Bibliografie tematiche / Fluidized-bed combustion

Letteratura scientifica selezionata sul tema "Fluidized-bed combustion"

Autore: Grafiati
Pubblicato: 4 giugno 2021
Ultima modifica: 30 gennaio 2023

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Articoli di riviste sul tema "Fluidized-bed combustion"

1

Erdiwansyah, Mahidin, Husni Husin, Nasaruddin, Muhtadin, Muhammad Faisal, Asri Gani, Usman e Rizalman Mamat. "Combustion Efficiency in a Fluidized-Bed Combustor with a Modified Perforated Plate for Air Distribution". Processes 9, n. 9 (24 agosto 2021): 1489. http://dx.doi.org/10.3390/pr9091489.

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Combustion efficiency is one of the most important parameters especially in the fluidized-bed combustor. Investigations into the efficiency of combustion in fluidized-bed combustor fuels using solid biomass waste fuels in recent years are increasingly in demand by researchers around the world. Specifically, this study aims to calculate the combustion efficiency in the fluidized-bed combustor. Combustion efficiency is calculated based on combustion results from the modification of hollow plates in the fluidized-bed combustor. The modified hollow plate aims to control combustion so that the fuel incorporated can burn out and not saturate. The combustion experiments were tested using palm oil biomass solid waste fuels such as palm kernel shell, oil palm midrib, and empty fruit bunches. The results of the measurements showed that the maximum combustion temperature for the palm kernel shell fuel reached 863 °C for M1 and 887 °C for M2. The maximum combustion temperature measurements for M1 and M2 from the oil palm midrib fuel testing reached 898 °C and 858 °C, respectively, while the maximum combustion temperature for M1 and M2 from the empty fruit bunches fuel was 667 °C and M2 847 °C, respectively. The rate of combustion efficiency with the modification of the hole plate in the fluidized-bed combustor reached 96.2%. Thermal efficiency in fluidized-bed combustors for oil palm midrib was 72.62%, for PKS was 70.03%, and for empty fruit bunches was 52.43%. The highest heat transfer rates for the oil palm midrib fuel reached 7792.36 W/m2, palm kernel shell 7167.38 W/m2, and empty fruit bunches 5127.83 W/m2. Thus, the modification of the holed plate in the fluidized-bed combustor chamber showed better performance of the plate than without modification.
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2

Grubor, Borislav, Dragoljub Dakic, Stevan Nemoda, Milica Mladenovic, Milijana Paprika e Simeon Oka. "Research in the fluidized bed combustion in the Laboratory for thermal engineering and energy - Part B: Achievements in technology implementation". Thermal Science 23, Suppl. 5 (2019): 1655–67. http://dx.doi.org/10.2298/tsci180725290g.

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Paper gives a review of the most important results of extensive and wide-ranging research program on R&D of fluidized bed combustion technology in the Laboratory for Thermal Engineering and Energy of the VINCA Institute of Nuclear Sciences. Paper presents detailed overview of R&D activities from the beginning in the second half of the 1970's up to present days. These activities encompass applied research achievements in the field of characterization of limestones and bed agglomeration and sintering and modeling of overall processes during fluidized bed combustion, all of which have facilitated the R&D of the fluidized bed combustion technology. Attention is also given to steady-state combustion testing of a wide-range of fuels (coals, liquid fuels, biomass, waste solid and liquid materials, etc.) in our fluidized bed combustor and development of original methodology for testing the suitability of fuels for fluidized bed combustion, as well as specific achievements in the area of technology application in Serbia.
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3

Leckner, Bo. "Fluidized Bed Combustion". Energy 30, n. 1 (gennaio 2005): 97–99. http://dx.doi.org/10.1016/j.energy.2004.02.024.

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4

HOSODA, Hideo. "Fluidized bed peat combustion." Journal of the Fuel Society of Japan 65, n. 9 (1986): 778–82. http://dx.doi.org/10.3775/jie.65.9_778.

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5

Ismagilov, Z. R., e M. A. Kerzhentsev. "Fluidized bed catalytic combustion". Catalysis Today 47, n. 1-4 (gennaio 1999): 339–46. http://dx.doi.org/10.1016/s0920-5861(98)00315-0.

