Relevant bibliographies by topics / Light Naphtha

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  1. Journal articles
  2. Dissertations / Theses
  3. Book chapters
  4. Conference papers

Academic literature on the topic 'Light Naphtha'

Author: Grafiati
Published: 4 June 2021
Last updated: 5 February 2022

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Journal articles on the topic "Light Naphtha"

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Lengyel, A., S. Magyar, D. Kalló, and J. Hancsók. "Catalytic Coprocessing of Delayed Coker Light Naphtha with Light Straight-run Naphtha/FCC Gasoline." Petroleum Science and Technology 28, no. 9 (2010): 946–54. http://dx.doi.org/10.1080/10916460902937059.

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Chuzlov, Viacheslav A., Emilia D. Ivanchina, Igor’ M. Dolganov, and Konstantin V. Molotov. "Simulation of Light Naphtha Isomerization Process." Procedia Chemistry 15 (2015): 282–87. http://dx.doi.org/10.1016/j.proche.2015.10.045.

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Li, Dadong, Mingfeng Li, Yang Chu, Hong Nie, and Yahua Shi. "Skeletal isomerization of light FCC naphtha." Catalysis Today 81, no. 1 (2003): 65–73. http://dx.doi.org/10.1016/s0920-5861(03)00103-2.

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Valavarasu, G., and B. Sairam. "Light Naphtha Isomerization Process: A Review." Petroleum Science and Technology 31, no. 6 (2013): 580–95. http://dx.doi.org/10.1080/10916466.2010.504931.

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Kozlov, I. T., V. A. Khavkin, and B. K. Nefedov. "Selective hydrocracking of light naphtha cuts." Chemistry and Technology of Fuels and Oils 21, no. 7 (1985): 346–49. http://dx.doi.org/10.1007/bf00723841.

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M. Hussain, Halah, and Abdulhaleem A.K. Mohammed. "Experimental Study of Iraqi Light Naphtha Isomerization over Ni-Pt/H-Mordenite." Iraqi Journal of Chemical and Petroleum Engineering 20, no. 4 (2019): 61–66. http://dx.doi.org/10.31699/ijcpe.2019.4.10.

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Hydroisomerization of Iraqi light naphtha was studied on prepared Ni-Pt/H-mordenite catalyst at a temperature range of 220-300°C, hydrogen to hydrocarbon molar ratio of 3.7, liquid hourly space velocity (LHSV) 1 hr-1 and at atmospheric pressure.
 The result shows that the hydrisomerization of light naphtha increases with the increase in reaction temperature at constant LHSV. However, above 270 0C the isomers formation decreases and the reaction is shifted towards the hydrocracking reaction, a higher octane number of naphtha was formed at 270 °C.
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Cheng, Qi-tong, Ben-xian Shen, Hui Sun, Ji-gang Zhao, and Ji-chang Liu. "Methanol promoted naphtha catalytic pyrolysis to light olefins on Zn-modified high-silicon HZSM-5 zeolite catalysts." RSC Advances 9, no. 36 (2019): 20818–28. http://dx.doi.org/10.1039/c9ra02793a.

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Exploring the relationship between the properties and catalytic reactivity of the Zn-modified high-silicon ZSM-5 in the methanol/naphtha coupling reaction and achieving the efficient utilization of naphtha.
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Schmidt, Roland, M. Bruce Welch, and Bruce B. Randolph. "Oligomerization of C5Olefins in Light Catalytic Naphtha." Energy & Fuels 22, no. 2 (2008): 1148–55. http://dx.doi.org/10.1021/ef800005v.

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Vemot, E. H., R. T. Drew, and M. L. Kane. "Acute Toxicologic Evaluation of Light Alkyklate Naphtha." Journal of the American College of Toxicology 1, no. 2 (1990): 124. http://dx.doi.org/10.1177/109158189000100244.

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Hammadi, Ahmed Najeeb, and Ibtehal K. Shakir. "Adsorption Behavior of Light Naphtha Components on Zeolite (5A) and Activated Carbon." Iraqi Journal of Chemical and Petroleum Engineering 20, no. 4 (2019): 27–33. http://dx.doi.org/10.31699/ijcpe.2019.4.5.

