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Journal articles on the topic 'Pulverised fuel'

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Author: Grafiati

Published: 10 December 2022

Last updated: 28 January 2023

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1

Zhang, J., J. Coulthard, and R. P. Keech. "Characteristics of ABB Pulverised Fuel Meters." Measurement and Control 41, no. 1 (February 2008): 24–27. http://dx.doi.org/10.1177/002029400804100106.

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ABB PFMaster solids flow meters have proven to be very useful worldwide in coal-fired power stations for monitoring and controlling Pulverised Fuel (PF) velocity and mass-flow rates at various locations in the boiler fuel supply system. However, little has been published of the meter's response on a pneumatic conveyor where both the air and the solids input were each measured independently. This is a brief report of tests carried out on a two such metersin a university pneumatic conveyor.

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2

Zhang, Jianyong, John Coulthard, Ruixue Cheng, and Ray Keech. "Measuring Pulverised Fuel: Using Electrostatic Meters." Measurement and Control 42, no. 3 (April 2009): 87–90. http://dx.doi.org/10.1177/002029400904200307.

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3

Coulthard, J., R. Cheng, J. Zhang, and R. P. Keech. "Testing of Electrostatic Pulverised Fuel Meters." Measurement and Control 44, no. 8 (October 2011): 252–54. http://dx.doi.org/10.1177/002029401104400805.

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4

Davison, A. G., S. Durham, A. J. Taylor, and C. J. Schilling. "Asthma caused by pulverised fuel ash." BMJ 292, no. 6535 (June 14, 1986): 1561. http://dx.doi.org/10.1136/bmj.292.6535.1561.

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5

Iqbal Khan, Mohammad. "Prediction Model and Relationship of Compressive and Tensile Strengths for High Performance Concrete." Applied Mechanics and Materials 377 (August 2013): 92–98. http://dx.doi.org/10.4028/www.scientific.net/amm.377.92.

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Analytical models for compressive strength and tensile strength of high performance concrete are presented. High performance concrete was developed using binary and ternary blending combinations consisting of ordinary Portland cement, pulverised fuel ash and silica fume. Pulverised fuel ash and silica fume were incorporated as partial cement replacements for the preparation of various combinations of blended systems. Compressive strength and tensile strength of concrete containing ordinary Portland cement, pulverised fuel ash and silica fume at various ages are reported. Based on the experimentally obtained results, analytical prediction models were developed. These models enabled the establishment of isoresponse contours showing the interactive influence between the various parameters investigated.

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6

Willson, P. M., and T. E. Chappell. "Pulverised Fuel Flame Monitoring in Utility Boilers." Measurement and Control 18, no. 2 (March 1985): 66–72. http://dx.doi.org/10.1177/002029408501800205.

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7

Coulthard, J., R. Cheng, P. Kane, J. Osborne, and R. P. Keech. "Pulverised-Fuel Monitoring at Methil Power Station." Measurement and Control 30, no. 1 (February 1997): 6–8. http://dx.doi.org/10.1177/002029409703000102.

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8

Pronobis, Marek, and Rafał Litka. "Rate of corrosion of waterwalls in supercritical pulverised fuel boilers." Chemical and Process Engineering 33, no. 2 (June 1, 2012): 263–77. http://dx.doi.org/10.2478/v10176-012-0026-x.

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Rate of corrosion of waterwalls in supercritical pulverised fuel boilers This paper presents an analysis of the corrosion hazard in the burner belt area of waterwalls in pulverised fuel (PF) boilers that results from low-NOx combustion. Temperature distributions along the waterwall tubes in subcritical (denoted as SUB) and supercritical (SUP) boilers were calculated and compared. Two hypothetical distributions of CO concentrations were assumed in the near-wall layer of the flue gas in the boiler furnace, and the kinetics of the waterwall corrosion were analysed as a function of the local temperature of the tubes. The predicted rate of corrosion of the boiler furnace waterwalls in the supercritical boilers was compared with that of in the subcritical boilers.

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9

Coulthard, J., P. Kane, R. Cheng, R. P. Keech, and J. T. Osborne. "Online pulverised-fuel monitoring at Methil power station." Power Engineering Journal 11, no. 1 (February 1, 1997): 27–30. http://dx.doi.org/10.1049/pe:19970106.

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10

Lee, S. "Potential Groundwater Contamination from Pulverised Fuel Ash (PFA)." Mineralogical Magazine 58A, no. 2 (1994): 515–16. http://dx.doi.org/10.1180/minmag.1994.58a.2.06.

