ปริมาณพลังงานของแก๊สเชื้อเพลิงจากเหง้ามันสำปะหลังในเครื่องปฏิกรณ์ฟลูอิไดซ์เบด
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ส.ค. 31, 2018
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ปริมาณพลังงาน; การผลิตแก๊สเชื้อเพลิง; แก๊สเชื้อเพลิง; เหง้ามันสำปะหลัง; ฟลูอิไดซ์เบด
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บทคัดย่อ
การผลิตแก๊สเชื้อเพลิงของเหง้ามันสำปะหลังในเครื่องปฏิกรณ์ฟลูอิไดซ์เบดเป็นการศึกษาหาปริมาณผลได้ของผลิตภัณฑ์และปริมาณพลังงานของแก๊สเชื้อเพลิงที่ระดับอุณหภูมิต่าง ๆ มีวัตถุประสงค์เพื่อศึกษาอุณหภูมิปฏิกิริยา 5 ระดับ คือ 500 600 700 800 และ 900 องศาเซลเซียสต่อปริมาณผลได้ของผลิตภัณฑ์และปริมาณพลังงานของแก๊สเชื้อเพลิง ซึ่งแก๊สแอลพีจีคือแหล่งพลังงานความร้อนสำหรับอุ่นเครื่องก่อนทำการทดลองและระหว่างทดลองและอากาศถูกใช้เป็นแก๊สพา ปริมาณผลได้ของผลิตภัณฑ์ได้ จากการสมดุลมวลก่อนและหลังการทดลอง โดยมีเครื่องวิเคราะห์แก๊ส GC 8A สำหรับวิเคราะห์องค์ประกอบแก๊ส ผลการทดลองพบว่า อุณหภูมิปฏิกิริยา 900 องศาเซลเซียส ให้ปริมาณผลได้ของแก๊สสูงสุดร้อยละ 90.9 โดยน้ำหนัก แต่แก๊สที่ได้มีค่าความร้อนต่ำสุดเป็น 12 เมกะจูลต่อกิโลกรัม ขณะที่อุณหภูมิปฏิกิริยา 800 องศาเซลเซียส คืออุณหภูมิที่เหมาะสำหรับผลิตแก๊สเชื้อเพลิง เพราะมีปริมาณผลได้ของแก๊สและปริมาณพลังงานของแก๊สร้อยละ 85 โดยนํ้าหนัก
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รูปแบบการอ้างอิง
[1]
แดงทน ว. และ ดวงอุปมา เ., “ปริมาณพลังงานของแก๊สเชื้อเพลิงจากเหง้ามันสำปะหลังในเครื่องปฏิกรณ์ฟลูอิไดซ์เบด”, RMUTI Journal, ปี 11, ฉบับที่ 2, น. 88–99, ส.ค. 2018.
ประเภทบทความ
บทความวิจัย
เอกสารอ้างอิง
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[9] Yang, E., Jun, M., Haijun, H., and Wenfu, C. (2015). Chemical Composition and Potential Bioactivity of Volatile from Fast Pyrolysis of Rice Husk. Journal of Analytical and Applied Pyrolysis. Vol. 112, pp. 394-400. DOI: 10.1016/j.jaap.2015.02.021
[10] Yildiz, G., Ronsse, F., Venderbosch, R., Duren, R. V., Kersten, S. R. A., and Prins, W. (2015). Effect of Biomass Ash in Catalytic Fast Pyrolysis of Pine Wood. Applied Catalysis B: Environmental. Vol. 168-169, pp. 203-11. DOI: 10.1016/j.apcatb.2014.12.044
[11] Zhang, L., Li, T., Quyn, D., Dong, L., Qiu, P., and Li, C. -Z. (2015). Formation of Nascent Char Structure During the Fast Pyrolysis of Mallee Wood and Low-Rank Coals. Fuel. Vol. 150, pp. 486-492. DOI: 10.1016/j.fuel.2015.02.066
[12] Funke, A. and Ziegler, F. (2011). Heat of Reaction Measurements for Hydrothermal Carbonization of Biomass. Bioresource Technology. Vol. 102, Issue 16, pp. 7595-7598. DOI: 10.1016/j.biortech.2011.05.016
[13] McDonald-Wharry, J., Manley-Harris, M., and Pickering, K. (2013). Carbonisation of Biomass-Derived Chars and the Thermal Reduction of a Graphene Oxide Sample Studied Using Raman Spectroscopy. Carbon. Vol. 59, pp. 383-405. DOI: 10.1016/j.carbon.2013.03.033
[14] Du, S. -W., Chen, W. -H., and Lucas, J. A. (2014). Pretreatment of Biomass by Torrefaction and Carbonization for Coal Blend used in Pulverized Coal Injection. Bioresource Technology. Vol. 161, pp. 333-339. DOI: 10.1016/j.biortech.2014.03.090
[15] Sermyagina, E., Saari, J., Kaikko, J., and Vakkilainen, E. (2015). Hydrothermal Carbonization of Coniferous Biomass: Effect of Process Parameters on Mass and Energy Yields. Journal of Analytical and Applied Pyrolysis. Vol. 113, pp. 551-556
[16] Wu, Q., Zhang, S., Hou, B., Zheng, H., Deng, W., and Liu, D. (2015). Study on the Preparation of Wood Vinegar from Biomass Residues by Carbonization Process. Bioresource Technology. Vol. 179, pp. 98-103. DOI: 10.1016/j.biortech.2014.12.026
