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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Main Authors: Yanqing Zhang, Xiaohui Wang, Yuanfeng Qi, Fei Xi
Format: Article
Language:English
Published: MDPI AG 2019-01-01
Series:International Journal of Environmental Research and Public Health
Subjects:
Online Access:https://www.mdpi.com/1660-4601/16/3/384
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spelling 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 &#176;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>&#8722;</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>&#8722;</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>&#8722;</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 &#176;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>&#8722;</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>&#8722;</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>&#8722;</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
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AT xiaohuiwang incinerationkineticanalysisofupstreamoilysludgeandsectionalizedmodelingindifferentialintegralmethod
AT yuanfengqi incinerationkineticanalysisofupstreamoilysludgeandsectionalizedmodelingindifferentialintegralmethod
AT feixi incinerationkineticanalysisofupstreamoilysludgeandsectionalizedmodelingindifferentialintegralmethod
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