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11

Haas, J., M. Tamura, and R. Weber. "Characterisation of coal blends for pulverised fuel combustion." Fuel 80, no. 9 (July 2001): 1317–23. http://dx.doi.org/10.1016/s0016-2361(00)00216-7.

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12

Simons, H. S., and J. W. Jeffery. "An X-ray study of pulverised fuel ash." Journal of Applied Chemistry 10, no. 8 (May 4, 2007): 328–36. http://dx.doi.org/10.1002/jctb.5010100804.

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13

Ma, L., M. Gharebaghi, R. Porter, M. Pourkashanian, J. M. Jones, and A. Williams. "Modelling methods for co-fired pulverised fuel furnaces." Fuel 88, no. 12 (December 2009): 2448–54. http://dx.doi.org/10.1016/j.fuel.2009.02.030.

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14

Pronobis, Marek, Kazimierz Mroczek, Mateusz Tymoszuk, Szymon Ciukaj, Robert Wejkowski, Tomasz Janda, and Katarzyna Jagodzińska. "Optimisation of coal fineness in pulverised-fuel boilers." Energy 139 (November 2017): 655–66. http://dx.doi.org/10.1016/j.energy.2017.07.057.

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15

Stanek, W., M. Szega, L. Blacha, M. Niesler, and M. Gawron. "Exergo-Ecological Assessment Of Auxiliary Fuel Injection Into Blast-Furnace." Archives of Metallurgy and Materials 60, no. 2 (June 1, 2015): 711–19. http://dx.doi.org/10.1515/amm-2015-0196.

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Abstract Metallurgy represents complex technological chain supplied with different kinds of primary resources. Iron metallurgy based on blast-furnace process, dominates in world steel production. Metallurgical coke is the basic fuel in this case. Its production is connected with several environmental disadvantageous impacts. One of them is the extended production chain from primary energy to final energy. The reduction of coke consumption in the process can be achieved e.g. by injection of auxiliary fuels or increasing the thermal parameters in the process. In present injection of pulverised coal dominates while recirculation of top-gas seems to be future technology. However, the latter one requires the CO2 removal that additionally extended the production chain. The evaluation of resources management in complex energy-technological systems required application of advanced method based on thermodynamics. In the paper the system exergo-ecological assessment of pulverised coal injection into blast-furnace and top-gas recirculation has been applied. As a comparative criterion the thermo-ecological cost has been proposed.

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16

Winter, M. G., and B. G. Clarke. "Improved use of pulverised fuel ash as general fill." Geotechnical Engineering 155, no. 2 (April 2002): 133–41. http://dx.doi.org/10.1680/geng.155.2.133.38652.

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17

Winter, M. G., and B. G. Clarke. "Improved use of pulverised fuel ash as general fill." Proceedings of the Institution of Civil Engineers - Geotechnical Engineering 155, no. 2 (April 2002): 133–41. http://dx.doi.org/10.1680/geng.2002.155.2.133.

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18

Backreedy, R. I., J. M. Jones, M. Pourkashanian, D. J. Waldron, and A. Williams. "Application of coal combustion model to pulverised fuel furnaces." Journal of the Energy Institute 79, no. 2 (June 1, 2006): 101–9. http://dx.doi.org/10.1179/174602206x103521.

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19

Coulthard, J., R. P. Keech, R. Cheng, B. Armstrong, J. Zhang, and P. Asquith. "Measuring & Controlling Solids Split Using Pulverised Fuel Meters." Measurement and Control 36, no. 7 (September 2003): 204–8. http://dx.doi.org/10.1177/002029400303600702.

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20

Zhang, Jianyong, John Coulthard, Ruixue Cheng, and Ray Keech. "On — Line Low Measurement and Control of Pulverised Fuel." Measurement and Control 37, no. 9 (November 2004): 273–75. http://dx.doi.org/10.1177/002029400403700902.

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21

Shaw, Peter. "Collembola of pulverised fuel ash sites in east London." European Journal of Soil Biology 39, no. 1 (January 2003): 1–8. http://dx.doi.org/10.1016/s1164-5563(02)00002-x.

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22

Van, Y., B. Byrne, and J. Coulthard. "Radiation attenuation of pulverised fuel in pneumatic conveying systems." Transactions of the Institute of Measurement and Control 15, no. 3 (August 1993): 98–103. http://dx.doi.org/10.1177/014233129301500301.

