Relevant bibliographies by topics / Liquid Fuel Production

Academic literature on the topic 'Liquid Fuel Production'

Author: Grafiati
Published: 10 December 2022
Last updated: 28 January 2023

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Journal articles on the topic "Liquid Fuel Production"

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Tsukahara, Kenichiro, and Shigeki Sawayama. "Liquid Fuel Production Using Microalgae." Journal of the Japan Petroleum Institute 48, no. 5 (2005): 251–59. http://dx.doi.org/10.1627/jpi.48.251.

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Badger, Phillip C., and Jacqueline D. Broder. "Ethanol Production from Food Processing Wastes." HortScience 24, no. 2 (April 1989): 227–32. http://dx.doi.org/10.21273/hortsci.24.2.227.

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Abstract Liquid fuels, the most versatile form of energy, primarily are produced from oil. They are subject to wide price fluctuations and critical shortages. Ethanol, which can be used as a liquid fuel or liquid fuel supplement, readily can be produced from starch and sugar feedstocks. Ethanol production from cellulosic sources or biomass can provide renewable, domestically produced fuel from the decentralized sources of U.S. farms and forests. Such production has other stategic implications for the United States, such as strengthening the farm economy, reducing vulnerability to oil boycotts, and reducing the amounts of dollars exported. More information is available on using ethanol in internal combustion engines than any other nonpetroleum-based liquid fuel. For these reasons, ethanol represents the best near-term choice for a liquid fuel from biomass.
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Dobó, Zsolt, Gergő Kecsmár, Zsófia Jakab, Gábor Nagy, and Tamás Koós. "Production of Liquid Hydrocarbons from Plastic Wastes." International Journal of Engineering and Management Sciences 4, no. 4 (December 12, 2019): 345–50. http://dx.doi.org/10.21791/ijems.2019.4.39.

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Thermal pyrolysis of HDPE, LDPE, PP and PS plastic wastes were performed in a batch reactor and the yields of pyrolysis oils and liquid transportation fuels prepared by atmospheric distillation were determined. The gasoline fractions were tested in a traditional spark-ignition engine without any modifications or fuel blending. Fuel consumption and exhaust gas emission (NOx, CO) were measured and compared to a commercial fuel (RON = 95). PS generated 70.5% gasoline range hydrocarbons from the solid waste, followed by PP with 42.1%, LDPE with 40.8% and HDPE with 37.3%. The fuel consumption was reduced by 9.1-9.4% in the case of PS compared to reference measurement. Reduction in fuel consumption was noticeable at HDPE, LDPE and PP as well. PS gasoline decreased by 91-96%, while HDPE, LDPE and PP more likely increased the CO emission of the engine compared to commercial gasoline. The results show that pyrolysis of plastic wastes is a promising method to generate value added liquid transportation fuels and reduce the footprint of waste accumulation in landfills.
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Ackerson, M. D., N. L. Johnson, M. Le, E. C. Clausen, and J. L. Gaddy. "Biosolubilization and liquid fuel production from coal." Applied Biochemistry and Biotechnology 24-25, no. 1 (March 1990): 913–28. http://dx.doi.org/10.1007/bf02920304.

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Yokoyama, Shin-ya, Akira Suzuki, Masanori Murakami, Tomoko Ogi, and Katsuya Koguchi. "LIQUID FUEL PRODUCTION FROM ETHANOL FERMENTATION STILLAGE." Chemistry Letters 15, no. 5 (May 5, 1986): 649–52. http://dx.doi.org/10.1246/cl.1986.649.

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Osipov, A. M., and T. G. Shendrik. "Production of synthetic liquid fuel from coals." Fuel and Energy Abstracts 37, no. 3 (May 1996): 179. http://dx.doi.org/10.1016/0140-6701(96)88485-2.

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Düz, Mehtap, and Gökmen ŞEKER. "CALCULATION OF FISSILE FUEL PRODUCTION IN SOME MINOR ACTINIDES BASED ON THORIUM." Euroasia Journal of Mathematics, Engineering, Natural & Medical Sciences 9, no. 20 (March 25, 2022): 1–5. http://dx.doi.org/10.38065/euroasiaorg.823.

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In this study, a hybrid reactor with fission fusion reaction was modeled. As a fluid in design; 10% ThC2 + 0.1-1% AmF3 + 89.9-89% Li20Sn80 and 10% ThC2 + 0.1-1% NpF4 + 89.9-89% Li20Sn80 molten salt was used. In the first liquid wall, second liquid wall and shield regions of the reactor, the fissile fuel production was calculated using the MCNPX-2.7.0. ENDF/B-VII.0 nuclear reaction cross section library was used for numerical calculations.
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Hafeez, Sanaa, George Manos, S. M. Al-Salem, Elsa Aristodemou, and Achilleas Constantinou. "Liquid fuel synthesis in microreactors." Reaction Chemistry & Engineering 3, no. 4 (2018): 414–32. http://dx.doi.org/10.1039/c8re00040a.