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Light naphtha one of the products from distillation column in oil refineries used as feedstock for gasoline production. The major constituents of light naphtha are (Normal Paraffin, Isoparaffin, Naphthene, and Aromatic). In this paper, we used zeolite (5A) with uniform pores size (5Aº) to separate normal paraffin from light naphtha, due to suitable pore size for this process and compare the behavior of adsorption with activated carbon which has a wide range of pores size (micropores and mesopores) and high surface area. The process is done in a continuous system - Fixed bed reactor- at the vap
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Dissertations / Theses on the topic "Light Naphtha"

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SHIU, HAU-SHIANG, and 徐豪祥. "Upgrading of Light Naphtha." Thesis, 2009. http://ndltd.ncl.edu.tw/handle/18099383587263687050.

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碩士<br>國立中正大學<br>化學工程所<br>97<br>The goal of study is desulfide by absorbent .Application that π-complexation between nickel oxide and sulfide to achieve desulfurization. The adsorbent is prepared by zeolite and Ni(NO3)26H2O.After calcination,the structure of adsorbents were characterized by FT-IR(Fourier transform-Infrared spectroscopy),synchrotron XRD(X-ray diffraction) and XAS(X-ray adsorption spectroscopy).The desulfurization was tested by adsorption column under 14.7psig , room temperature,WHSV=0.8h-1,the feed concentration of benzothiophene in octane is 2000ppm.With the complementally char
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饒瑞孟. "Light Naphtha Isomerization Catalysts: Preparation, Characteration and Catalysis." Thesis, 1995. http://ndltd.ncl.edu.tw/handle/30955118944138297733.

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碩士<br>國立中正大學<br>化學工程研究所<br>83<br>The effects of catalyst preparation and pretreatment and the role of second metal, nickle, on the metal dispersion of mordenite-supported Pt catalysts and the resulting catalyst performance were investigated by examining CO chemisorption, octane barrel upgrading of n-pantane(C5) ,n-hexane (C6) and n-heptane (C7) isomerization, fuel gas formation of n-heptane (C7) hydrocracking, and. catalyst deactivation by sulfur poisoning. The test reactions were carried out with a continuous fixed-bed reaction system and the operation conditions were similar to those of a
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Chen, Zong-ying, and 陳宗盈. "Development of Methods for Nitrogen Removal from Light Naphtha." Thesis, 2006. http://ndltd.ncl.edu.tw/handle/17011493316766292538.

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碩士<br>國立中正大學<br>化學工程所<br>94<br>The present reseacch is related to a liquid-liquid extraction method and conception for removing nitrogen from the light petroleum oils to an ultra-low level and making them suitable as the feedstocks for the down stream catalytic processes, which use high performance zeolitic catalysts. The desirable reactions are catalyzed at the strong acidic sites of these catalysts, which are very vulnerable to poison from the basic nitrogen in the feedstock. This method is highly efficient in extracting contaminate of the basic nitrogen compounds from the C6 to C8 aromati
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Kuen-Yu, Tsai, and 蔡昆裕. "The Study of DI Diesel Engine Performance and Emissionin Blended Fuel Adding Light Naphtha in Bio-diesel." Thesis, 2003. http://ndltd.ncl.edu.tw/handle/84418505183360087378.

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碩士<br>國立臺北科技大學<br>車輛工程系碩士班<br>91<br>The purpose of this research is to reduce atmospheric pollution and extent the life of the petrol-diesel. This study used the blended fuel which was added light naphtha in bio-diesel to be a fuel in using diesel engine. In the experiment, It used blended fuel adding premium diesel in bio-diesel in the single cylinder direct injection diesel engine with under the condition of unchanged engine original design. The results of this experiment shows that the blended fuel fifty-fifty percent bio-diesel and light naphtha was worse than premium diesel for fuel consu
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Bárcia, Patrick da Silva. "Separation of light naphtha for the octane upgrading of gasoline : adsorption and membrane technologies and new adsorbents." Tese, 2010. http://hdl.handle.net/10216/58567.

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Lan, Chien-Chang, and 藍建昌. "The Effects of Blend Fuel Ratio of Cottonseed Oil and Light Naphtha on the DI Diesel Engine." Thesis, 2005. http://ndltd.ncl.edu.tw/handle/fhwujg.