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6

Tavoulareas, E. Stratos. "Fluidized-Bed Combustion Technology". Annual Review of Energy and the Environment 16, n. 1 (novembre 1991): 25–57. http://dx.doi.org/10.1146/annurev.eg.16.110191.000325.

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7

Hainley, D. C., M. Z. Haji-Sulaiman, S. Yavuzkurt e A. W. Scaroni. "Operating Experience With a Fluidized Bed Test Combustor". Journal of Energy Resources Technology 109, n. 2 (1 giugno 1987): 58–65. http://dx.doi.org/10.1115/1.3231325.

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This paper presents operating experience with a fluidized bed combustor burning various coals. The primary focus is on the effect of relevant coal properties on combustor performance. Tests were carried out using anthracite, HVB and HVC bituminous and sub-bituminous A coals, and petroleum coke. Comparisons of the performance of the combustion on the various fuels are made. A two-stage fluidized bed combustor operating in a single-stage mode without recycle was employed. Experimental measurements included temperature, fuel feed rate, fluidization velocity and bed height. For some of the coals, bed agglomeration was found to occur. The results indicate that coal properties have an important effect upon the operation of the fluidized bed combustor.
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Mladenovic, Milica, Dragoljub Dakic, Stevan Nemoda, Rastko Mladenovic, Aleksandar Eric, Branislav Repic e Mirko Komatina. "Combustion of low grade fractions of Lubnica coal in fluidized bed". Thermal Science 16, n. 1 (2012): 297–311. http://dx.doi.org/10.2298/tsci1201297m.

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In this paper a method of examination of fuel suitability for fluidized bed combustion is presented. The research of combustion characteristics of low grade fractions of Lubnica brown coal in the fluidized bed by the aforementioned methodology has been carried out on a laboratory semi-industrial apparatus of 200 kWt. Description of the experimental fluidized bed combustion facility is given, as well as experimental results, with the focus on furnace temperature distribution, in order to determine the location of the zone of intensive combustion. Based on investigation results, which are focused on combustion quality (combustion completion) as well as on satisfying the environmental protection criteria, it can be stated that the investigated coal is suitable for burning in bubbling, as well as in circulating fluidized bed.
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Han, J., T. Shimizu, M. Wataru, H. Kim e G. Wang. "Polypropylene Combustion in a Fluidized Bed Combustor". Energy Sources, Part A: Recovery, Utilization, and Environmental Effects 32, n. 12 (15 aprile 2010): 1121–29. http://dx.doi.org/10.1080/15567030802612499.

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Liang, Yu Wen, Hui Song e Yuan Xin Li. "Optimization Design of Limestone Conveyor System in Circulating Fluidized Bed Boiler". Applied Mechanics and Materials 602-605 (agosto 2014): 731–33. http://dx.doi.org/10.4028/www.scientific.net/amm.602-605.731.

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The qualities of the limestone conveyor system running directly affect the efficiency of circulating fluidized bed boiler combustion. Aiming at the problems of limestone conveyor system, this paper optimizes the design of the control system and the ring limestone fluidized bed boiler combustion control system networking, the use of configuration technology for real-time data control system to monitor and implement manual and automatic switching function. While improving the delivery system and improve the combustion efficiency of the boiler. For the circulating fluidized bed boiler combustion system provides a reference value.
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Tesi sul tema "Fluidized-bed combustion"

1

Hossain, Abu Norman. "Combustion of solid fuel in a fluidized bed combustor". Ohio : Ohio University, 1998. http://www.ohiolink.edu/etd/view.cgi?ohiou1176492911.

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Hossain, Abu Noman. "Combustion of solid fuel in a fluidized bed combustor". Ohio University / OhioLINK, 1998. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1176492911.

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Rao, Arjun Shankar. "Carbonation of fluidized bed combustion solids". Thesis, University of Ottawa (Canada), 2006. http://hdl.handle.net/10393/27412.