[17] Bridgwater, A. V., Toft, A. J., and Brammer, J. G. (2002). A Techno-Economic Comparison of Power Production by Biomass Fast Pyrolysis with Gasification and Combustion. Renewable and Sustainable Energy Reviews. Vol. 6, Issue 3, pp. 181-246. DOI: 10.1016/S1364-0321(01)00010-7
[18] Pattiya, A. (2011). Bio-Oil Production Via Fast Pyrolysis of Biomass Residues from Cassava Plants in a Fluidised-Bed Reactor. Bioresource Technology. Vol. 102, Issue 2, pp. 1959-67. DOI: 10.1016/j.biortech.2010.08.117
[19] Theengineeringtoolbox. (2017). Fuel Gases and Heating Values. Access (19 October 2017). Availble (https://www.engineeringtoolbox.com/heating-values-fuel-gases-d_823.html)
[20] Çengel, Y. A. and Boles, M. A. (2006). Thermodynamics: An Engineering Approach 5th edition. The McGraw-Hill Companies. pp. 883-973.
[21] Lanza, R., Dalle Nogare, D., and Canu, P. (2009). Gas Phase Chemistry in Cellulose Fast Pyrolysis. Industrial & Engineering Chemistry Research. Vol. 48, Issue 3, pp. 1391-1399. DOI: 10.1021/ie801280g
[22] Billaud, J., Valin, S., Peyrot, M., and Salvador, S. (2016). Influence of H2O, CO2 and O2 Addition on Biomass Gasification in Entrained Flow Reactor Conditions: Experiments and Modelling. Fuel. Vol. 166, pp. 166-178. DOI: 10.1016/j.fuel.2015.10.046
[23] Chutichai, B., Patcharavorachot, Y., Assabumrungrat, S., and Arpornwichanop, A. (2015). Parametric Analysis of a Circulating Fluidized Bed Biomass Gasifier for Hydrogen Production. Energy. Vol. 82, pp. 406-13. DOI: 10.1016/j.energy.2015.01.051
[2] Arvidsson, M., Morandin, M., and Harvey, S. (2015). Biomass Gasification-Based Syngas Production for a Conventional Oxo Synthesis Plant-Greenhouse Gas Emission Balances and Economic Evaluation. Journal of Cleaner Production. Vol. 99, pp. 192-205. DOI: 10.1016/j.jclepro.2015.03.005
[3] Huijun, G., Laihong, S., Fei, F., and Shouxi, J. (2015). Experiments on Biomass Gasification Using Chemical Looping with Nickel-Based Oxygen Carrier in a 25 kWth Reactor. Applied Thermal Engineering. Vol. 85, pp. 52-60. DOI: 10.1016/j.applthermaleng.2015.03.082
[4] Lanza, R., Dalle Nogare, D., and Canu, P. (2008). Gas Phase Chemistry in Cellulose Fast Pyrolysis. Industrial & Engineering Chemistry Research. Vol. 48, Issue 3, pp. 1391-1399. DOI: 10.1021/ie801280g
[5] Wang, Z., He, T., Qin, J., Wu, J., Li, J., and Zi, Z. (2015). Gasification of Biomass with Oxygen-Enriched Air in a Pilot Scale Two-Stage Gasifier. Fuel. Vol. 150, pp. 386-393. DOI: 10.1016/j.fuel.2015.02.056
[6] Ateş, F. and Erginel, N. (2012). The Regression Analysis of Fast Pyrolysis Product Yields and Determination of Product Quality. Fuel. Vol. 102, pp. 681-690. DOI: 10.1016/j.fuel.2012.05.051
[7] Kim, J. W., Lee, H. W., Lee, I. -G., Jeon, J. -K., Ryu, C., and Park, S. H. (2014). Influence of Reaction Conditions on Bio-Oil Production from Pyrolysis of Construction Waste Wood. Renewable Energy. Vol. 65, pp. 41-48. DOI: 10.1016/j.renene.2013.07.009
[8] Koo, W. -M., Jung, S. -H., and Kim, J. -S. (2014). Production of Bio-Oil with Low Contents of Copper and Chlorine by Fast Pyrolysis of Alkaline Copper Quaternary-Treated Wood in a Fluidized Bed Reactor. Energy. Vol. 68, pp. 555-561. DOI: 10.1016/j.energy.2014.02.020
