IDEAS home Printed from https://ideas.repec.org/a/gam/jeners/v12y2019i5p884-d211782.html
   My bibliography  Save this article

An Improved Comprehensive Model of Pyrolysis of Large Coal Particles to Predict Temperature Variation and Volatile Component Yields

Author

Listed:
  • Wenning Zhou

    (School of Energy and Environmental Engineering, University of Science and Technology Beijing, Beijing 100083, China
    Beijing Key Laboratory of Energy Saving and Emission Reduction for Metallurgical Industry, University of Science and Technology Beijing, Beijing 100083, China)

  • Hailong Huo

    (School of Energy and Environmental Engineering, University of Science and Technology Beijing, Beijing 100083, China)

  • Qinye Li

    (School of Energy and Environmental Engineering, University of Science and Technology Beijing, Beijing 100083, China)

  • Ruifeng Dou

    (School of Energy and Environmental Engineering, University of Science and Technology Beijing, Beijing 100083, China
    Beijing Key Laboratory of Energy Saving and Emission Reduction for Metallurgical Industry, University of Science and Technology Beijing, Beijing 100083, China)

  • Xunliang Liu

    (School of Energy and Environmental Engineering, University of Science and Technology Beijing, Beijing 100083, China
    Beijing Key Laboratory of Energy Saving and Emission Reduction for Metallurgical Industry, University of Science and Technology Beijing, Beijing 100083, China)

Abstract

In this work, an improved comprehensive model was developed for large coal particles to predict temperature variation and volatile component yields. The kinetics model of volatile component yields, where the volatile matters were assumed to comprise nine species, was combined with heat transfer model. The interaction between volatile yield and heat transfer during pyrolysis of large Maltby coal particles was investigated. An apparent temperature difference has been observed between the surface and core of particles at the initial heating stage. The non-uniform temperature distribution inside coal particles causes non-simultaneous volatile yields release from the surface and core area. The volatile release occurs after the coal temperature rises higher than 350 °C, and its yield steeply increases within the temperature range of 450–520 °C. The peak of volatile release rate corresponds to about 485 °C due to the rapid release of tar and H 2 O. The tar is almost completely released at around 550 °C. With the increasing particle size, the difference in temperature and volatile yield between the surface and core increases at the end of heating. The results are expected to provide insights into the interaction between heat transfer and volatile yields during pyrolysis of large coal particles.

Suggested Citation

  • Wenning Zhou & Hailong Huo & Qinye Li & Ruifeng Dou & Xunliang Liu, 2019. "An Improved Comprehensive Model of Pyrolysis of Large Coal Particles to Predict Temperature Variation and Volatile Component Yields," Energies, MDPI, vol. 12(5), pages 1-15, March.
  • Handle: RePEc:gam:jeners:v:12:y:2019:i:5:p:884-:d:211782
    as

    Download full text from publisher

    File URL: https://www.mdpi.com/1996-1073/12/5/884/pdf
    Download Restriction: no

    File URL: https://www.mdpi.com/1996-1073/12/5/884/
    Download Restriction: no
    ---><---

    References listed on IDEAS

    as
    1. Chen, Zhaohui & Li, Yunjia & Lai, Dengguo & Geng, Sulong & Zhou, Qi & Gao, Shiqiu & Xu, Guangwen, 2018. "Coupling coal pyrolysis with char gasification in a multi-stage fluidized bed to co-produce high-quality tar and syngas," Applied Energy, Elsevier, vol. 215(C), pages 348-355.
    2. Jiang, Xuguang & Chen, Dandan & Ma, Zengyi & Yan, Jianhua, 2017. "Models for the combustion of single solid fuel particles in fluidized beds: A review," Renewable and Sustainable Energy Reviews, Elsevier, vol. 68(P1), pages 410-431.
    3. Zeng, Xi & Wang, Fang & Li, Hongling & Wang, Yin & Dong, Li & Yu, Jian & Xu, Guangwen, 2014. "Pilot verification of a low-tar two-stage coal gasification process with a fluidized bed pyrolyzer and fixed bed gasifier," Applied Energy, Elsevier, vol. 115(C), pages 9-16.
    4. Pei, Pei & Wang, Qicheng & Wu, Daohong, 2015. "Application and research on Regenerative High Temperature Air Combustion technology on low-rank coal pyrolysis," Applied Energy, Elsevier, vol. 156(C), pages 762-766.
    Full references (including those not matched with items on IDEAS)