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Fluidized bed combustion (FBC) ash from the combustion of high-sulphur fuels with limestone addition can contain from 15 to 25% quick lime content. This excess calcium oxide gives the ash numerous undesirable properties such as strong exothermicity on wetting and high-pH leachate that must be treated before discharge. It also leads to the formation of ettringite with significant deleterious expansion in the landfill. In consequence, carbonation of FBC ash is desirable in order to reduce its alkalinity and improve its disposal characteristics. The current technique to reduce the exothermic character of the ash involves hydrating the ash in two stages, leading to the consumption of large quantities of water. Sonication along with simultaneous carbonation of the ash yields a product suitable for direct disposal in landfills with the minimum of water addition (to achieve the optimum proctor levels for maximum compaction of the ash in the landfill site). This work explores the use of sonochemical-enhanced carbonation of FBC ash. Tests have been conducted using four ashes, two of which differ in age only and are from the Nova Scotia Power 183 MWe CFBC (circulating fluidized bed combustor) boiler. The other two ashes are from the CFBC boilers at A/C power and Piney Creek, U.S.A. Tests with additives such as sodium chloride (at levels comparable with that in seawater) and seawater from Nova Scotia have also been carried out. Tests were carried out at low (20°, 40°C) and high (60°, 80°C) temperatures. Sonicated samples were also analyzed using TGA (Thermogravimetric analysis), TGA-FTIR (Thermogravimetric and Fourier transform infra red spectroscopy analysis) and XRD (X-ray diffraction) techniques to determine the influence of other calcium compounds (OCC). The size reduction brought about by sonication was quantified using wet sieving. The ash reactivity displays a strong temperature dependency with almost complete carbonation of the ashes being achieved in minutes at higher temperatures. Additives were found to increase the level of hydration of the ashes in line with previous work; however, carbonation levels were unaffected. TGA, TGA-FTIR and XRD analysis of the samples indicated that other calcium compounds (OCC) were also formed during hydration.
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Lin, Jeng-Liang Keener Harold M. "Corncob combustion in a fluidized bed /". Connect to resource, 1991. http://rave.ohiolink.edu/etdc/view?acc%5Fnum=osu1145451174.

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Lin, Jeng-Liang. "Corncob combustion in a fluidized bed". The Ohio State University, 1991. http://rave.ohiolink.edu/etdc/view?acc_num=osu1145451174.

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Xu, Jiangang Chemical Sciences &amp Engineering Faculty of Engineering UNSW. "Coal related bed material agglomeration in pressurized fluidized bed combustion". Awarded by:University of New South Wales. School of Chemical Sciences and Engineering, 2006. http://handle.unsw.edu.au/1959.4/25131.

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Abstract (sommario):
The thermodynamic behaviours in a PFBC combustor were simulated for the ash from all of the six coals with sand and limestone as bed material. Ash components determined the ash thermodynamic behaviour at high temperature, and each component had different effects. For assessment of the potential for bed material agglomeration, the temperature at which 15% of the ash would become liquid (T15) was calculated with the coal ash, the cyclone ash and the cyclone ash mixed with varying amounts of limestone. Both the bed ash and fly ash, collected from an industrial PFBC plant, consisted of limestone/lime particles with different extent of sulphation, and coal ash particles. The calcium aluminosilicate material formed on the coal ash particles but not on the limestone particles. The aluminosilicate materials appeared to be formed from fine ash and lime particles at some local hot zones in the boiler. The melted materials may glue ash and bed material particle into large particles leading to bed agglomeration and defluidization. Four mechanisms were proposed for the formation of bed material agglomeration in PFBC, which may occur under different conditions. One mechanism explains the bed material agglomeration with the high localized high temperature zone due to the improper design or operation, while the bed agglomeration through the other three mechanisms results from the unsuitable coals burnt in the PFBC combustor. The maximum char temperature and the minimum T15 were used simultaneously to predict the tendency towards bed material agglomeration in PFBC burning different coals. Both char properties and ash properties should be considered during coal selection process for PFBC, to ameliorate the potential problem of bed agglomeration.
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Wildegger-Gaissmaier, Anna Elisabeth. "Fluidized bed utilization of South Australian coals". Title page, contents and abstract only, 1988. http://web4.library.adelaide.edu.au/theses/09PH/09phw672.pdf.

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Gogolek, Peter Edmund Gordon. "Mathematical modelling of fluctuations in fluidized bed combustion". Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0006/NQ31928.pdf.

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Vaart, D. R. van der. "The combustion of gas in a fluidized bed". Thesis, University of Cambridge, 1985. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.355686.

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Yliniemi, J. (Juho). "Alkali activation-granulation of fluidized bed combustion fly ashes". Doctoral thesis, Oulun yliopisto, 2017. http://urn.fi/urn:isbn:9789526215624.

