (w/w) of the biomass samples instead of the 12% conversion efficiency in traditional carbonization. The calorific value of firewood was 16.31–19.66 MJ kg–1 and bio-oil was 23.3–33.37 MJ kg–1. The use of bio-oil for household energy and bio-char for carbon storage reduced end use emission by 71.48–118.06%, which could increase adaptation to climate change in comparison to open stove firewood by using clean fuel and reducing indoor pollution.
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Oasmaa, Anja. « CHAPTER 8. Bio-Oil Stabilization ». Dans Green Chemistry Series, 138–59. Cambridge : Royal Society of Chemistry, 2017. http://dx.doi.org/10.1039/9781788010245-00138.

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Kumar, R., et V. Strezov. « Thermochemical Production of Bio-Oil ». Dans Biowaste and Biomass in Biofuel Applications, 197–266. Boca Raton : CRC Press, 2023. http://dx.doi.org/10.1201/9781003265597-9.

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Nithiya, K., P. Subramanian, D. Praveen Kumar, P. Komalabharathi et V. Karuppasamy Vikraman. « Bio-Oil : A Green Biofuel ». Dans Encyclopedia of Green Materials, 1–9. Singapore : Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-16-4921-9_106-1.

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Forghani, Amir Ahmad, David M. Lewis et Phillip Pendleton. « Catalytic Hydro-Cracking of Bio-Oil to Bio-Fuel ». Dans Biodegradation and Bioconversion of Hydrocarbons, 205–23. Singapore : Springer Singapore, 2016. http://dx.doi.org/10.1007/978-981-10-0201-4_6.

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Cabrera, Ever Estrada, Jayanta Kumar Patra et Maria del Pilar Rodriguez-Torres. « Biotechnological-Based Production of Bio-Oil and Vegetable Oil ». Dans Interdisciplinary Biotechnological Advances, 95–109. Singapore : Springer Nature Singapore, 2023. http://dx.doi.org/10.1007/978-981-19-9187-5_6.

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Zhang, Qi, Tiejun Wang et Chuangzhi Wu. « Upgrading Bio-Oil by Catalytic Esterification ». Dans Proceedings of ISES World Congress 2007 (Vol. I – Vol. V), 2372–77. Berlin, Heidelberg : Springer Berlin Heidelberg, 2008. http://dx.doi.org/10.1007/978-3-540-75997-3_479.

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Dwivedi, Naveen, et Shubha Dwivedi. « Bio-Oil Production from Algal Feedstock ». Dans Liquid Biofuel Production, 351–71. Hoboken, NJ, USA : John Wiley & Sons, Inc., 2019. http://dx.doi.org/10.1002/9781119459866.ch11.

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Actes de conférences sur le sujet "Bio-oil"

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Bahri, Syaiful, Edy Saputra, Irene Detrina, Yusnitawati et Muhdarina. « Bio oil from palm oil industry solid waste ». Dans International Conference on Energy and Sustainable Development : Issues and Strategies (ESD 2010). IEEE, 2010. http://dx.doi.org/10.1109/esd.2010.5598783.

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Al-abbas, Mustafa Hamid, Wan Aini Wan Ibrahim et Mohd Marsin Sanagi. « Recycling used palm oil and used engine oil to produce white bio oil, bio petroleum diesel and heavy fuel ». Dans INTERNATIONAL CONFERENCE ON FUNDAMENTAL AND APPLIED SCIENCES 2012 : (ICFAS2012). AIP, 2012. http://dx.doi.org/10.1063/1.4757466.

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Daniel P Geller, Manuel Garcìa-Pérez, John W Goodrum, Keshav C Das et Brian P Bibens. « Multicomponent Bio-oil/Biodiesel Based Fuels ». Dans 2009 Reno, Nevada, June 21 - June 24, 2009. St. Joseph, MI : American Society of Agricultural and Biological Engineers, 2009. http://dx.doi.org/10.13031/2013.27448.

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Shimanskaya, Elena. « BIO-OIL UPGRADING OVER HYDROTHERMAL CATALYSTS ». Dans 19th SGEM International Multidisciplinary Scientific GeoConference EXPO Proceedings. STEF92 Technology, 2019. http://dx.doi.org/10.5593/sgem2019/4.1/s17.008.

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Yin, Qianqian, Shurong Wang, Xinbao Li, Zuogang Guo et Yueling Gu. « Review of Bio-oil Upgrading Technologies and Experimental Study on Emulsification of Bio-oil and Diesel ». Dans 2010 International Conference on Optoelectronics and Image Processing (ICOIP). IEEE, 2010. http://dx.doi.org/10.1109/icoip.2010.112.