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Fukuzumi, Shunichi. "Production of Liquid Solar Fuels and Their Use in Fuel Cells." Joule 1, no. 4 (December 2017): 689–738. http://dx.doi.org/10.1016/j.joule.2017.07.007.

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Connor, Michael R., and Shota Atsumi. "Synthetic Biology Guides Biofuel Production." Journal of Biomedicine and Biotechnology 2010 (2010): 1–9. http://dx.doi.org/10.1155/2010/541698.

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The advancement of microbial processes for the production of renewable liquid fuels has increased with concerns about the current fuel economy. The development of advanced biofuels in particular has risen to address some of the shortcomings of ethanol. These advanced fuels have chemical properties similar to petroleum-based liquid fuels, thus removing the need for engine modification or infrastructure redesign. While the productivity and titers of each of these processes remains to be improved, progress in synthetic biology has provided tools to guide the engineering of these processes through present and future challenges.
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Dissertations / Theses on the topic "Liquid Fuel Production"

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Anders, Mark. "Technoeconomic modelling of coal conversion processes for liquid fuel production." Thesis, Aston University, 1991. http://publications.aston.ac.uk/10240/.

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Since the oil crisis of 1973 considerable interest has been shown in the production of liquid fuels from alternative sources. In particular processes utilizing coal as the feedstock have received considerable interest. These processes can be divided into direct and indirect liquefaction and pyrolysis. This thesis describes the modelling of indirect coal liquefaction processes for the purpose of performing technical and economic assessment of the production of liquid fuels from coal and lignite, using a variety of gasification and synthesis gas liquefaction technologies. The technologies were modeled on a 'step model' basis where a step is defined as a combination of individual unit operations which together perform a significant function on the process streams, such as a methanol synthesis step or a gasification and physical gas cleaning step. Sample results of the modelling, covering a wide range of gasifiers, liquid synthesis processes and products are presented in this thesis. Due to the large number of combinations of gasifier, liquid synthesis processes, products and economic sensitivity cases, a complete set of results is impractical to present in a single publication. The main results show that methanol is the cheapest fuel to produce from coal followed by fuel alcohol, diesel from the Shell Middle Distillate Synthesis process,gasoline from Mobil Methanol to Gasoline (MTG) process, diesel from the Mobil Methanol Olefins Gasoline Diesel (MOGD) process and finally gasoline from the same process. Some variation in production costs of all the products was shown depending on type of gasifier chosen and feedstock.
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Pastore, Andrea. "Syngas production from heavy liquid fuel reforming in inert porous media." Thesis, University of Cambridge, 2010. https://www.repository.cam.ac.uk/handle/1810/237704.

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In the effort to introduce fuel cell technology in the field of decentralized and mobile power generators, a hydrocarbon reformer to syngas seems to be the way for the market uptake. In this thesis, a potential technology is developed and investigated, in order to convert commercial liquid fuel (diesel, kerosene and biodiesel) to syngas. The fundamental concept is to oxidise the fuel in a oxygen depleted environment, obtaining hydrogen and carbon monoxide as main products of the reaction. In order to extend the flammability limit of hydrocarbon/air mixtures, the rich combustion experiments have been carried out in a two-layer porous medium combustor, which stabilises a flame at the matrix interface and recirculates the enthalpy of the hot products in order to enhance the reaction rates at ultra-rich equivalence ratio. This thesis demonstrates the feasibility of the concept, by exploring characteristic parameters for a compact, reliable and cost effective device. Specifically, a range of equivalence ratios, thermal loads and porous materials have been examined. n-heptane was successfully reformed up to an equivalence ratio of 3, reaching a conversion efficiency (based on the lower heating value of H2 and CO over the fuel input) up to 75% for a packed bed of alumina beads. Thermal loads from P=2 to 12 kW at phi=2.0 demonstrated that heat losses can be reduced to 10%.Similarly, diesel, kerosene and bio-diesel were reformed to syngas in a Zirconia foam burner with conversion efficiency over 60%. The effect of different burners, thermal loads and equivalence ratios have also been assessed for these commercial fuels, leading to equivalent conclusions. A preliminary attempt to reduce the content of CO and hydrocarbons in the reformate has been also performed using commercial steam reforming and water-gas shift reaction catalysts, obtaining encouraging results. Finally, soot emission has been assessed, demonstrating particle formation for all the fuels above phi=2.0, with biodiesel showingthe lowest soot formation tendency among all the fuels tested.
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Lott, Tawney. "A political economy analysis of liquid fuel production incentives in South Africa." Master's thesis, University of Cape Town, 2017. http://hdl.handle.net/11427/27233.