    Most related items

    These are the items that most often cite the same works as this one and are cited by the same works as this one.
    1. Chen, Zhaohui & Li, Yunjia & Lai, Dengguo & Geng, Sulong & Zhou, Qi & Gao, Shiqiu & Xu, Guangwen, 2018. "Coupling coal pyrolysis with char gasification in a multi-stage fluidized bed to co-produce high-quality tar and syngas," Applied Energy, Elsevier, vol. 215(C), pages 348-355.
    2. Xu, Shipei & Zeng, Xi & Han, Zhennan & Cheng, Jiguang & Wu, Rongcheng & Chen, Zhaohui & Masĕk, Ondřej & Fan, Xianfeng & Xu, Guangwen, 2019. "Quick pyrolysis of a massive coal sample via rapid infrared heating," Applied Energy, Elsevier, vol. 242(C), pages 732-740.
    3. Tuttle, Jacob F. & Blackburn, Landen D. & Andersson, Klas & Powell, Kody M., 2021. "A systematic comparison of machine learning methods for modeling of dynamic processes applied to combustion emission rate modeling," Applied Energy, Elsevier, vol. 292(C).
    4. Enagi, Ibrahim I. & Al-attab, K.A. & Zainal, Z.A., 2018. "Liquid biofuels utilization for gas turbines: A review," Renewable and Sustainable Energy Reviews, Elsevier, vol. 90(C), pages 43-55.
    5. Liu, Peng & Le, Jiawei & Wang, Lanlan & Pan, Tieying & Lu, Xilan & Zhang, Dexiang, 2016. "Relevance of carbon structure to formation of tar and liquid alkane during coal pyrolysis," Applied Energy, Elsevier, vol. 183(C), pages 470-477.
    6. Zhang, Nan & Zhang, Jianliang & Wang, Guangwei & Ning, Xiaojun & Meng, Fanyi & Li, Chuanhui & Ye, Lian & Wang, Chuan, 2022. "Physicochemical characteristics of three-phase products of low-rank coal by hydrothermal carbonization: experimental research and quantum chemical calculation," Energy, Elsevier, vol. 261(PB).
    7. Yuan, XiangZhou & Fan, ShuMin & Choi, Seung Wan & Kim, Hyung-Taek & Lee, Ki Bong, 2017. "Potassium catalyst recovery process and performance evaluation of the recovered catalyst in the K2CO3-catalyzed steam gasification system," Applied Energy, Elsevier, vol. 195(C), pages 850-860.
    8. Elsner, Witold & Wysocki, Marian & Niegodajew, Paweł & Borecki, Roman, 2017. "Experimental and economic study of small-scale CHP installation equipped with downdraft gasifier and internal combustion engine," Applied Energy, Elsevier, vol. 202(C), pages 213-227.
    9. Fang, Neng & Li, Zhengqi & Xie, Cheng & Liu, Shuxuan & Zeng, Lingyan & Chen, Zhichao & Zhang, Bin, 2020. "The application of fly ash gasification for purifying the raw syngas in an industrial-scale entrained flow gasifier," Energy, Elsevier, vol. 195(C).
    10. Choi, Young-Kon & Mun, Tae-Young & Cho, Min-Hwan & Kim, Joo-Sik, 2016. "Gasification of dried sewage sludge in a newly developed three-stage gasifier: Effect of each reactor temperature on the producer gas composition and impurity removal," Energy, Elsevier, vol. 114(C), pages 121-128.
    11. Liu, Peng & Zhang, Dexiang & Wang, Lanlan & Zhou, Yang & Pan, Tieying & Lu, Xilan, 2016. "The structure and pyrolysis product distribution of lignite from different sedimentary environment," Applied Energy, Elsevier, vol. 163(C), pages 254-262.
    12. Rizkiana, Jenny & Guan, Guoqing & Widayatno, Wahyu Bambang & Hao, Xiaogang & Wang, Zhongde & Zhang, Zhonglin & Abudula, Abuliti, 2015. "Oil production from mild pyrolysis of low-rank coal in molten salts media," Applied Energy, Elsevier, vol. 154(C), pages 944-950.
    13. Du, Xin & Li, Yun, 2019. "Experimental comparison and optimization on granular bed filters with three types of filling schemes," Applied Energy, Elsevier, vol. 253(C), pages 1-1.