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23

Watt, J. D., and D. J. Thorne. "The composition and pozzolanic properties of pulverised fuel ashes." Journal of Applied Chemistry 16, no. 2 (May 4, 2007): 33–39. http://dx.doi.org/10.1002/jctb.5010160201.

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24

Adell, V., C. R. Cheeseman, A. Doel, A. Beattie, and A. R. Boccaccini. "Comparison of rapid and slow sintered pulverised fuel ash." Fuel 87, no. 2 (February 2008): 187–95. http://dx.doi.org/10.1016/j.fuel.2007.04.009.

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25

Dixit, C. S. Bhaskar, P. J. Paul, and H. S. Mukunda. "Part II: Computational studies on a pulverised fuel stove." Biomass and Bioenergy 30, no. 7 (July 2006): 684–91. http://dx.doi.org/10.1016/j.biombioe.2006.01.010.

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26

Dixit, C. S. Bhaskar, P. J. Paul, and H. S. Mukunda. "Part I: Experimental studies on a pulverised fuel stove." Biomass and Bioenergy 30, no. 7 (July 2006): 673–83. http://dx.doi.org/10.1016/j.biombioe.2006.01.011.

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27

Mizal Azzmi, Norazura, Jamaludin Mohamad Yatim, Hazlan Abdul Hamid, Azmahani Abdul Aziz, and Adole Michael Adole. "Mechanical properties of kenaf fibrous pulverized fuel ash concrete." MATEC Web of Conferences 250 (2018): 05007. http://dx.doi.org/10.1051/matecconf/201825005007.

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The main objective of the experimental work is to identify the mechanical properties of Kenaf Fiber incorporate with Ordinary Portland Cement (OPC) and Pulverised Fuel Ash (PFA) in the mix proportions of concrete. Kenaf Fibrous Concrete (KFC) and Kenaf Fibrous Pulverised Fuel Ash Concrete (KFPC) will be measured on physical and mechanical properties in order to investigate the suitability of this natural fiber as a composite material. A comparison of properties between these two composites will determine the density, workability, compressive, tensile, and flexural strength of the concrete. Eight different mixes with varying percentage of Kenaf fiber were prepared with 30N/mm2 strength at 28days ,56 days and 90 days. Short fiber with 25mm and 50mm length were randomly distribute in composite to enhance the tensile and durability. PFA was obtained by the process of burning in the Power Station Coal Ash at Tanjung Bin, Johor. The unburning powder from the process is called as a PFA generally suitable for cement replacement in the concrete mix. The pozzolanic reaction will improve the adhesion of cement gel, hence increased the properties of concrete in a long-term strength development. The result shows that the inclusion of Kenaf fiber improve tensile strength of composite, furthermore the 25% PFA mix increase the durability of concrete.

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28

Winter, M. G., and B. G. Clarke. "Discussion: Improved use of pulverised fuel ash as general fill." Proceedings of the Institution of Civil Engineers - Geotechnical Engineering 156, no. 1 (January 2003): 57–58. http://dx.doi.org/10.1680/geng.2003.156.1.57.

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29

Coulthard, J., R. Keech, and Ruixue Cheng. "Developments in pulverised fuel metering for coal fired power stations." Power Engineering Journal 14, no. 3 (June 1, 2000): 100–104. http://dx.doi.org/10.1049/pe:20000302.

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30

Perkins, P. V., and A. R. Vann. "The bulk density amelioration of minespoil with pulverised fuel ash." Soil Technology 10, no. 2 (February 1997): 111–14. http://dx.doi.org/10.1016/s0933-3630(96)00086-4.

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31

Chen, Jian-Yuan, A. P. Mann, and J. H. Kent. "Computational modelling of pulverised fuel burnout in tangentially fired furnaces." Symposium (International) on Combustion 24, no. 1 (January 1992): 1381–89. http://dx.doi.org/10.1016/s0082-0784(06)80161-x.

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32

Moghtaderi, Behdad. "Extinction of multi-species char clouds in pulverised fuel combustors." Fuel 83, no. 14-15 (October 2004): 1961–72. http://dx.doi.org/10.1016/j.fuel.2004.04.009.

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33

Milenkova, K. S., A. G. Borrego, D. Alvarez, J. Xiberta, and R. Menéndez. "Devolatilisation behaviour of petroleum coke under pulverised fuel combustion conditions." Fuel 82, no. 15-17 (October 2003): 1883–91. http://dx.doi.org/10.1016/s0016-2361(03)00191-1.