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Abstract Biomass, such as wood, binds CO2 as it grows, and is thus considered an environmentally friendly alternative fuel to replace coal. In Finland, biomass is typically co-combusted with peat, and also municipal waste is becoming more common as a fuel for power plants. Wood, peat and waste-based fuels are typically burned in fluidized bed combustion (FBC) boilers. Ash is the inorganic, incombustible residue resulting from combustion. The annual production of biomass and peat ash in Finland is 600 000 tonnes, and this amount is likely to increase in the future, since the use of coal for energy production will be discontinued during the 2020s. Unfortunately, FBC ash is still largely unutilized at the moment and is mainly dumped in landfills. The general aim of this thesis was to generate information which could potentially improve the utilization of FBC ash by alkali activation. The specific objective was to produce geopolymer aggregates by means of a simultaneous alkali activation-granulation process. It was shown that geopolymer aggregates with physical properties comparable to commercial lightweight expanded clay aggregates (LECAs) can be produced from FBC fly ash containing heavy metals. Although the ashes were largely unreactive and no new crystalline phases were formed by alkali activation, a new amorphous phase was observed in the XRD patterns, possibly representing micron-sized calcium aluminate silicate hydrate-type gels. The heavy metal immobilization efficiency of alkali activation varied with the type of fly ash. Good stabilization was generally obtained for cationic metals such as Ba, Pb and Zn, but in common with the results obtained with alkali activation of coal fly ash, anionic metals became leachable after alkali activation. The efficiency of immobilization depended on the physical and chemical properties of the fly ash and was not related to the total content of the element. All the geopolymer aggregates met the criteria for a lightweight aggregate (LWA) as defined by EN standard 13055-1. Their strength depended on the reactivity and particle size distribution of the fly ash. Mortars and concretes prepared with such geopolymer aggregates had higher mechanical strength, higher dynamic modulus of elasticity and higher density than concrete produced with commercial LECA, while exhibiting similar rheology and workability
Tiivistelmä Biopolttoaineet, esimerkiksi puu, ovat ympäristöystävällinen vaihtoehto kivihiilelle, koska ne sitovat hiilidioksidia kasvaessaan. Suomessa biopolttoaineita poltetaan tyypillisesti turpeen kanssa, ja nykyään myös jätteen hyödyntäminen polttoaineena on yleistynyt. Puu, turve ja jätepolttoaineet poltetaan tyypillisesti leijupetipoltto-tekniikalla. Tuhka on polton epäorgaaninen, palamaton jäännös. Puun ja turpeen tuhkaa tuotetaan Suomessa 600 000 tonnia vuodessa ja määrän odotetaan kasvavan, sillä kivihiilen poltto lopetetaan 2020-luvulla. Leijupetipolton tuhkaa ei tällä hetkellä juurikaan hyödynnetä ja tuhka päätyykin pääasiassa kaatopaikoille. Tämän tutkielman päämääränä oli tuottaa tietoa, joka parantaisi leijupetipolton tuhkien hyödyntämistä alkali-aktivaatiolla. Erityisesti tavoitteena oli valmistaa geopolymeeriaggregaatteja yhtäaikaisella alkali-aktivaatiolla ja rakeistuksella. Tutkielmassa osoitettiin, että raskasmetalleja sisältävistä tuhkista valmistettujen geopolymeeriaggregaattien fysikaaliset ominaisuudet ovat vertailukelpoiset kaupallisten kevytsora-aggregaattien (LECA) kanssa. Vaikka tuhkien reaktiivisuus oli matala, ja uusia kidefaaseja ei muodostunut alkaliaktivaatiolla, uusi amorfinen faasi havaittiin XRD-mittauksissa. Uusi amorfinen faasi oli mahdollisesti mikrometrikokoluokan kalsium-aluminaatti-silikaatti-hydraatti-tyyppinen rakenne. Raskasmetallien stabiloinnin tehokkuus vaihteli tuhkien välillä. Kationiset metallit, kuten barium, lyijy ja sinkki, stabiloituivat pääasiassa hyvin, mutta anionisten metallin liukoisuus kasvoi alkali-aktivoinnin myötä. Stabiloinnin tehokkuus riippui tuhkien fysikaalisista ja kemiallisista ominaisuuksista, mutta raskasmetallin kokonaispitoisuudella ei ollu vaikutusta. Kaikki geopolymeeriaggregaatit olivat kevytsora-aggregaatteja standardin EN 13055-1 mukaisesti. Aggregaattien lujuus riippui tuhkan reaktiivisuudesta ja partikkelikokojakaumasta. Geopolymeeriaggregaateilla valmistettujen laastien ja betonien mekaaninen lujuus, Youngin moduuli ja tiheys olivat korkeampia kuin kaupallisella kevytsora-aggregaateilla valmistetut, vaikka niiden reologia ja työstettävyys olivat samanlaisia
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Libri sul tema "Fluidized-bed combustion"

