Incineration Kinetic Analysis of Upstream Oily Sludge and Sectionalized Modeling in Differential/Integral Method
As the most significant solid residue generated in the oil production industry, upstream oily sludge was regarded as hazardous waste in China due to its toxicity and ignitability, and to date, the incineration process has been considered the most efficient method in practice. Due to the complicated...
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doaj-8402b6fe19444a7da5b6273ef542fcf12020-11-25T01:29:14ZengMDPI AGInternational Journal of Environmental Research and Public Health1660-46012019-01-0116338410.3390/ijerph16030384ijerph16030384Incineration Kinetic Analysis of Upstream Oily Sludge and Sectionalized Modeling in Differential/Integral MethodYanqing Zhang0Xiaohui Wang1Yuanfeng Qi2Fei Xi3School of Environmental and Municipal Engineering, Qingdao University of Technology, Qingdao 266033, ChinaTechnical Test Center of Shengli Oil Field, Dongying 257001, ChinaSchool of Environmental and Municipal Engineering, Qingdao University of Technology, Qingdao 266033, ChinaSchool of Environmental and Municipal Engineering, Qingdao University of Technology, Qingdao 266033, ChinaAs the most significant solid residue generated in the oil production industry, upstream oily sludge was regarded as hazardous waste in China due to its toxicity and ignitability, and to date, the incineration process has been considered the most efficient method in practice. Due to the complicated components of oily sludge, a kinetic model of the incineration process was difficult to build, and is still absent in engineering use. In this study, multiple non-isothermal thermogravimetric analysis (TGA) and differential scanning calorimetry (DSC) analysis were applied for the kinetic analysis of upstream oily sludge in air conditions. A viewpoint regarding the rules to sectionalize the reaction stages was raised, and a differential integral method to obtain the incineration kinetic model was provided. The results showed that four stages that were divided based on the weight-loss regions in the TGA curves and the endothermic/exothermic sections in the DSC curves were suitable to obtain an incineration kinetic model of oily sludge. The integral method was beneficial for obtaining the average activation energy of each stage, and the differential method was suitable for gaining the nth-order reaction rate equation and the pre-exponential factor before the operating temperature became lower than 635.968 °C. The average activation energies of stages one, two, three, and four were 60.87 KJ/mol, 78.11 KJ/mol, 98.82 KJ/mol, and 15.96 KJ/mol, respectively. The nth-order reaction rate equations and pre-exponential factors of stages one, two, and three were 0.82, 3.50, and 2.50, and <inline-formula> <math display="inline"> <semantics> <mrow> <msup> <mi mathvariant="normal">e</mi> <mrow> <mn>13.32</mn> </mrow> </msup> <msup> <mrow> <mi>min</mi> </mrow> <mrow> <mo>−</mo> <mn>1</mn> </mrow> </msup> </mrow> </semantics> </math> </inline-formula>, <inline-formula> <math display="inline"> <semantics> <mrow> <msup> <mi mathvariant="normal">e</mi> <mrow> <mn>19.69</mn> </mrow> </msup> <msup> <mrow> <mi>min</mi> </mrow> <mrow> <mo>−</mo> <mn>1</mn> </mrow> </msup> </mrow> </semantics> </math> </inline-formula>, and <inline-formula> <math display="inline"> <semantics> <mrow> <msup> <mi mathvariant="normal">e</mi> <mrow> <mn>21.00</mn> </mrow> </msup> <msup> <mrow> <mi>min</mi> </mrow> <mrow> <mo>−</mo> <mn>1</mn> </mrow> </msup> </mrow> </semantics> </math> </inline-formula>, respectively.https://www.mdpi.com/1660-4601/16/3/384oily sludgeincinerationkineticmodelingdifferential/integral method |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Yanqing Zhang Xiaohui Wang Yuanfeng Qi Fei Xi |
spellingShingle |