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The purpose of this study is to analyse the development of South Africa's liquid fuels industry from 1930s to the present and the various ways in which the state has extended subsidies and other measures of support to liquid fuels producers. The nature and extent of government support to the South African liquid fuels industry has remained hidden for many years, due to the veil of secrecy surrounding the industry prior to the country's transition to democracy. The study expands past analyses to identify and estimate the magnitude of subsidies to liquid fuels production in South Africa in the present. Using the historical institutional approach, the study then places these measures of support in the South African political economy environment so as to understand the institutional barriers to their reform. In doing so, the study sheds light on the drivers informing the endurance of the liquid fuels subsidy regime and state support to the liquid fuels industry following the transition to democracy.
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Comidy, Liam Jacob Frank First Lieutenant. "Technical, economic, and environmental assessment of liquid jet fuel production on aircraft carriers." Thesis, Massachusetts Institute of Technology, 2019. https://hdl.handle.net/1721.1/122407.

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Thesis: S.M., Massachusetts Institute of Technology, Department of Aeronautics and Astronautics, 2019
Cataloged from PDF version of thesis.
Includes bibliographical references (pages 50-54).
This work is a first order assessment of the technical feasibility and characteristics of technologies to produce fuel onboard aircraft carriers, which is of interested to the United States Navy. They are interested because the logistical burden and supply chain required for delivering fuel at sea is dangerous, expensive, and subject to changes in markets price for liquid fuels. This work is a first order assessment of the technical feasibility and characteristics of technologies to produce fuel onboard aircraft carriers. The plant is evaluated for three technology pathways: Alkaline electrolysis and the reverse water gas shift (AE+RWGS), solid oxide electrolysis and RWGS (SOEC+RWGS), and co-electrolysis of steam and CO₂. They are evaluated within two scenarios: a small infrequently operating plant leveraging excess nuclear power (Scenario A) and a large frequently operating plant with dedicated nuclear capacity.
In addition, a parameter sweep of fuel production capacity and capacity factor is conducted to assess impacts on fuel production costs. In Scenario A, the energy requirements ranged from 152-22OMWe and fuel production cost ranged from 1.91-4.49$/L. In Scenario B, the energy requirements ranged in 1380-2066MWe and fuel production costs ranged from 3.25-4.23$/L. In both scenarios, AE+RWGS was the most cost effective and co-electrolysis was the most energy efficient. The fuel produced reduced lifecycle CO₂ equivalent emissions by 85.3-90.2%. The plant volume and weight were 50-67% and 432% of a current aircraft carrier design at large scales. The results of the parameter sweep indicate that generally a larger more frequently operating plant is more cost effective, but dedicated nuclear capacity requirements diminishes this benefit.
The overall results indicate that a fuel production plant on an aircraft carrier is technically feasible and has the potential to be cost effective, though research into cost, weight, and volume reduction are still necessary.
by Liam Jacob Frank Comidy.
S.M.
S.M. Massachusetts Institute of Technology, Department of Aeronautics and Astronautics
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Zhang, Yusheng. "Development of a bench scale single batch biomass to liquid fuel facility." Thesis, University of Fort Hare, 2014. http://hdl.handle.net/10353/811.

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The research described in this dissertation was motivated by the global demand for energy that is not dependent on coal, oil, natural gas and other non-renewable fossil fuels. The technology used in this project is related to the use of biomass to produce a viable alternative to conventional sources of fuel. A bench scale biomass to liquid (BTL) facility was built and tested. This produced results confirming the feasibility of the BTL process. The findings of the pilot study outlined in this dissertation justified the conclusion that the next step will be to expand the capacity and productivity of the BTL pilot plant to an industrial scale. Biomass comes from a variety of renewable sources that are readily available. In this case, the material used in the fixed bed biomass gasification facility to generate wood gas was agricultural and forestry waste, such as straw and wood chips. The gasifier had the capacity to produce up to 10 cubic metres/hr of gas with a carbon monoxide and hydrogen content of between 20–40% by volume, when it was operated at ambient pressure and with air as the oxidizer. The gas, produced at a temperature above 700º C, was cooled in a quench/water scrubber in order to remove most of the mechanical impurities (tars and water-soluble inorganic particles), condensed and dried with corn cobs before being compressed in cylinders at over 100 bar (g) for use in the Fischer-Tropsch Synthesis (FTS). The syngas was subjected further to a series of refining processes which included removal of sulphur and oxygen. The sulphur removal technology chosen entailed applying modified activated carbon to adsorb H2S with the help of hydrolysis in order to convert organic sulphur impurities into H2S which reduced the sulphur content of the gas to less than 5 ppbv. Supported cobalt catalyst (100 grams), were loaded into a single-tube fixed bed FT reactor with an inner diameter of 50 mm. The reactor was fitted with a heating jacket through which, heated oil ran to cool the reactor during a normal reaction occurring at < 250 ºC, while nitrogen was used in the heating jacket during reduction, which occurred at temperatures up ~ 350 ºC. The FTS reaction was carried out at different pressures and temperatures. Liquid and wax products were produced from the facility. The properties of the liquid and solid hydrocarbons produced were found to be the same as FT products from other feed stocks, such as natural gas and coal.
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Chetty, Thamaraveni. "Factors influencing the success of ethanol production for use in liquid transport fuels in South Africa." Diss., University of Pretoria, 2007. http://hdl.handle.net/2263/23815.

