Hydrodynamic study of low-grade Indian coal and sawdust as bed inventory in a pressurized circulating fluidized bed

被引:20
作者
Mahapatro, Abinash [1 ]
Mahanta, Pinakeswar [1 ]
Jana, Kuntal [2 ]
机构
[1] Indian Inst Technol Guwahati, Dept Mech Engn, Gauhati 781039, Assam, India
[2] Natl Inst Technol Durgapur, Dept Mech Engn, Durgapur 713209, W Bengal, India
关键词
Pressurized circulating fluidized bed; Low-grade coal; Sawdust; Hydrodynamic study; Experiment; HEAT-TRANSFER BEHAVIOR; GASIFICATION; BIOMASS; COMBUSTION; BLENDS; RISER; COCOMBUSTION; PARAMETERS;
D O I
10.1016/j.energy.2019.116234
中图分类号
O414.1 [热力学];
学科分类号
摘要
Low-grade coal and biomass waste such as bamboo dust, sawdust, rice husk, etc. are abundantly available in India. Utilization of such resources to generate electricity is a challenging task with conventional methods. Atmospheric circulating fluidized bed (ACFB) is considered to be one of the potential devices to utilize coal or biomass or both for power production through gasification or combustion routes. In this paper, the effect of various operating parameters such as bed inventory, particle size, superficial velocity, blends of coal with sawdust (percentage by weight) and operating pressure on bed hydrodynamics, i.e., bed voidage, suspension density, and solid circulation rate were studied experimentally in a pressurized circulating fluidized bed (PCFB). The bed voidage decreases with an increase in operating pressure and increases with an increase in particle size. Maximum of 8.2% decrement in bed voidage is observed as operating pressure varies from atmospheric to 4 bar. Further, the suspension density is found to increase with an increase in inventory weight. Peak increment of 28.3% in suspension density is perceived with an increase in inventory weights at a pressure of 4 bar. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页数:9
相关论文
共 50 条
[31]   An Eulerian-Eulerian multifluid simulation for co-combustion of coal and sawdust in industrial scale circulating fluidized bed boiler [J].
Singh, Vasujeet ;
Nemalipuri, Pruthiviraj ;
Das, Harish Chandra ;
Vitankar, Vivek .
CLEANER ENERGY SYSTEMS, 2025, 10
[32]   Effect of pressure on loop seal operation for a pressurized circulating fluidized bed [J].
Cheng, LM ;
Basu, P .
POWDER TECHNOLOGY, 1999, 103 (03) :203-211
[33]   Effect of pressure on char combustion in a pressurized circulating fluidized bed boiler [J].
MacNeil, S ;
Basu, P .
FUEL, 1998, 77 (04) :269-275
[34]   Hydrodynamic characteristics of a large-scale triple-bed combined circulating fluidized bed [J].
Fushimi, Chihiro ;
Guan, Guoqing ;
Nakamura, Yu ;
Ishizuka, Masanori ;
Tsutsumi, Atsushi ;
Matsuda, Satoru ;
Hatano, Hiroyuki ;
Suzuki, Yoshizo .
POWDER TECHNOLOGY, 2011, 209 (1-3) :1-8
[35]   Factors affecting steam gasification rate of low rank coal char in a pressurized fluidized bed [J].
Matsuoka, Koichi ;
Kajiwara, Daisuke ;
Kuramoto, Koji ;
Sharma, Atul ;
Suzuki, Yoshizo .
FUEL PROCESSING TECHNOLOGY, 2009, 90 (7-8) :895-900
[36]   Bed-inventory overturn mechanism for pant-leg circulating fluidized bed boilers [J].
Wang, Zhe ;
Sun, Jining ;
Yang, Zhiwei ;
West, Logan ;
Li, Zheng .
POWDER TECHNOLOGY, 2011, 214 (03) :469-476
[37]   Experimental study on combustion characteristics of pulverized coal preheated in a circulating fluidized bed [J].
Man, Chengbo ;
Zhu, Jianguo ;
Ouyang, Ziqu ;
Liu, Jingzhang ;
Lyu, Qinggang .
FUEL PROCESSING TECHNOLOGY, 2018, 172 :72-78
[38]   Role of cobalt and calcium on coal catalytic hydrogasification in a pressurized fluidized bed [J].
Qu, Xuan ;
Yan, Shuai ;
Yan, Xiaoqiang ;
Zhang, Jianshu ;
Zheng, Qi ;
An, Yingbao .
FUEL, 2019, 239 :347-356
[39]   A comprehensive simulation of catalytic coal gasification in a pressurized jetting fluidized bed [J].
Li, Weiwei ;
Song, Yuncai .
FUEL, 2022, 317
[40]   Co-utilization of two coal mine residues: Non-catalytic co-combustion of coal bed methane and coal gangue in a circulating fluidized bed [J].
Chen, Yanrong ;
Li, Haojie ;
Yang, Zhongqing ;
Fan, Hu .
ADVANCES IN MECHANICAL ENGINEERING, 2015, 7 (09) :1-8