CIESC Journal ›› 2019, Vol. 70 ›› Issue (8): 3033-3039.DOI: 10.11949/j.issn.0438-1157.20190099
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Yiqun HUANG1(),Man ZHANG1,Miao MIAO1,Boyu DENG1,Jin CAI2,Yuxin WU1,Junfu LYU1,Yan JIN2,Hairui YANG1()
Received:
2019-01-29
Revised:
2019-03-18
Online:
2019-08-05
Published:
2019-08-05
Contact:
Hairui YANG
黄逸群1(),张缦1,苗苗1,邓博宇1,蔡晋2,吴玉新1,吕俊复1,金燕2,杨海瑞1()
通讯作者:
杨海瑞
作者简介:
黄逸群(1993—),男,博士研究生,<email>huangyq1993@163.com</email>
基金资助:
CLC Number:
Yiqun HUANG, Man ZHANG, Miao MIAO, Boyu DENG, Jin CAI, Yuxin WU, Junfu LYU, Yan JIN, Hairui YANG. Combustion kinetics study of oil shale semi-coke[J]. CIESC Journal, 2019, 70(8): 3033-3039.
黄逸群, 张缦, 苗苗, 邓博宇, 蔡晋, 吴玉新, 吕俊复, 金燕, 杨海瑞. 油页岩半焦燃烧动力学研究[J]. 化工学报, 2019, 70(8): 3033-3039.
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URL: https://hgxb.cip.com.cn/EN/10.11949/j.issn.0438-1157.20190099
样品 | 工业分析/% | Qar,net/(kJ/kg) | |||
---|---|---|---|---|---|
Mar | Aar | Var | FCar | ||
桦甸油页岩 | 7.06 | 62.08 | 26.60 | 4.26 | 9517.9 |
桦甸油页岩半焦 | 0.64 | 83.14 | 5.74 | 10.48 | 3767.2 |
Table 1 Proximate analysis and heat value of Huadian oil shale semicoke used in experiments
样品 | 工业分析/% | Qar,net/(kJ/kg) | |||
---|---|---|---|---|---|
Mar | Aar | Var | FCar | ||
桦甸油页岩 | 7.06 | 62.08 | 26.60 | 4.26 | 9517.9 |
桦甸油页岩半焦 | 0.64 | 83.14 | 5.74 | 10.48 | 3767.2 |
燃烧温度/℃ | 氧气浓度/(mol/m3) | n | m | k |
---|---|---|---|---|
800 | 2.178 | 0.995 | 1.115 | 0.112 |
1.936 | 0.926 | 1.115 | 0.112 | |
1.694 | 0.774 | 1.115 | 0.112 | |
1.452 | 0.703 | 1.115 | 0.112 | |
750 | 2.277 | 0.790 | 0.850 | 0.093 |
2.024 | 0.655 | 0.850 | 0.093 | |
1.771 | 0.473 | 0.850 | 0.093 | |
1.518 | 0.398 | 0.850 | 0.093 | |
700 | 2.394 | 0.686 | 0.815 | 0.084 |
2.128 | 0.609 | 0.815 | 0.084 | |
1.862 | 0.496 | 0.815 | 0.084 | |
1.596 | 0.557 | 0.815 | 0.084 | |
650 | 2.529 | 1.019 | 1.149 | 0.060 |
2.248 | 0.782 | 1.149 | 0.060 | |
1.967 | 0.805 | 1.149 | 0.060 | |
1.686 | 0.579 | 1.149 | 0.060 | |
600 | 2.673 | 1.055 | 0.897 | 0.055 |
2.376 | 0.688 | 0.897 | 0.055 | |
2.079 | 0.743 | 0.897 | 0.055 | |
1.782 | 0.503 | 0.897 | 0.055 |
Table 2 Kinetic model parameters
燃烧温度/℃ | 氧气浓度/(mol/m3) | n | m | k |
---|---|---|---|---|
800 | 2.178 | 0.995 | 1.115 | 0.112 |
1.936 | 0.926 | 1.115 | 0.112 | |
1.694 | 0.774 | 1.115 | 0.112 | |
1.452 | 0.703 | 1.115 | 0.112 | |
750 | 2.277 | 0.790 | 0.850 | 0.093 |
2.024 | 0.655 | 0.850 | 0.093 | |
1.771 | 0.473 | 0.850 | 0.093 | |
1.518 | 0.398 | 0.850 | 0.093 | |
700 | 2.394 | 0.686 | 0.815 | 0.084 |
2.128 | 0.609 | 0.815 | 0.084 | |
1.862 | 0.496 | 0.815 | 0.084 | |
1.596 | 0.557 | 0.815 | 0.084 | |
650 | 2.529 | 1.019 | 1.149 | 0.060 |
2.248 | 0.782 | 1.149 | 0.060 | |
1.967 | 0.805 | 1.149 | 0.060 | |
1.686 | 0.579 | 1.149 | 0.060 | |
600 | 2.673 | 1.055 | 0.897 | 0.055 |
2.376 | 0.688 | 0.897 | 0.055 | |
2.079 | 0.743 | 0.897 | 0.055 | |
1.782 | 0.503 | 0.897 | 0.055 |
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