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Against the backdrop of rising fuel prices and increasing demand for transport fuels, coupled with government’s imperative to reduce high unemployment levels by developing the agricultural sector to support a bio-fuels sector, it was considered necessary to conduct research to determine the factors that would influence the success of bio-ethanol production for use in liquid transport fuels. The literature review highlighted five key factors that were developed into research questions to establish whether these factors are relevant to the South African context and which are considered more important. The research was conducted using a combination of face-to-face interviews and telephonic interviews to gather opinions from 16 subject matter experts in the field of bio-fuels. A questionnaire was used to drill down into each of the factors individually, to determine the importance of that factor as it relates to bio-ethanol production. The findings reveal that the absence of clear and sound government policy poses the biggest hindrance to the establishment of the industry. Furthermore, that agricultural development is a major factor for the success of bio-ethanol production as the industry is dependant on the availability of competitive feed stocks in order to be sustainable. Finally, that job creation is the motivating factor for the establishment of the industry since it addresses a government imperative to reduce unemployment levels in South Africa.
Dissertation (MBA)--University of Pretoria, 2007.
Gordon Institute of Business Science (GIBS)
unrestricted
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Al-Harrasi, Wail Saif Salim. "Novel plasma catalytic systems for Fischer-Tropsch reactions : intensified gas-to-liquid fuel production." Thesis, University of Newcastle Upon Tyne, 2011. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.578549.

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One of the impacts of climate change is the emergence of food, energy and water shortages which can be circumvented through intensified technologies in agriculture, energy and chemical/biological processes. Furthermore, depleting fossil fuel reserves requires the establishment of alternative sustainable energy resources. Biomass based energy and chemicals technology is an important component of sustainable development which can be integrated with food and water generation. However, due to distributed nature of biomass, biomass based energy technology needs to be distributed generation which would benefit from low temperature and pressure operation. Syngas produced from gasification of waste/biomass can be. converted to power or liquid fuel after cleaning. Although process intensification (PI) is still in its infancy, potentially, it is highly suitable for the distributed production of power and liquid fuels. The objective of this study is to develop a syngas-to-liquid fuel conversion process suitable for distributed production using principles of PI through the intensification of Fischer Tropsch Synthesis (FTS). The first approach was by using structured catalysts in monolithic forms for FTS. The second approach was to couple the structured catalyst with non thermal plasma by using dielectric barrier discharge (DBD) in hybrid FTS reactors. A hybrid reactor was designed and fabricated to test this novel catalytic system. Co and Co/Cu catalysts were prepared and characterised using scanning electron microscopy, energy dispersive X-ray spectroscopy, X-ray diffraction and transmission electron microscopy. The reactor was used in the FTS using H, and CO under various processing conditions (temperature, pressure, Hz/CO molar ratio, gas flowrate and plasma power) and the products were analysed using gas chromatography. It is shown that Co/Cu catalyst in plasma assisted FTS was feasible, converting up to 38% of CO at 90W, 1 bar, Hz/CO= 2, 25ml/min and 25°C. This conversion was obtained at 230°C and 6 bar in conventional FTS. This research showed that DBD in FTS enables running the reaction at room temperature and atmospheric pressure avoiding the risks and costs associated with high pressure processes. It was also shown that plasma affected the activity of the catalysts, preventing it from agglomeration.
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Chang, Ai-Fu. "Process Modeling of Next-Generation Liquid Fuel Production - Commercial Hydrocracking Process and Biodiesel Manufacturing." Diss., Virginia Tech, 2011. http://hdl.handle.net/10919/58043.