Yanqing Zhang Xiaohui Wang Yuanfeng Qi Fei Xi Incineration Kinetic Analysis of Upstream Oily Sludge and Sectionalized Modeling in Differential/Integral Method International Journal of Environmental Research and Public Health oily sludge incineration kinetic modeling differential/integral method |
author_facet |
Yanqing Zhang Xiaohui Wang Yuanfeng Qi Fei Xi |
author_sort |
Yanqing Zhang |
title |
Incineration Kinetic Analysis of Upstream Oily Sludge and Sectionalized Modeling in Differential/Integral Method |
title_short |
Incineration Kinetic Analysis of Upstream Oily Sludge and Sectionalized Modeling in Differential/Integral Method |
title_full |
Incineration Kinetic Analysis of Upstream Oily Sludge and Sectionalized Modeling in Differential/Integral Method |
title_fullStr |
Incineration Kinetic Analysis of Upstream Oily Sludge and Sectionalized Modeling in Differential/Integral Method |
title_full_unstemmed |
Incineration Kinetic Analysis of Upstream Oily Sludge and Sectionalized Modeling in Differential/Integral Method |
title_sort |
incineration kinetic analysis of upstream oily sludge and sectionalized modeling in differential/integral method |
publisher |
MDPI AG |
series |
International Journal of Environmental Research and Public Health |
issn |
1660-4601 |
publishDate |
2019-01-01 |
description |
As the most significant solid residue generated in the oil production industry, upstream oily sludge was regarded as hazardous waste in China due to its toxicity and ignitability, and to date, the incineration process has been considered the most efficient method in practice. Due to the complicated components of oily sludge, a kinetic model of the incineration process was difficult to build, and is still absent in engineering use. In this study, multiple non-isothermal thermogravimetric analysis (TGA) and differential scanning calorimetry (DSC) analysis were applied for the kinetic analysis of upstream oily sludge in air conditions. A viewpoint regarding the rules to sectionalize the reaction stages was raised, and a differential integral method to obtain the incineration kinetic model was provided. The results showed that four stages that were divided based on the weight-loss regions in the TGA curves and the endothermic/exothermic sections in the DSC curves were suitable to obtain an incineration kinetic model of oily sludge. The integral method was beneficial for obtaining the average activation energy of each stage, and the differential method was suitable for gaining the nth-order reaction rate equation and the pre-exponential factor before the operating temperature became lower than 635.968 °C. The average activation energies of stages one, two, three, and four were 60.87 KJ/mol, 78.11 KJ/mol, 98.82 KJ/mol, and 15.96 KJ/mol, respectively. The nth-order reaction rate equations and pre-exponential factors of stages one, two, and three were 0.82, 3.50, and 2.50, and <inline-formula> <math display="inline"> <semantics> <mrow> <msup> <mi mathvariant="normal">e</mi> <mrow> <mn>13.32</mn> </mrow> </msup> <msup> <mrow> <mi>min</mi> </mrow> <mrow> <mo>−</mo> <mn>1</mn> </mrow> </msup> </mrow> </semantics> </math> </inline-formula>, <inline-formula> <math display="inline"> <semantics> <mrow> <msup> <mi mathvariant="normal">e</mi> <mrow> <mn>19.69</mn> </mrow> </msup> <msup> <mrow> <mi>min</mi> </mrow> <mrow> <mo>−</mo> <mn>1</mn> </mrow> </msup> </mrow> </semantics> </math> </inline-formula>, and <inline-formula> <math display="inline"> <semantics> <mrow> <msup> <mi mathvariant="normal">e</mi> <mrow> <mn>21.00</mn> </mrow> </msup> <msup> <mrow> <mi>min</mi> </mrow> <mrow> <mo>−</mo> <mn>1</mn> </mrow> </msup> </mrow> </semantics> </math> </inline-formula>, respectively. |
topic |
oily sludge incineration kinetic modeling differential/integral method |
url |
https://www.mdpi.com/1660-4601/16/3/384 |
work_keys_str_mv |
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