[9] Yang, E., Jun, M., Haijun, H., and Wenfu, C. (2015). Chemical Composition and Potential Bioactivity of Volatile from Fast Pyrolysis of Rice Husk. Journal of Analytical and Applied Pyrolysis. Vol. 112, pp. 394-400. DOI: 10.1016/j.jaap.2015.02.021
[10] Yildiz, G., Ronsse, F., Venderbosch, R., Duren, R. V., Kersten, S. R. A., and Prins, W. (2015). Effect of Biomass Ash in Catalytic Fast Pyrolysis of Pine Wood. Applied Catalysis B: Environmental. Vol. 168-169, pp. 203-11. DOI: 10.1016/j.apcatb.2014.12.044
[11] Zhang, L., Li, T., Quyn, D., Dong, L., Qiu, P., and Li, C. -Z. (2015). Formation of Nascent Char Structure During the Fast Pyrolysis of Mallee Wood and Low-Rank Coals. Fuel. Vol. 150, pp. 486-492. DOI: 10.1016/j.fuel.2015.02.066
[12] Funke, A. and Ziegler, F. (2011). Heat of Reaction Measurements for Hydrothermal Carbonization of Biomass. Bioresource Technology. Vol. 102, Issue 16, pp. 7595-7598. DOI: 10.1016/j.biortech.2011.05.016
[13] McDonald-Wharry, J., Manley-Harris, M., and Pickering, K. (2013). Carbonisation of Biomass-Derived Chars and the Thermal Reduction of a Graphene Oxide Sample Studied Using Raman Spectroscopy. Carbon. Vol. 59, pp. 383-405. DOI: 10.1016/j.carbon.2013.03.033
[14] Du, S. -W., Chen, W. -H., and Lucas, J. A. (2014). Pretreatment of Biomass by Torrefaction and Carbonization for Coal Blend used in Pulverized Coal Injection. Bioresource Technology. Vol. 161, pp. 333-339. DOI: 10.1016/j.biortech.2014.03.090
[15] Sermyagina, E., Saari, J., Kaikko, J., and Vakkilainen, E. (2015). Hydrothermal Carbonization of Coniferous Biomass: Effect of Process Parameters on Mass and Energy Yields. Journal of Analytical and Applied Pyrolysis. Vol. 113, pp. 551-556
[16] Wu, Q., Zhang, S., Hou, B., Zheng, H., Deng, W., and Liu, D. (2015). Study on the Preparation of Wood Vinegar from Biomass Residues by Carbonization Process. Bioresource Technology. Vol. 179, pp. 98-103. DOI: 10.1016/j.biortech.2014.12.026
[17] Bridgwater, A. V., Toft, A. J., and Brammer, J. G. (2002). A Techno-Economic Comparison of Power Production by Biomass Fast Pyrolysis with Gasification and Combustion. Renewable and Sustainable Energy Reviews. Vol. 6, Issue 3, pp. 181-246. DOI: 10.1016/S1364-0321(01)00010-7
[18] Pattiya, A. (2011). Bio-Oil Production Via Fast Pyrolysis of Biomass Residues from Cassava Plants in a Fluidised-Bed Reactor. Bioresource Technology. Vol. 102, Issue 2, pp. 1959-67. DOI: 10.1016/j.biortech.2010.08.117
[19] Theengineeringtoolbox. (2017). Fuel Gases and Heating Values. Access (19 October 2017). Availble (https://www.engineeringtoolbox.com/heating-values-fuel-gases-d_823.html)
[20] Çengel, Y. A. and Boles, M. A. (2006). Thermodynamics: An Engineering Approach 5th edition. The McGraw-Hill Companies. pp. 883-973.
[21] Lanza, R., Dalle Nogare, D., and Canu, P. (2009). Gas Phase Chemistry in Cellulose Fast Pyrolysis. Industrial & Engineering Chemistry Research. Vol. 48, Issue 3, pp. 1391-1399. DOI: 10.1021/ie801280g
[22] Billaud, J., Valin, S., Peyrot, M., and Salvador, S. (2016). Influence of H2O, CO2 and O2 Addition on Biomass Gasification in Entrained Flow Reactor Conditions: Experiments and Modelling. Fuel. Vol. 166, pp. 166-178. DOI: 10.1016/j.fuel.2015.10.046
[23] Chutichai, B., Patcharavorachot, Y., Assabumrungrat, S., and Arpornwichanop, A. (2015). Parametric Analysis of a Circulating Fluidized Bed Biomass Gasifier for Hydrogen Production. Energy. Vol. 82, pp. 406-13. DOI: 10.1016/j.energy.2015.01.051