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Ardhayanti, Lutfia Isna, et Imam Sahroni. « Bio-char and bio-oil as slow pyrolysis product from agricultural waste ». Dans PROCEEDINGS OF THE 3RD INTERNATIONAL SEMINAR ON METALLURGY AND MATERIALS (ISMM2019) : Exploring New Innovation in Metallurgy and Materials. AIP Publishing, 2020. http://dx.doi.org/10.1063/5.0002696.

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Zhang, Jixiang, Zhongyang Luo, Qi Dang, Jun Wang et Wen Chen. « Upgrading of bio-oil in supercritical ethanol ». Dans 2011 International Conference on Electronics, Communications and Control (ICECC). IEEE, 2011. http://dx.doi.org/10.1109/icecc.2011.6067948.

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AL YAQOOBI, ATHEER, DAVID HOGG et WILLIAM B. « Microbubble Distillation of Bio oil Model Components ». Dans Third International Conference on Advances in Bio-Informatics, Bio-Technology and Environmental Engineering- ABBE 2015. Institute of Research Engineers and Doctors, 2015. http://dx.doi.org/10.15224/978-1-63248-060-6-06.

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Khumsak, Onarin, Weerapong Wattananoi et Nakorn Worasuwannarak. « Bio-oil production from the torrefied biomass ». Dans 2011 IEEE Conference on Clean Energy and Technology (CET). IEEE, 2011. http://dx.doi.org/10.1109/cet.2011.6041438.

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Jang, Na Ri, et Beom Soo Kim. « Bio-based Polymer Networks from Vegetable Oil ». Dans 14th Asia Pacific Confederation of Chemical Engineering Congress. Singapore : Research Publishing Services, 2012. http://dx.doi.org/10.3850/978-981-07-1445-1_206.

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Rapports d'organisations sur le sujet "Bio-oil"

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Evans, R. J., S. Czernik, R. French et K. Magrini. Distributed Bio-Oil Reforming. Office of Scientific and Technical Information (OSTI), mai 2005. http://dx.doi.org/10.2172/15016869.

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Resasco, Daniel, Lance Lobban, Steven Crossley, Vikas Khanna, Christos Maravelias, Lucia Petkovic et Nhung Duong. Fractionation and catalytic upgrading of bio-oil. Office of Scientific and Technical Information (OSTI), janvier 2018. http://dx.doi.org/10.2172/1417911.

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David J. Muth, Jake Jacobson, Kara Cafferty et Rober. Feedstock Pathways for Bio-oil and Syngas Conversi. Office of Scientific and Technical Information (OSTI), mars 2013. http://dx.doi.org/10.2172/1107262.

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Butcher, T. A., R. Trojanowski, O. Mante, G. Wei, Y. Celebi et J. Huber. Bio-Oil Deployment in the Home Heating Market. Office of Scientific and Technical Information (OSTI), juillet 2016. http://dx.doi.org/10.2172/1389226.

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Elangovan, S., Douglas C. Elliott, Daniel Santosa, Sabrina Spatari et Mukund Karanjikar. Novel Electro-Deoxygenation Process for Bio-oil Upgrading. Office of Scientific and Technical Information (OSTI), juin 2018. http://dx.doi.org/10.2172/1458768.

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Warrington, G., Jim Keiser et Raynella Connatser. Corrosion Studies of Pine-Derived Bio-Oil and Heavy Fuel Oil Blends. Office of Scientific and Technical Information (OSTI), février 2020. http://dx.doi.org/10.2172/1632093.

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Tews, Iva J., et Douglas C. Elliott. Low-Severity Hydroprocessing to Stabilize Bio-oil : TechnoEconomic Assessment. Office of Scientific and Technical Information (OSTI), août 2014. http://dx.doi.org/10.2172/1227072.

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Abdullah, Zia, Brad Chadwell, Rachid Taha, Barry Hindin et Kevin Ralston. Upgrading of Intermediate Bio-Oil Produced by Catalytic Pyrolysis. Office of Scientific and Technical Information (OSTI), juin 2015. http://dx.doi.org/10.2172/1209232.

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Brown, Robert C., Ryan Smith, Mark Wright, Douglas Elliott, Daniel Resasco et Steven Crossley. Stabilization of Bio-Oil Fractions for Insertion into Petroleum Refineries. Office of Scientific and Technical Information (OSTI), septembre 2014. http://dx.doi.org/10.2172/1157587.

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Brown, Robert C., Terrence Meyer, Rodney Fox, Shankar Submramaniam, Brent Shanks et Ryan G. Smith. A Systems Approach to Bio-Oil Stabilization - Final Technical Report. Office of Scientific and Technical Information (OSTI), décembre 2011. http://dx.doi.org/10.2172/1055935.

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