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碩士<br>國立臺北科技大學<br>車輛工程系所<br>93<br>Although blend fuel of cottonseed oil 50% and light naphtha 50% could decrease the Smoke concentration 36% and the NOX concentration 11% of the exhaust gas emission than premium diesel, the BSFC would increase about 6%. If we change the blend ratio of the fuel as cottonseed oil 40% and light naphtha 60%, it could decrease the BSFC, but the exhaust gas emission concentration would increase by engine dyno test. And when we change the blend ratio of the fuel as cottonseed oil 60% and light naphtha 40%, the experimental results show that the exhaust gas emission c
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Chen, Tung-Peng, and 陳東朋. "Producing gasohol from aqueous ethanol using gasoline as the solvent and the desulfurization of the light naphtha." Thesis, 2009. http://ndltd.ncl.edu.tw/handle/96551415578525881924.

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碩士<br>國立中正大學<br>化學工程所<br>97<br>The goal of study is to improve the quality of gasoline. The extraction and adsorption are both the ways to produce quality gasoline. The study have two parts: (1) Producing gasohol from aqueous ethanol using gasoline as the solvent ;(2) The desulfurization of the light naphtha. (1) Producing gasohol from aqueous ethanol using gasoline as the solvent: There are two tests in this part: Simulated 3-stage extraction test and the York- Scheibel laboratory continuous extractor test. The goal of these tests is to make the gasohol with extracting the aqueous ethanol con
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Bárcia, Patrick da Silva. "Separation of light naphtha for the octane upgrading of gasoline : adsorption and membrane technologies and new adsorbents." Doctoral thesis, 2010. http://hdl.handle.net/10216/58567.

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The aim of this work is to contribute for the development of adsorption based separation processes with considerable potential for commercial application on the refining industry, namely, in the separation of high research octane number (HRON) paraffins from light naphtha fractions. The development of an adsorption process requires first a detailed knowledge of equilibria and kinetics of adsorption and their impact on the dynamic response of an adsorption column. Accordingly, we start collecting single and mixture adsorption equilibrium isotherms of C6 isomers, n-hexane (nHEX), 3-methyl
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Bárcia, Patrick da Silva. "Separation of light naphtha for the octane upgrading of gasoline: adsorption and membrane technologies and new adsorbents." Doctoral thesis, 2010. http://hdl.handle.net/10198/3409.

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The aim of this work is to contribute for the development of adsorption based separation processes with considerable potential for commercial application on the refining industry, namely, in the separation of high research octane number (HRON) paraffins from light naphtha fractions. The development of an adsorption process requires first a detailed knowledge of equilibria and kinetics of adsorption and their impact on the dynamic response of an adsorption column. Accordingly, we start collecting single and mixture adsorption equilibrium isotherms of C6 isomers, n-hexane (nHEX), 3-methyl
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Atef, Nour. "Numerically investigating the effects of gasoline surrogate physical and chemical properties in a gasoline compression ignition (GCI) engine." Diss., 2018. http://hdl.handle.net/10754/628032.

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Gasoline compression ignition (GCI) engines show promise in meeting stringent new environmental regulations, as they are characterized by high efficiency and low emissions. Simulations using chemical kinetic models provide an important platform for investigating the behaviors of the fuels inside these engines. However, because real fuels are complex, simulations require surrogate mixtures of small numbers of species that can replicate the properties of real fuels. Accordingly, the development of high fidelity, well-validated kinetic models for surrogates is critical in order to accuratel
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Book chapters on the topic "Light Naphtha"

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Fukase, S., N. Igarashi, K. Aimoto, and K. Kato. "Deactivation of Light Naphtha Aromatization Catalyst." In ACS Symposium Series. American Chemical Society, 1996. http://dx.doi.org/10.1021/bk-1996-0634.ch016.

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Nitschke, W., D. M. Kramer, A. Riedel, and U. Liebl. "From Naphtho- to Benzoquinones - (R)evolutionary Reorganisations of Electron Transfer Chains." In Photosynthesis: from Light to Biosphere. Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-009-0173-5_225.

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Davarnejad, Reza, Jamal Azizi, and Shaghayegh Bahari. "A Look at the Industrial Production of Olefins Based on Naphtha Feed: A Process Study of a Petrochemical Unit." In Alkenes - Recent Advances, New Perspectives and Applications [Working Title]. IntechOpen, 2021. http://dx.doi.org/10.5772/intechopen.100017.