1

J, Anthony E., a cura di. Fluidized bed combustion. New York: M. Dekker, 2004.

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2

Cuenca, M. Alvarez, e E. J. Anthony, a cura di. Pressurized Fluidized Bed Combustion. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0617-7.

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3

Makhorin, Konstantin Epifanovich. Szhiganie topliva v psevdoozhizhennom sloe. Kiev: Nauk. dumka, 1989.

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4

Decamps, F. F. E. De wervellaag als beloftevolle brander voor allerlei vaste brandstoffen. Brussel, België: Studiecentrum voor Kernenergie, 1985.

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5

Asian Conference on Fluidized-Bed & Three-Phase Reactors (1988 Tokyo, Japan). Proceedings of the Asian Conference on fluidized-bed & three-phase reactors, December 14-17, 1988 Sanjo-Kaikan, Tokyo, Japan. [s.℗: s.n., 1988.

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Kuchin, Gennadiĭ Petrovich. Szhiganie nizkosortnykh topliv v psevdoozhizhennom sloe. Kiev: "Tekhnika", 1987.

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7

Wirth, Karl-Ernst. Zirkulierende Wirbelschichten: Strömungsmechanische Grundlagen, Anwendung in der Feuerungstechnik. Berlin: Springer, 1990.

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8

Tung, S. E. Atmospheric fluidized-bed combustion: A technical source book. Cambridge, Mass: Massachusetts Institute of Technology, 1987.

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Tung, S. E. Atmospheric fluidized-bed combustion: A technical source book. Cambridge, Mass: Massachusetts Institute of Technology, 1987.

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10

Simone, L. De. La combustione in letto fluido. Roma: ENEA, Comitato nazionale per la ricerca e per lo sviluppo dell'energia nucleare e delle energie alternative, 1987.

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Capitoli di libri sul tema "Fluidized-bed combustion"

1

Bryden, Kenneth M., Kenneth W. Ragland e Song-Charng Kong. "Fluidized Bed Combustion". In Combustion Engineering, 395–420. 3a ed. Boca Raton: CRC Press, 2022. http://dx.doi.org/10.1201/b22232-21.

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Basu, Prabir. "Combustion". In Circulating Fluidized Bed Boilers, 89–119. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-06173-3_4.

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Habiger, Kenneth E. "Fluidized Bed Combustion". In Power Plant Engineering, 689–709. Boston, MA: Springer US, 1996. http://dx.doi.org/10.1007/978-1-4613-0427-2_21.

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Hoy, H. R., A. G. Roberts e J. E. Stantan. "Introduction". In Pressurized Fluidized Bed Combustion, 1–37. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0617-7_1.

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Pitt, R. U. "The combined cycle". In Pressurized Fluidized Bed Combustion, 366–418. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0617-7_10.

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Rosen, M. A., e D. A. Horazak. "Energy and exergy analyses of PFBC power plants". In Pressurized Fluidized Bed Combustion, 419–48. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0617-7_11.

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Shoemaker, R. "Process control". In Pressurized Fluidized Bed Combustion, 449–74. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0617-7_12.

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Cuenca, M. Alvarez, A. S. Carmona e J. C. Garcia. "The demonstration units: Escatrón and Tidd, four years of operation". In Pressurized Fluidized Bed Combustion, 475–514. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0617-7_13.

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Dellefield, R. J. "Economics of PFBC technology". In Pressurized Fluidized Bed Combustion, 515–42. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0617-7_14.

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Wheeldon, J. M. "Addendum: Results of EPRI’s Engineering and Economic Evaluation of PFBC Power Plant Designs". In Pressurized Fluidized Bed Combustion, 542–54. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0617-7_15.