    14. Jeong, Hyo Jae & Seo, Dong Kyun & Hwang, Jungho, 2014. "CFD modeling for coal size effect on coal gasification in a two-stage commercial entrained-bed gasifier with an improved char gasification model," Applied Energy, Elsevier, vol. 123(C), pages 29-36.
    15. Choi, Young-Kon & Ko, Ji-Ho & Kim, Joo-Sik, 2017. "A new type three-stage gasification of dried sewage sludge: Effects of equivalence ratio, weight ratio of activated carbon to feed, and feed rate on gas composition and tar, NH3, and H2S removal and r," Energy, Elsevier, vol. 118(C), pages 139-146.
    16. Unyaphan, Siriwat & Tarnpradab, Thanyawan & Takahashi, Fumitake & Yoshikawa, Kunio, 2017. "Improvement of tar removal performance of oil scrubber by producing syngas microbubbles," Applied Energy, Elsevier, vol. 205(C), pages 802-812.
    17. Fang, Neng & Li, Zhengqi & Xie, Cheng & Liu, Shuxuan & Lu, Yue & Zeng, Lingyan & Chen, Zhichao, 2021. "Influence of the multi-burner bias angle on the air/particle flow characteristics in an improved fly ash entrained-flow gasifier," Energy, Elsevier, vol. 234(C).
    18. Wang, Fang & Zeng, Xi & Sun, Yanlin & Zhang, Juwei & Zhao, Zhigang & Wang, Yonggang & Xu, Guangwen, 2015. "Jetting pre-oxidation fluidized bed gasification process for caking coal: Fundamentals and pilot test," Applied Energy, Elsevier, vol. 160(C), pages 80-87.
    19. Wang, Chao & Zhu, Lianfeng & Zhang, Mengjuan & Han, Zhennan & Jia, Xin & Bai, Dingrong & Duo, Wenli & Bi, Xiaotao & Abudula, Abuliti & Guan, Guoqing & Xu, Guangwen, 2022. "A two-stage circulated fluidized bed process to minimize tar generation of biomass gasification for fuel gas production," Applied Energy, Elsevier, vol. 323(C).
    20. Li, Jinhu & Ye, Xinhao & Burra, Kiran G. & Lu, Wei & Wang, Zhiwei & Liu, Xuan & Gupta, Ashwani K., 2023. "Synergistic effects during co-pyrolysis and co-gasification of polypropylene and polystyrene," Applied Energy, Elsevier, vol. 336(C).

    Corrections

    All material on this site has been provided by the respective publishers and authors. You can help correct errors and omissions. When requesting a correction, please mention this item's handle: RePEc:gam:jeners:v:12:y:2019:i:5:p:884-:d:211782. See general information about how to correct material in RePEc.

    If you have authored this item and are not yet registered with RePEc, we encourage you to do it here. This allows to link your profile to this item. It also allows you to accept potential citations to this item that we are uncertain about.

    If CitEc recognized a bibliographic reference but did not link an item in RePEc to it, you can help with this form .

    If you know of missing items citing this one, you can help us creating those links by adding the relevant references in the same way as above, for each refering item. If you are a registered author of this item, you may also want to check the "citations" tab in your RePEc Author Service profile, as there may be some citations waiting for confirmation.

    For technical questions regarding this item, or to correct its authors, title, abstract, bibliographic or download information, contact: MDPI Indexing Manager (email available below). General contact details of provider: https://www.mdpi.com .

    Please note that corrections may take a couple of weeks to filter through the various RePEc services.

    IDEAS is a RePEc service. RePEc uses bibliographic data supplied by the respective publishers.