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This dissertation includes two process modeling studies -- (1) predictive modeling of large-scale integrated refinery reaction and fractionation systems from plant data – hydrocracking process; and (2) integrated process modeling and product design of biodiesel manufacturing. \r\n1. Predictive Modeling of Large-Scale Integrated Refinery Reaction and Fractionation Systems from Plant Data -- Hydrocracking Processes: This work represents a workflow to develop, validate and apply a predictive model for rating and optimization of large-scale integrated refinery reaction and fractionation systems from plant data. We demonstrate the workflow with two commercial processes -- medium-pressure hydrocracking unit with a feed capacity of 1 million ton per year and high-pressure hydrocracking unit with a feed capacity of 2 million ton per year in the Asia Pacific. This work represents the detailed procedure for data acquisition to ensure accurate mass balances, and for implementing the workflow using Excel spreadsheets and a commercial software tool, Aspen HYSYS from Aspen Technology, Inc. The workflow includes special tools to facilitate an accurate transition from lumped kinetic components used in reactor modeling to the boiling point based pseudo-components required in the rigorous tray-by-tray distillation simulation. Two to three months of plant data are used to validate models' predictability. The resulting models accurately predict unit performance, product yields, and fuel properties from the corresponding operating conditions.\r\n2. Integrated Process Modeling and Product Design of Biodiesel Manufacturing: This work represents first a comprehensive review of published literature pertaining to developing an integrated process modeling and product design of biodiesel manufacturing, and identifies those deficient areas for further development. It also represents new modeling tools and a methodology for the integrated process modeling and product design of an entire biodiesel manufacturing train. We demonstrate the methodology by simulating an integrated process to predict reactor and \r\nseparator performance, stream conditions, and product qualities with different feedstocks. The results show that the methodology is effective not only for the rating and optimization of an existing biodiesel manufacturing, and but also for the design of a new process to produce biodiesel with specified fuel properties.
Ph. D.
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Loegel, Thomas N. "High Performance Liquid Chromatography of Petroleum Asphaltenes and Capillary Electrophoresis of Glycosaminoglycan Carbohydrates." Miami University / OhioLINK, 2012. http://rave.ohiolink.edu/etdc/view?acc_num=miami1354241855.

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Duangsuwan, Wiriya. "Experimental studies of the mixing of alcohols with vegetable oil using gas-liquid compound drops for applications in bio-fuel production." Thesis, University of Surrey, 2010. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.521716.

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Books on the topic "Liquid Fuel Production"

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Peschka, Walter. Liquid Hydrogen: Fuel of the Future. Vienna: Springer Vienna, 1992.

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Anders, Mark. Technoeconomic modelling of coal conversion processes for liquid fuel production. Birmingham: Aston University. Department of Chemical Engineering and Applied Chemistry, 1991.

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Kerstetter, James D. Wheat straw for ethanol production in Washington: a resource, technical, and economic assessment. Olympia, WA: Washington State University, Cooperative Extension Energy Program, 2001.

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Bridgwater, A. V. Technical and economic modelling of processes for liquid fuel production in Europe. Luxembourg: Commission of the European Communities, 1991.

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Liquid fuels: Types, properties, and production. Hauppauge, N.Y: Nova Science Publishers, 2011.

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Chenoweth, Mary E. Two concepts in the production of liquid fossil fuels. Santa Monica, CA: Rand Corp., 1987.

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Klerk, Arno de. Synthetic liquids production and refining. Washington, DC: American Chemical Society, 2011.

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Sidorenko, Oleg. Biological systems in the processing of secondary products and agricultural waste. ru: INFRA-M Academic Publishing LLC., 2021. http://dx.doi.org/10.12737/1102076.

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The manual describes technologies for processing secondary products and agricultural waste using macro-and micro-organisms. The regulations of modern biotechnologies of microbial synthesis, bioconversion of secondary raw materials are briefly presented, methods of its processing and characteristics of the obtained target products of bioconversion are described. Practical classes introduce students to modern methods of improving environmental quality and production waste from commercial products (organic fertilizers, bacterial preparations, feed additives, etc.), as well as obtain the cheapest fuel and energy resources (biogas, alcohols, acids, liquid biofuels, etc.). Meets the requirements of Federal state educational standards of higher education of the last generation. It is intended for students of higher educational institutions of technological specialties.
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Oakey, John. Fuel Flexible Energy Generation: Solid, Liquid and Gaseous Fuels. Elsevier Science & Technology, 2015.

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Fuel Flexible Energy Generation: Solid, Liquid and Gaseous Fuels. Woodhead Publishing, 2015.

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Book chapters on the topic "Liquid Fuel Production"

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Shadangi, Krushna Prasad, and Kaustubha Mohanty. "Effect of Upgrading Techniques on Fuel Properties and Composition of Bio-Oil." In Liquid Biofuel Production, 373–85. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2019. http://dx.doi.org/10.1002/9781119459866.ch12.

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Pattanayak, Satarupa, Nirupama Prasad, and Sumit Kumar Jana. "Recycle of Plastic Waste to Liquid Fuel: A Sustainable Energy Production." In Clean Energy Production Technologies, 51–66. Singapore: Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-16-9135-5_3.

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Yokoyama, Shin-Ya, Tomoko Ogi, Katsuya Koguchi, Tomoaki Minowa, Masanori Murakami, and Akira Suzuki. "Liquid Fuel Production from Ethanol Fermentation Stillage by Thermochemical Conversion." In Research in Thermochemical Biomass Conversion, 792–803. Dordrecht: Springer Netherlands, 1988. http://dx.doi.org/10.1007/978-94-009-2737-7_60.

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Rajeswari, Gunasekaran, Samuel Jacob, and Rintu Banerjee. "Perspective of Liquid and Gaseous Fuel Production from Aquatic Energy Crops." In Sustainable Biofuel and Biomass, 167–82. Includes bibliographical references and index: Apple Academic Press, 2019. http://dx.doi.org/10.1201/9780429265099-9.