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Olefins (ethylene, propylene and butadiene) as raw materials play an important role in a lot of chemical and polymer products. In industrial scale, there are several techniques from crude oil, natural gas, coal and methanol for the olefins production. Each of these has some advantages. The petrochemicals with liquid feed can simultaneously produce all of the olefins. Shazand Petrochemical Co. (as the first olefins production unit in Iran) produces all of the olefins using naphtha (light and heavy) feed. In this chapter, the production process of olefins based on naphtha will be studied from the beginning to the end (involving pyrolysis, compression, chilling and fractionation processes).
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Fukase, S., N. Igarashi, K. Kato, T. Nomura, and Y. Ishibashi. "Development of light naphtha aromatization process using a conventional fixed bed unit." In catalysts in Petroleum Refining and Petrochemical Industries 1995, Proceedings of the 2nd International Conference on Catalysts in Petroleum refining and Petrochemical Industries. Elsevier, 1996. http://dx.doi.org/10.1016/s0167-2991(96)80045-0.

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Kimura, Takao. "115 The development of sulfated zirconium oxide catalyst for isomerization of light naphtha." In Science and Technology in Catalysis 2002, Proceedings of the Fourth Tokyo conference on Advance Catalytic Science and Technology. Elsevier, 2003. http://dx.doi.org/10.1016/s0167-2991(03)80272-0.

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Han, Sang Yun, Chul Wee Lee, Jeong Ri Kim, et al. "Selective Formation of Light Olefins by the Cracking of Heavy Naphtha over Acid Catalysts." In Carbon Dioxide Utilization for Global Sustainability, Proceedings of 7ththe International Conference on Carbon Dioxide Utilization. Elsevier, 2004. http://dx.doi.org/10.1016/s0167-2991(04)80237-4.

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Wei, Y., Z. Liu, G. Wang, et al. "Production of light olefins and aromatic hydrocarbons through catalytic cracking of naphtha at lowered temperature." In Molecular Sieves: From Basic Research to Industrial Applications, Proceedings of the 3rd International Zeolite Symposium (3rd FEZA). Elsevier, 2005. http://dx.doi.org/10.1016/s0167-2991(05)80468-9.

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Fukase, S., N. Igarashi, K. Aimoto, H. Inoue, and H. Ono. "A new process of light naphtha aromatization using a zeolite-based catalyst with long-time stability." In Studies in Surface Science and Catalysis. Elsevier, 1997. http://dx.doi.org/10.1016/s0167-2991(97)80718-5.

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Conference papers on the topic "Light Naphtha"

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Hammadi, Ahmed Najeeb, and Ibtehal Kareem Shakir. "Enhancement the octane number of light naphtha by adsorption process." In 2ND INTERNATIONAL CONFERENCE ON MATERIALS ENGINEERING & SCIENCE (IConMEAS 2019). AIP Publishing, 2020. http://dx.doi.org/10.1063/5.0000129.

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Vallinayagam, R., S. Vedharaj, S. Mani Sarathy, and Robert W. Dibble. "Diethyl Ether as an Ignition Enhancer for Naphtha Creating a Drop in Fuel for Diesel." In ASME 2016 Internal Combustion Engine Division Fall Technical Conference. American Society of Mechanical Engineers, 2016. http://dx.doi.org/10.1115/icef2016-9324.

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Direct use of naphtha in compression ignition (CI) engines is not advisable because its lower cetane number negatively impacts the auto ignition process. However, engine or fuel modifications can be made to operate naphtha in CI engines. Enhancing a fuel’s auto ignition characteristics presents an opportunity to use low cetane fuel, naphtha, in CI engines. In this research, Di-ethyl ether (DEE) derived from ethanol is used as an ignition enhancer for light naphtha. With this fuel modification, a “drop-in” fuel that is interchangeable with existing diesel fuel has been created. The ignition cha
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Vallinayagam, R., S. Vedharaj, Yanzhao An, et al. "Compression Ignition of Light Naphtha and Its Multicomponent Surrogate under Partially Premixed Conditions." In 13th International Conference on Engines & Vehicles. SAE International, 2017. http://dx.doi.org/10.4271/2017-24-0078.

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Zhang, Yu, Alexander Voice, Tom Tzanetakis, Michael Traver, and David Cleary. "An Evaluation of Combustion and Emissions Performance With Low Cetane Naphtha Fuels in a Multi-Cylinder Heavy-Duty Diesel Engine." In ASME 2015 Internal Combustion Engine Division Fall Technical Conference. American Society of Mechanical Engineers, 2015. http://dx.doi.org/10.1115/icef2015-1055.