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34

Clarke, B. G., and R. Coombs. "Specifying and using pulverised fuel ash as an engineered fill." Waste Management 16, no. 1-3 (January 1996): 101–8. http://dx.doi.org/10.1016/s0956-053x(96)00031-1.

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35

Yelland, Thomas S., Syed Sheraz Daood, and William Nimmo. "Comparing fuel additives for fireside corrosion inhibition in pulverised fuel boilers using thermodynamic modelling." Calphad 74 (September 2021): 102283. http://dx.doi.org/10.1016/j.calphad.2021.102283.

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36

Archary, Hamresin, Walter Schmitz, and Louis Jestin. "Mass flow and particle size monitoring of pulverised fuel vertical spindle mills." Chemical and Process Engineering 37, no. 2 (June 1, 2016): 175–97. http://dx.doi.org/10.1515/cpe-2016-0016.

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Abstract The first step towards condition based maintenance of the milling plant is the implementation of online condition monitoring of the mill. The following paper presents and analyses methods of monitoring the key performance factors of a vertical spindle mill that is suited for implementation on older power stations, i.e. the quantity (mass flow rate) and quality (particle fineness) of the pulverised fuel produced by the mill. It is shown herein that the mill throughput can be monitored on-line using a simple mill energy balance that successfully predicts the coal throughput within 2.33% as compared to a calibrated coal feeder. A sensitivity analysis reveals that the coal moisture is a critical measurement for this method to be adopted as an on-line mass flow monitoring tool. A laser based particle size analyser tool was tested for use in the power plant environment as an online monitoring solution to measure pulverised fuel fineness. It was revealed that several factors around the set-up and operation of the instrument have an influence on the perceived results. Although the instrument showed good precision and repeatability of results, these factors must be taken into account in order to improve the accuracy of the reported results before the instrument can be commissioned as an on-line monitoring solution.

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37

Awe, Yewande, Chris Cheeseman, and Chris Sollars. "Permeability of lime-activated pulverised fuel ash to metal-containing permeants." Waste Management & Research 19, no. 1 (February 2001): 35–44. http://dx.doi.org/10.1177/0734242x0101900105.

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38

Lam, Katherine K. Y. "Coral recruitment onto an experimental pulverised fuel ash–concrete artificial reef." Marine Pollution Bulletin 46, no. 5 (May 2003): 642–53. http://dx.doi.org/10.1016/s0025-326x(02)00482-4.

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39

Thomas, C. G., M. E. Gosnell, E. Gawronski, D. Phont-anant, and M. Shibaoka. "The behaviour of inertinite macerals under pulverised fuel (pf) combustion conditions." Organic Geochemistry 20, no. 6 (August 1993): 779–88. http://dx.doi.org/10.1016/0146-6380(93)90062-g.

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40

Wai-chung, Peter Leung. "Strength Development of Concrete Made with Locally Produced Pulverised Fuel Ash." HKIE Transactions 3, no. 2 (January 1996): 15–24. http://dx.doi.org/10.1080/1023697x.1996.10667699.

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41

Bou, E., M. F. Quereda, D. Lever, A. R. Boccaccini, and C. R. Cheeseman. "Production of pulverised fuel ash tiles using conventional ceramic production processes." Advances in Applied Ceramics 108, no. 1 (January 2009): 44–49. http://dx.doi.org/10.1179/174367509x345006.

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42

Bawa, M. A., M. Hadi, H. Dandakouta, and A. Aliyu. "Investigation of Excessive Wear of Ashaka Coal Mill Riser Duct and Idendifying the Optimum Solution." Saudi Journal of Engineering and Technology 7, no. 2 (February 9, 2022): 69–78. http://dx.doi.org/10.36348/sjet.2022.v07i02.002.

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Cement plants use fuel in burning limestone to make clinker in kilns. Due to high cost of fuels, most Cement plants are changing from high-cost liquid fuel like heavy fuel to cheap solid fuel like coal. Ashaka adopt the later. The coal is first pulverised in a ball mill and leaves the mill through a riser duct by pneumatic transport before been used in the kiln as fuel. The riser duct undergoes excessive wear which result in frequent downtime and affect the intendent purpose of fuel substitution. Also, the pulverised coal escaping under pressure through eroded areas on the duct increase the risk of fire and reduce the overall safety of the workshop. Current method which involved patching the duct by welding fail to solve the problem. This work investigates the root cause of the frequent wear of the riser duct by checking the abrasiveness of the coal being transported, checking the effect of the duct profile on wear through simulation using computational fluid dynamics (CFD). Checking the duct material rate of wear and providing the best solution in terms of cost and feasibility. After simulation using CFD it was revealed that the duct profile contributed to the wear rate. Since changing the profile will be costly, a different solution approach was considered i.e., surface finishing. Different Material samples suggested to be used as surface finishing on the duct were tested for wear at different angles using an abrasive test equipment. The test equipment which conforms with ASTM was designed, simulated using CFD and constructed. The best material with good wear resistance was found to be galvanised steel coated with automobile anti gravel and grounded with P1000. Coating the internal of the riser duct with the above material is considered to be the optimum solution in terms of cost and feasibility.