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Wang, Tiejun, Chenguang Wang, Qi Zhang, Chuangzhi Wu, and Longlong Ma. "Catalytic Reforming of Biomass Raw Fuel Gas to Syngas for FT Liquid Fuels Production." In Proceedings of ISES World Congress 2007 (Vol. I – Vol. V), 2366–71. Berlin, Heidelberg: Springer Berlin Heidelberg, 2008. http://dx.doi.org/10.1007/978-3-540-75997-3_478.

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Ruggeri, Bernardo, Tonia Tommasi, and Sara Sanfilippo. "Valorization of Liquid End-Residues of H2 Production by Microbial Fuel Cell." In BioH2 & BioCH4 Through Anaerobic Digestion, 137–59. London: Springer London, 2015. http://dx.doi.org/10.1007/978-1-4471-6431-9_7.

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Townsend, Jason M., Charles A. S. Hall, Timothy A. Volk, David Murphy, Godfrey Ofezu, Bobby Powers, Amos Quaye, and Michelle Serapiglia. "Energy Return on Investment (EROI), Liquid Fuel Production, and Consequences for Wildlife." In Peak Oil, Economic Growth, and Wildlife Conservation, 29–61. New York, NY: Springer New York, 2014. http://dx.doi.org/10.1007/978-1-4939-1954-3_2.

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Rominiyi, O. L., O. M. Ikumapayi, E. O. Orumwense, O. S. Fatoba, and E. T. Akinlabi. "Design and Fabrication of a Gasifier for the Production of Liquid Fuel—A Case Study of Spondias mombin." In Lecture Notes in Mechanical Engineering, 131–45. Singapore: Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-19-3307-3_12.

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Bhattacharya, Sourish, Surajbhan Sevda, Pooja Bachani, Pooja Bachani, Vamsi Bharadwaj, Vamsi Bharadwaj, and Sandhya Mishra. "Waste Biomass Utilization for Liquid Fuels: Challenges & Solution." In Liquid Biofuel Production, 73–87. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2019. http://dx.doi.org/10.1002/9781119459866.ch3.

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Chen, Wei Ning, and Jiahua Shi. "Microbial Production of Liquid Biofuels through Metabolic Engineering." In Microbial Fuels, 353–78. Boca Raton : CRC Press, [2018]: CRC Press, 2017. http://dx.doi.org/10.1201/9781351246101-10.

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Conference papers on the topic "Liquid Fuel Production"

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Shcheklein, Sergey. "PRODUCTION OF LIQUID FUEL FROM WOOD." In 19th SGEM International Multidisciplinary Scientific GeoConference EXPO Proceedings. STEF92 Technology, 2019. http://dx.doi.org/10.5593/sgem2019/4.1/s17.052.

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Najser, Jan, Václav Peer, and Martin Vantuch. "Biomass gasification for liquid fuel production." In XIX. THE APPLICATION OF EXPERIMENTAL AND NUMERICAL METHODS IN FLUID MECHANICS AND ENERGETICS 2014: Proceedings of the International Conference. AIP Publishing LLC, 2014. http://dx.doi.org/10.1063/1.4892710.

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Tuly, S. S., Md Momen Shahriar Joarder, and Md Enamul Haque. "Liquid fuel production by pyrolysis of polythene and PET plastic." In 8TH BSME INTERNATIONAL CONFERENCE ON THERMAL ENGINEERING. AIP Publishing, 2019. http://dx.doi.org/10.1063/1.5115938.

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Arahim, Andry Anggoro, Widayat, and Hadiyanto. "Liquid fuel production from motorized vehicle tires with pirolysis process." In INTERNATIONAL CONFERENCE ON SCIENCE AND APPLIED SCIENCE (ICSAS2020). AIP Publishing, 2020. http://dx.doi.org/10.1063/5.0030380.

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Barbosa, Fábio Coelho. "Power to Liquid (PtL) Synthetic Aviation Fuel - A Sustainable Pathway for Jet Fuel Production." In SAE BRASIL 2021 Web Forum. 400 Commonwealth Drive, Warrendale, PA, United States: SAE International, 2022. http://dx.doi.org/10.4271/2021-36-0034.

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Chudnovsky, B., L. Levin, A. Talanker, A. Kunin, J. Cohen, R. Harpaz, and J. Karni. "Advanced Power Plant Concept With Application of Exhaust CO2 to Liquid Fuel Production." In ASME 2017 Power Conference Joint With ICOPE-17 collocated with the ASME 2017 11th International Conference on Energy Sustainability, the ASME 2017 15th International Conference on Fuel Cell Science, Engineering and Technology, and the ASME 2017 Nuclear Forum. American Society of Mechanical Engineers, 2017. http://dx.doi.org/10.1115/power-icope2017-3037.