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Atti di convegni sul tema "Fluidized-bed combustion"

1

Valk, M. "Fluidized Bed Combustors". In Advanced Course in Fluidized Bed Combustion. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ichmt.1986.advcoursefluidbedcomb.30.

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2

Radovanovic, M., M. Valk, B. Alblas, W. Prins e W. P. M. van Swaaij. "Combustion in Fluidized Beds". In Advanced Course in Fluidized Bed Combustion. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ichmt.1986.advcoursefluidbedcomb.60.

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van Swaaij, W. P. M., e W. Prins. "Fundamentals of Fluidization". In Advanced Course in Fluidized Bed Combustion. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ichmt.1986.advcoursefluidbedcomb.50.

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Masson, H. A. "Fuel Circulation and Segregation in FBC". In Advanced Course in Fluidized Bed Combustion. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ichmt.1986.advcoursefluidbedcomb.70.

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Draijer, W. "Heat Transfer in FB-Boilers". In Advanced Course in Fluidized Bed Combustion. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ichmt.1986.advcoursefluidbedcomb.80.

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Spitsbergen, U., Ch J. Vincent, H. A. Akse e B. Kamphuis. "Limestone Additions and Flue Gas Sampling Systems". In Advanced Course in Fluidized Bed Combustion. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ichmt.1986.advcoursefluidbedcomb.90.

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Radovanovic, M. "IntroductionWhy PBC?" In Advanced Course in Fluidized Bed Combustion. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ichmt.1986.advcoursefluidbedcomb.20.

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8

Rademacher, F. J. C., e G. Haaker. "Materials Handling". In Advanced Course in Fluidized Bed Combustion. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ichmt.1986.advcoursefluidbedcomb.40.

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9

Radovanovic, M. "Prerface". In Advanced Course in Fluidized Bed Combustion. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ichmt.1986.advcoursefluidbedcomb.10.

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10

Kortleven, A. "Thermodynamic Cycles with FBC". In Advanced Course in Fluidized Bed Combustion. Connecticut: Begellhouse, 1986. http://dx.doi.org/10.1615/ichmt.1986.advcoursefluidbedcomb.100.

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Rapporti di organizzazioni sul tema "Fluidized-bed combustion"

1

Botros, P. Fluidized-bed combustion. Office of Scientific and Technical Information (OSTI), aprile 1990. http://dx.doi.org/10.2172/6325839.

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2

Brown, R. C., M. R. Dawson e S. Noble. Bed material agglomeration during fluidized bed combustion. Office of Scientific and Technical Information (OSTI), febbraio 1993. http://dx.doi.org/10.2172/6869469.

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3

Author, Not Given. Pulsed atmospheric fluidized bed combustion. Office of Scientific and Technical Information (OSTI), maggio 1992. http://dx.doi.org/10.2172/6963987.

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4

Banerjee, Subhodeep, e Robin Hughes. Biomass Combustion in a Circulating Fluidized Bed Combustor. Office of Scientific and Technical Information (OSTI), settembre 2020. http://dx.doi.org/10.2172/1659115.

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5

Hughes, Robin, e Subhodeep Banerjee. Biomass Combustion in a Circulating Fluidized Bed Combustor. Office of Scientific and Technical Information (OSTI), settembre 2020. http://dx.doi.org/10.2172/1660765.

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6

Brown, R. C., M. R. Dawson e J. L. Smeenk. Bed material agglomeration during fluidized bed combustion. Final report. Office of Scientific and Technical Information (OSTI), gennaio 1996. http://dx.doi.org/10.2172/216299.

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7

Anthony, E. J., H. A. Becker, R. K. Code, R. W. McCleave e J R Stephenson. Bubbling fluidized bed combustion of Syncrude coke. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1987. http://dx.doi.org/10.4095/304362.

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8

Anthony, E. J., D. L. Desai e F. D. Friedrich. Fluidized bed combustion of Devco Prince test rejects. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1987. http://dx.doi.org/10.4095/304358.

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9

Lau, I. T., e F. D. Friedrich. Influence of fuel properties on fluidized bed combustion. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1988. http://dx.doi.org/10.4095/304398.

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10

Lau, I. T., D. T. Liang, L. Jia e E. J. Anthony. Circulating fluidized bed combustion characteristics of Suncor limestone. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1993. http://dx.doi.org/10.4095/304570.

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