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https://hdl.handle.net/20.500.12104/109975
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Campo DC | Valor | Lengua/Idioma |
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dc.contributor.author | Malik, Abdul | |
dc.date.accessioned | 2025-09-02T20:44:38Z | - |
dc.date.available | 2025-09-02T20:44:38Z | - |
dc.date.issued | 2024-06-28 | |
dc.identifier.uri | https://wdg.biblio.udg.mx | |
dc.identifier.uri | https://hdl.handle.net/20.500.12104/109975 | - |
dc.description.abstract | Calcareous scales can form in industrial and domestic pipelines, heat exchangers, desalination plants, or cooling towers, causing obstruction and flow reduction, high-pressure drops, low heat transfer coefficients, and other harmful effects, resulting in a negative economic impact. The composition of calcareous scales varies depending on the type and quality of the water in which they form and usually consists of carbonate minerals. In this study, we evaluated an organic acid mixture that is environmentally friendly, descaling solution to remove calcareous scales on embedded domestic pipelines. The results presented include speciation diagrams of the descaling solution at different concentrations in contact with calcium carbonate using the software MEDUSA. The results indicate that stable citrate and phosphate complexes are formed at 1 < pH < 4. XRD and FTIR analyses of the recrystallized scales from embedded pipelines in the descaling solution show different calcium carbonate polymorphs. The LPR technique allows us to calculate the corrosion rates of embedded carbon pipeline sections in contact with the descaling solutions at different concentrations. A corrosion rate reduction of 39 % was observed for 0.1 M descaling solution compared with 0.1 M HCl. Two distinct inhibitors were evaluated: one derived from the leaves of Agave Americana, and another from an ionic liquid known as 1-Pentadecyl-3-methylimidazolium bromide. The findings indicate an efficiency range of approximately 34-50% for the agave extract, whereas the ionic liquid exhibited superior performance, achieving efficiencies of 65 to 87%, both cases below the expected values of 90%. Furthermore, simulations of pressure drop in pipelines with calcareous carbonate deposits were conducted using the COMSOL Multiphysics 5.5 software. Thanks to the use of an adaptable mesh, it was possible to predict the dissolution kinetics and the dominant velocity and pressure profiles within the encrusted pipes. An instrumented testing apparatus was designed to investigate the dissolution rate under different flow conditions. | |
dc.description.tableofcontents | Chapter 1 1 1.1 Introduction 1 1.2 Previous research work 4 1.3 Justification 6 1.4 Hypothesis 6 1.5 Main objective 6 1.6 Specific objectives 6 Chapter 2 8 Scale Formation 8 2.1 Overview (Scaling) 8 2.2 Scale formation process in pipes 9 2.3 Mechanism of scaling 13 2.3.1 Nucleation 14 2.3.2 Factors Affecting Scale Formation 16 2.3.3 Effect of Temperature 16 2.3.4 pH Function in Descaling Solution 16 2.4 Role of Acids in Descaling Solution 17 2.5 Fouling 19 2.6 Calcium Chemistry 21 2.7 Corrosion Process 22 2.7.1 Causes of Corrosion Process 24 2.7.2 Factors That Affect the Corrosion Process 25 2.7.3 Nature of Metal 25 2.7.4 Nature of Corroding Environment 27 2.8 Types of Corrosion 27 2.8.1 Uniform Corrosion 28 2.8.2 Uniform Corrosion 28 2.8.3 Galvanic Corrosion 29 2.8.4 Corrosion Erosion and Wear 30 2.8.5 Intergranular Corrosion 30 2.8.6 Cavitation Corrosion 31 2.8.7 Hydrogen Embrittlement 31 2.9 Corrosion Inhibitors 32 Chapter 3 36 3.1 COMSOL Multiphysics 36 3.2 Simulation (COMSOL Multiphysics) 39 3.3 Electrochemical Measurements 42 3.3.1 Tafel Extrapolation 43 3.3.2 Linear Polarization Resistance 44 3.3.3 Electrochemical Impedance Spectroscopy 45 Chapter 4 49 4.1 Introduction 49 4.2 Experimental Procedure for The Research 50 4.2.1 Preparation of the Descaling Solution 50 4.2.2 Preparation of Corrosion Inhibitors 50 4.2.3 Electrochemical Characterization 51 4.2.4 Structural and Physicochemical Characterization 51 4.3 Results And Discussion 52 4.3.1 Characterization of Organic Acids and Compounds 53 4.4 Morphology of The Treated Incrustation 57 4.5 FTIR Analysis of Supernatants and Precipitates 59 4.6 Electrochemical Experiments of Embedded Tubes in the Descaling Solutions. 60 4.7 Potentiodynamic Polarization Measurements and Inhibitors Testing of Agave Plant Extract 62 4.8 Potentiodynamic Polarization Measurement and Inhibitors Testing of Liquid Ionic 1-Pentadecy 1-3- ethylimidazolium Bromide 66 Chapter 5 69 5.1 Introduction 69 5.2 Modeling of The Calcareous Deposit Dissolution 70 5.3 Transport of Diluted Species 70 5.4 Laminar Flow Interface (Spf) 71 5.5 Deformed Geometry (Dg) 74 5.6 Summary 78 Chapter 6 79 Conclusions 79 Bibliography 80 | |
dc.format | application/PDF | |
dc.language.iso | eng | |
dc.publisher | Biblioteca Digital wdg.biblio | |
dc.publisher | Universidad de Guadalajara | |
dc.rights.uri | https://www.riudg.udg.mx/info/politicas.jsp | |
dc.subject | Development Non-Corrosive Biodegradable | |
dc.title | “Development of Simultaneous Non-Corrosive and Biodegradable Descaling and Inhibition System Solution” | |
dc.type | Tesis de Doctorado | |
dc.rights.holder | Universidad de Guadalajara | |
dc.rights.holder | Malik, Abdul | |
dc.coverage | GUADALAJARA, JALISCO | |
dc.type.conacyt | doctoralThesis | |
dc.degree.name | DOCTORADO EN CIENCIAS EN INGENIERIA QUIMICA | |
dc.degree.department | CUCEI | |
dc.degree.grantor | Universidad de Guadalajara | |
dc.rights.access | openAccess | |
dc.degree.creator | DOCTORADO EN CIENCIAS EN INGENIERO EN QUIMICA | |
dc.contributor.director | Casillas Santana, Norberto | |
Aparece en las colecciones: | CUCEI |
Ficheros en este ítem:
Fichero | Tamaño | Formato | |
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DCUCEI10215FT.pdf | 6.4 MB | Adobe PDF | Visualizar/Abrir |
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