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Today there is a growing concern about the ramifications of global warming resulting from the use of fossil fuels and the associated carbon dioxide emissions. Oxy-fuel combustion is a promising response to this issue, since the product of the combustion is a CO2 rich flue gas, which requires no further separation from other emission gases and thus can be sequestrated, or utilized. Here we present an analysis of a novel technology for combining oxy-fuel combustion with utilization of the CO2 rich flue gas for syntetic fuel production. The technology concept involves a new method of using concentrated solar energy for the dissociation of carbon dioxide (CO2) to carbon monoxide (CO) and oxygen (O2). Simultaneously, the same device can dissociate water (H2O) to hydrogen (H2) and oxygen (O2). The CO, or the mixture of CO and H2 (called Syngas), can then be used as a gaseous fuel (e.g. in power plants), or converted to a liquid fuel (e.g. methanol), which is relatively easy to store and transport, and can be used in motor vehicles and electricity generation facilities. The oxygen produced in the process can be used in oxy-fuel combustion or other advanced combustion methods in power plants. In this study it is assumed that a typical sub-critical, 575 MW, coal firing power plant is converted to oxy-fuel combustion. The flue gases from that power plant are then used as raw material for fuel production. The aim of the study is to estimate the optimal conceptual design of a power generation plant, including liquid/gaseous fuel generation facility. In the present study we used a series of special models for simulating the heat balance, heat transfer, performance and emissions of an oxy-fuel converted utility boiler. We also employed cycle simulation software that facilitates the optimization of an electricity generation plant with CO2 conversion to liquid fuel and usage of the fuel produced from CO2 for additional electricity production. The simulation results show that the amount of fuel produced, additional power generated and power station self consumption may be changed over a wide range, depending on the size of the solar field, which provides the energy for the liquid fuel production. The paper includes an overview of some of the key technical considerations of the new concept of CO2 conversion to fuel. Based on the obtained results it may be concluded that the methodology presented in this study is an attractive option for CO2 emission reduction, which can be implemented in existing and/or new power generation units. The technology proposed in this paper is not indented as an alternative for replacing coal combustion with natural gas, however may be used effectively with oxy-fuel combustion of either coal or natural gas.
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Hawkes, G. L., J. E. O’Brien, and M. G. McKellar. "Liquid Bio-Fuel Production From Non-Food Biomass via High Temperature Steam Electrolysis." In ASME 2011 International Mechanical Engineering Congress and Exposition. ASMEDC, 2011. http://dx.doi.org/10.1115/imece2011-62588.

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Two hybrid energy processes that enable production of synthetic liquid fuels that are compatible with the existing conventional liquid transportation fuels infrastructure are presented. Using biomass as a renewable carbon source, and supplemental hydrogen from high-temperature steam electrolysis (HTSE), these two hybrid energy processes have the potential to provide a significant alternative petroleum source that could reduce US dependence on imported oil. The first process discusses a hydropyrolysis unit with hydrogen addition from HTSE. The second process discusses a process named Bio-Syntrolysis. The Bio-Syntrolysis process combines hydrogen from HTSE with CO from an oxygen-blown biomass gasifier that yields syngas to be used as a feedstock for synthesis of liquid transportation fuels via a Fischer-Tropsch process. Conversion of syngas to liquid hydrocarbon fuels, using a biomass-based carbon source, expands the application of renewable energy beyond the grid to include transportation fuels. It can also contribute to grid stability associated with non-dispatchable power generation. The use of supplemental hydrogen from HTSE enables greater than 90% utilization of the biomass carbon content which is about 2.5 times higher than carbon utilization associated with traditional cellulosic ethanol production. If the electrical power source needed for HTSE is based on nuclear or renewable energy, the process is carbon neutral. INL has demonstrated improved biomass processing prior to gasification. Recyclable biomass in the form of crop residue or energy crops would serve as the feedstock for this process. A process model of syngas production using high temperature electrolysis and biomass gasification is presented. Process heat from the biomass gasifier is used to heat steam for the hydrogen production via the high temperature steam electrolysis process. Oxygen produced form the electrolysis process is used to control the oxidation rate in the oxygen-blown biomass gasifier.
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Ahmad, Razi, Ragunathan Santiagoo, Norhafezah Kasmuri, Shamala Ramasamy, Nurul Nafizah Salim, and Nur Nasulhah Kasim. "Liquid fuel production from co-pyrolysis of rice husk and polystyrene waste mixture." In PROCEEDINGS OF 8TH INTERNATIONAL CONFERENCE ON ADVANCED MATERIALS ENGINEERING & TECHNOLOGY (ICAMET 2020). AIP Publishing, 2021. http://dx.doi.org/10.1063/5.0051563.

