化工学报 ›› 2019, Vol. 70 ›› Issue (8): 2928-2937.DOI: 10.11949/0438-1157.20190411
姜微微1(),郝文倩1,刘雪景1(),韩振南1,岳君容2,许光文1,2()
收稿日期:
2019-04-18
修回日期:
2019-07-01
出版日期:
2019-08-05
发布日期:
2019-08-05
通讯作者:
刘雪景,许光文
作者简介:
姜微微(1994—),女,硕士研究生,基金资助:
Weiwei JIANG1(),Wenqian HAO1,Xuejing LIU1(),Zhennan HAN1,Junrong YUE2,Guangwen XU1,2()
Received:
2019-04-18
Revised:
2019-07-01
Online:
2019-08-05
Published:
2019-08-05
Contact:
Xuejing LIU,Guangwen XU
摘要:
通过微型流化床反应分析仪(MFBRA)和热重分析仪(TGA)对比研究了菱镁矿粉在氮气和空气气氛中的煅烧反应特性和反应动力学特性。结果表明:菱镁矿在氮气和空气中测得的表观活化能相似,说明空气中的氧气对菱镁矿的煅烧没有影响。MFBRA中菱镁矿粉在800℃以上完全分解的时间只有短短数秒,显著少于在TGA中完全分解的时间,揭示了TGA和MFBRA在测定反应动力学方面的差异。MFBRA测定菱镁矿在空气和氮气气氛中分解的表观活化能(约125 kJ/mol)和指前因子(105 s-1)显著低于TGA所得结果(约200 kJ/mol,1015 s-1),进一步测试表明这与TGA中的反应受气氛抑制有关。即菱镁矿在TGA坩埚内分解产生的CO2不能及时随气流排出,抑制了轻烧反应的进行,而MFBRA可有效降低外扩散对反应的影响。但两种仪器测试的反应均遵循成核与生长控制模型。对于流化床反应,证明了MFBRA测试结果具有更高的准确性,为有气体生成的煅烧或分解反应(如菱镁矿轻烧)提供了可靠的反应测试方法和仪器。
中图分类号:
姜微微, 郝文倩, 刘雪景, 韩振南, 岳君容, 许光文. 微型流化床内菱镁矿轻烧反应特性及动力学[J]. 化工学报, 2019, 70(8): 2928-2937.
Weiwei JIANG, Wenqian HAO, Xuejing LIU, Zhennan HAN, Junrong YUE, Guangwen XU. Characteristic and kinetics of light calcination of magnesite in micro fluidized bed reaction analyzer[J]. CIESC Journal, 2019, 70(8): 2928-2937.
模型 | N2 | Air | |||||
---|---|---|---|---|---|---|---|
E/ (kJ/mol) | lgA | R 2 | E/ (kJ/mol) | lgA | R 2 | ||
G(x)= -ln(1-x) | 124.45 | 5.61 | 0.997 | 125.09 | 5.69 | 0.996 | |
G(x)=1-(1-x)1/3 | 128.67 | 5.36 | 0.997 | 129.32 | 5.39 | 0.996 | |
G(x)=1-(1-x)1/2 | 123.25 | 5.30 | 0.998 | 121.08 | 5.08 | 0.998 |
表1 依据MFBRA测试空气和氮气气氛中菱镁矿粉轻烧数据计算的等温模型法表观活化能
Table 1 Activation energy of magnesite calcination reaction calculated according to isothermal model for MFBRA-measured data in N2 and air atmospheres
模型 | N2 | Air | |||||
---|---|---|---|---|---|---|---|
E/ (kJ/mol) | lgA | R 2 | E/ (kJ/mol) | lgA | R 2 | ||
G(x)= -ln(1-x) | 124.45 | 5.61 | 0.997 | 125.09 | 5.69 | 0.996 | |
G(x)=1-(1-x)1/3 | 128.67 | 5.36 | 0.997 | 129.32 | 5.39 | 0.996 | |
G(x)=1-(1-x)1/2 | 123.25 | 5.30 | 0.998 | 121.08 | 5.08 | 0.998 |
模型 | β→0 | β=1℃/min | β=5℃/min | β=10℃/min | ||||
---|---|---|---|---|---|---|---|---|
E/(kJ/mol) | E/(kJ/mol) | r | E/(kJ/mol) | r | E/(kJ/mol) | r | ||
N2 | G(x)= -ln(1-x) | 201.72 | 187.88 | 0.994 | 224.46 | 0.997 | 224.81 | 0.997 |
G(x)=1- (1-x)1/2 | 191.02 | 187.88 | 0.994 | 224.48 | 0.997 | 224.84 | 0.997 | |
G(x)=1- (1-x)1/3 | 228.12 | 166.02 | 0.993 | 198.53 | 0.997 | 202.75 | 0.996 | |
air | G(x)= -ln(1-x) | 236.76 | 225.72 | 0.997 | 224.79 | 0.997 | 224.61 | 0.997 |
G(x)=1-(1-x)1/2 | 197.21 | 187.14 | 0.995 | 186.82 | 0.996 | 186.59 | 0.995 | |
G(x)=1-(1-x)1/3 | 209.74 | 199.72 | 0.997 | 198.83 | 0.997 | 198.62 | 0.997 |
表2 利用Coats-Redfern公式根据文献报道的机理模型拟合TGA测试数据的结果
Table 2 Fitting results using Coats-Redfern formula for literature-reported mechanism models based on TGA data
模型 | β→0 | β=1℃/min | β=5℃/min | β=10℃/min | ||||
---|---|---|---|---|---|---|---|---|
E/(kJ/mol) | E/(kJ/mol) | r | E/(kJ/mol) | r | E/(kJ/mol) | r | ||
N2 | G(x)= -ln(1-x) | 201.72 | 187.88 | 0.994 | 224.46 | 0.997 | 224.81 | 0.997 |
G(x)=1- (1-x)1/2 | 191.02 | 187.88 | 0.994 | 224.48 | 0.997 | 224.84 | 0.997 | |
G(x)=1- (1-x)1/3 | 228.12 | 166.02 | 0.993 | 198.53 | 0.997 | 202.75 | 0.996 | |
air | G(x)= -ln(1-x) | 236.76 | 225.72 | 0.997 | 224.79 | 0.997 | 224.61 | 0.997 |
G(x)=1-(1-x)1/2 | 197.21 | 187.14 | 0.995 | 186.82 | 0.996 | 186.59 | 0.995 | |
G(x)=1-(1-x)1/3 | 209.74 | 199.72 | 0.997 | 198.83 | 0.997 | 198.62 | 0.997 |
Analyzer | E/(kJ/mol) | lgA | G(x) |
---|---|---|---|
TGA (N2) | 205.94 | 15.68 | -ln(1-x) |
TGA (air) | 236.60 | 15.81 | -ln(1-x) |
MFBRA (N2) | 125.74 | 5.61 | -ln(1-x) |
MFBRA (air) | 124.16 | 5.69 | -ln(1-x) |
表3 利用TGA和MFBRA测定的氮气和空气气氛中的菱镁矿粉轻烧动力学参数
Table 3 Kinetic parameters of magnesite calcination in N2 and air atmospheres measured using TGA and MFBRA
Analyzer | E/(kJ/mol) | lgA | G(x) |
---|---|---|---|
TGA (N2) | 205.94 | 15.68 | -ln(1-x) |
TGA (air) | 236.60 | 15.81 | -ln(1-x) |
MFBRA (N2) | 125.74 | 5.61 | -ln(1-x) |
MFBRA (air) | 124.16 | 5.69 | -ln(1-x) |
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