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43

Pawlak-Kruczek, Halina, Michał Ostrycharczyk, Marcin Baranowski, Michał Czerep, and Jacek Zgóra. "Co-Firing of Biomass with Pulverised Coal in Oxygen Enriched Atmosphere." Chemical and Process Engineering 34, no. 2 (June 1, 2013): 215–26. http://dx.doi.org/10.2478/cpe-2013-0018.

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The aim of the paper is a comparative study of co-firing high shares of wooden and agro-biomass with hard coal under oxy-fuel and air conditions in the laboratory scale reactor for pulverised fuels. The investigations of co-combustion behaviour NOx and SO2 emission and burnout were carried out for selected blends. Detailed investigations were concentrated on determining the effect of dosing oxygen method into the burner on NOx emission. The paper presents the results of co-firing blends with 20 and 50% share of biomass by mass in air and oxy-combustion condition. Biomass oxy-cofiring integrated with CCS (CO2 capture) technology could be a carbon negative technology. The reduction of NOx emissions in the conditions of oxy-co-firing is dependent on the concentration of oxygen in the primary stream of oxidiser. A significant reduction of NOx was achieved in the case of low oxygen concentration in the primary stream for each investigated blends. Co-firing of biomass with coal in an oxygen enriched atmosphere enhances combustion behaviour, lowers fuel burnout and as a result increases of the boiler efficiency.

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44

Al-Abbas, Audai Hussein, Jamal Naser, David Dodds, and Aaron Blicblau. "Numerical Modelling of Oxy-Fuel Combustion in a Full-Scale Tangentially-Fired Pulverised Coal Boiler." Procedia Engineering 56 (2013): 375–80. http://dx.doi.org/10.1016/j.proeng.2013.03.135.

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45

Coulthard, J., R. Cheng, Jian Yong Zhang, and R. P. Keech. "Test Procedures and Signal Misinterpretation for Electrostatic Gas-Solids Flowmeters." Advanced Materials Research 508 (April 2012): 1–5. http://dx.doi.org/10.4028/www.scientific.net/amr.508.1.

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This paper discusses the current methods used to test electrostatic pulverised fuel meters in a laboratory environment and the precautions to be taken to ensure that meaningful results are obtained. In particular, the effect of particle attrition is discussed and results presented from a laboratory test facility at the University of Teesside.

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46

Tan, O. H., S. J. Wilcox, G. C. Premier, C. K. Tan, and J. Ward. "Monitoring pulverised coal flames." Journal of the Energy Institute 80, no. 3 (September 1, 2007): 131–39. http://dx.doi.org/10.1179/174602207x216237.

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47

WOOLEY, GR, RM CONLIN, and RE JOYCE. "DISCUSSION. PULVERISED FUEL ASH CONCRETE IN CONSTRUCTION OF NATURAL DRAUGHT COOLING TOWERS." Proceedings of the Institution of Civil Engineers 86, no. 6 (December 1989): 1205–7. http://dx.doi.org/10.1680/iicep.1989.3663.

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48

Adell, V., C. R. Cheeseman, M. Ferraris, M. Salvo, F. Smeacetto, and A. R. Boccaccini. "Characterising the sintering behaviour of pulverised fuel ash using heating stage microscopy." Materials Characterization 58, no. 10 (October 2007): 980–88. http://dx.doi.org/10.1016/j.matchar.2006.10.004.

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49

Bwalya, M. M., and M. H. Moys. "A model for pulverised fuel production in an air-swept tube mill." Minerals Engineering 43-44 (April 2013): 154–58. http://dx.doi.org/10.1016/j.mineng.2012.11.005.

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50

Thompson, D., and B. B. Argent. "Thermodynamic equilibrium study of trace element mobilisation under pulverised fuel combustion conditions." Fuel 81, no. 3 (February 2002): 345–61. http://dx.doi.org/10.1016/s0016-2361(01)00145-4.

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