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Mrad, Nadia, Maria Paraschiv, Fethi Aloui, Mohand Tazerout, and Sassi Ben Nasrallah. "Production of Liquid Hydrocarbon Fuel by Catalytic Cracking of Waste Fish Fat in Continuous Pilot System." In ASME-JSME-KSME 2011 Joint Fluids Engineering Conference. ASMEDC, 2011. http://dx.doi.org/10.1115/ajk2011-17012.

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Liquid fuels can be produced from triglyceride sources via thermo-catalytic process. In the present work, the production of bio-fuel by catalytic cracking of waste fish fat in a continuous reactor at atmospheric pressure has been studied. Different catalysts were used and maximum bio-oil yield of 66% with the lowest acidity of 4.3 mgKOH/goil was obtained with a controlled reaction temperature of 500°C and Na2CO3 as a catalyst. After chemical treatment of this bio-oil, the acidity decreases to 1.5mgKOH/goil. These bio-fuels were characterized according to their physico-chemical properties, and compared with the diesel fuel. The results show that the catalytic cracking process represents an alternative method to produce bio-fuels with physico-chemical characteristics similar to petroleum fuels from fish oil industrial residues.
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Hinkley, James T., Robbie K. McNaughton, John Pye, Woei Saw, and Ellen B. Stechel. "The challenges and opportunities for integration of solar syngas production with liquid fuel synthesis." In SOLARPACES 2015: International Conference on Concentrating Solar Power and Chemical Energy Systems. Author(s), 2016. http://dx.doi.org/10.1063/1.4949205.

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Reports on the topic "Liquid Fuel Production"

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Feinberg, D., and M. Karpuk. CO sub 2 sources for microalgae-based liquid fuel production. Office of Scientific and Technical Information (OSTI), August 1990. http://dx.doi.org/10.2172/6588442.

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Thomas, K. P., and D. E. Hunter. The evaluation of a coal-derived liquid as a feedstock for the production of high-density aviation turbine fuel. Office of Scientific and Technical Information (OSTI), August 1989. http://dx.doi.org/10.2172/6286660.

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Kolodziejczyk, Bart. Unsettled Issues Concerning the Use of Green Ammonia Fuel in Ground Vehicles. SAE International, February 2021. http://dx.doi.org/10.4271/epr2021003.

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While hydrogen is emerging as a clean alternative automotive fuel and energy storage medium, there are still numerous challenges to implementation, such as the economy of hydrogen production and deployment, expensive storage materials, energy intensive compression or liquefaction processes, and limited trial applications. Synthetic ammonia production, on the other hand, has been available on an industrial scale for nearly a century. Ammonia is one of the most-traded commodities globally and the second most-produced synthetic chemical after sulfuric acid. As an energy carrier, it enables effective hydrogen storage in chemical form by binding hydrogen atoms to atmospheric nitrogen. While ammonia as a fuel is still in its infancy, its unique properties render it as a potentially viable candidate for decarbonizing the automotive industry. Yet, lack of regulation and standards for automotive applications, technology readiness, and reliance on natural gas for both hydrogen feedstocks to generate the ammonia and facilitate hydrogen and nitrogen conversion into liquid ammonia add extra uncertainty to use scenarios. Unsettled Issues Concerning the Use of Green Ammonia Fuel in Ground Vehicles brings together collected knowledge on current and future prospects for the application of ammonia in ground vehicles, including the technological and regulatory challenges for this new type of clean fuel.
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Furlong, M. W., J. D. Fox, J. G. Masin, and D. J. Soderberg. Production of jet fuel from coal-derived liquids. Office of Scientific and Technical Information (OSTI), January 1987. http://dx.doi.org/10.2172/6501866.

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Furlong, M., J. Fox, J. Masin, and D. Soderberg. Production of jet fuel from coal-derived liquids. Office of Scientific and Technical Information (OSTI), January 1990. http://dx.doi.org/10.2172/7159098.

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Furlong, M., J. Fox, and J. Masin. Production of jet fuel from coal-derived liquids. Office of Scientific and Technical Information (OSTI), January 1989. http://dx.doi.org/10.2172/6937238.

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Furlong, M., J. Fox, and J. Masin. Production of jet fuel from coal-derived liquids. Office of Scientific and Technical Information (OSTI), January 1988. http://dx.doi.org/10.2172/6893088.

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Furlong, M., J. Fox, and J. Masin. Production of jet fuel from coal-derived liquids. Office of Scientific and Technical Information (OSTI), January 1988. http://dx.doi.org/10.2172/6893074.

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Furlong, M., J. Fox, J. Masin, and D. Soderberg. Production of jet fuel from coal-derived liquids. Office of Scientific and Technical Information (OSTI), January 1988. http://dx.doi.org/10.2172/7159088.

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Johnson, R. W., W. C. Zackro, G. Czajkowski, P. P. Shah, and A. P. Kelly. Production of jet fuels from coal-derived liquids. Office of Scientific and Technical Information (OSTI), March 1989. http://dx.doi.org/10.2172/5088162.

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