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Future projections in global transportation fuel use show a demand shift towards diesel and away from gasoline. At the same time greenhouse gas regulations will drive higher vehicle fuel efficiency and lower well-to-wheel CO2 production. Naphtha, a contributor to the gasoline stream and requiring less processing at the refinery level, is an attractive candidate to mitigate this demand shift while lowering the overall greenhouse gas impact. In this work, low cetane and high volatility gasoline-like fuels have shown potential to achieve high fuel efficiency with low engine-out emissions in a pro
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Won, Hyun Woo, Alexandre Bouet, Florence Duffour, and Loic Francqueville. "Naphtha Fuel on a Light Duty Single Cylinder Compression Ignition Engine with Two Different Compression Ratios." In SAE 2016 International Powertrains, Fuels & Lubricants Meeting. SAE International, 2016. http://dx.doi.org/10.4271/2016-01-2302.

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Moriya, Shinji, Hideyuki Takeda, Rikio Yaginuma, and Tomonori Matsumoto. "Adaptability for Diesel Engine from Coal Liquefied Oil (Case of Light Naphtha & Fraction Gas Oil )." In 2nd International Energy Conversion Engineering Conference. American Institute of Aeronautics and Astronautics, 2004. http://dx.doi.org/10.2514/6.2004-5524.

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Molie`re, Michel, Philippe Cozzarin, Se´bastien Bouchet, and Philippe Rech. "Catalytic Detection of Fuel Leaks in Gas Turbine Units: 2 — Gas Fuels Containing Hydrogen, Carbon Monoxide and Inert." In ASME Turbo Expo 2006: Power for Land, Sea, and Air. ASMEDC, 2006. http://dx.doi.org/10.1115/gt2006-90290.

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The detection of explosive gas and vapors is a critical safety function in Gas Turbines (GT) units. On one hand, this subject is being revisited by the GT community and safety organizations with a main focus on conventional gas fired power units. On the other hand one sees currently an increasing use of alternative primary energies for GT units including both gaseous and liquid fuels such as LPG, naphtha, syngas and a wide series of low and medium BTU gas fuels. This has prompted GE Energy to undertake a comprehensive evaluation of commercial catalytic detectors that are of common use in the d
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Komodromos, Aristotelis, George Moniatis, Frixos Kontopoulos, et al. "Measurement and Abatement of PM Emitted by Stationary Gas Turbines: Experience Gained With Different Fuels and Combustor Types." In ASME Turbo Expo 2018: Turbomachinery Technical Conference and Exposition. American Society of Mechanical Engineers, 2018. http://dx.doi.org/10.1115/gt2018-76393.

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Whichever the type of combustion installation, liquid fuels burned in gas turbines tend to generate particulate matter (PM) emissions, which consist in soot only or in ash plus soot, according to their ash-free or ash-forming character. Standard diffusion flame combustion systems are known as “universal” combustors, capable to burn both ash-free (naphtha, light and heavy distillates) and ash-forming (crude and heavy) fuels. In contrast, DLN systems are designed to burn gaseous fuels and light distillates. PMs in the range of a few parts per million represent a solid micropollutant, the measure
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Stalder, Jean-Pierre, and Phil Roberts. "Firing Low Viscosity Liquid Fuels in Heavy Duty Gas Turbines." In ASME Turbo Expo 2003, collocated with the 2003 International Joint Power Generation Conference. ASMEDC, 2003. http://dx.doi.org/10.1115/gt2003-38691.

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Sustained economic growth has created a strong demand for electrical energy worldwide. Security of fuel supply and cost are therefore very often critical issues for thermal capacity additions. Also the distance from fuel sources and available fuel transport infrastructure is an important factor in the cost of generation. Many plant locations have only limited supplies of conventional gas turbine fuels, namely natural gas and distillate fuels, thus a drive to diversify the fuels involved. For other electricity producers, the optimal use of existing or potential fuel resources is a must for econ
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Moliere, Michel, Matthieu Vierling, and Rich Symonds. "Interest for Liquid Fuels in Power Generation Gets Renewed." In ASME Turbo Expo 2010: Power for Land, Sea, and Air. ASMEDC, 2010. http://dx.doi.org/10.1115/gt2010-22149.

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As investments in power additions are under scrutiny, the viability and sustainability of generation projects are increasingly challenged by planners, and the debate about the most appropriate primary energy and prime mover is renewed with a sharper focus. Faced with limited forecasts on future growth, today’s power generators are looking cautiously at power addition blueprints and placing increased emphasis on equipment versatility and fuel flexibility in a move to eliminate single fuel reliance. Heavy duty gas turbines (HDGTs) can mitigate the uncertainty about operation factor and plant cap
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