Code: | EQ0082 | Acronym: | PS I |
Keywords | |
---|---|
Classification | Keyword |
OFICIAL | Technological Sciences (Chemical Engineering) |
Active? | Yes |
Responsible unit: | Department of Chemical and Biological Engineering |
Course/CS Responsible: | Master in Chemical Engineering |
Acronym | No. of Students | Study Plan | Curricular Years | Credits UCN | Credits ECTS | Contact hours | Total Time |
---|---|---|---|---|---|---|---|
MIEQ | 93 | Syllabus | 3 | - | 6 | 63 | 162 |
The main aim of this course is to illustrate the importance of separation and purification processes for the technological and economical feasibility of industrial processes, giving the students the necessary background for the selection, analysis and design of some of the most common separation processes that can be found in the chemical and similar industries. In particular: solvent extraction, distillation, evaporation and drying.
The students are expected to attain the following skills:
- Identify the basic principles governing the different classes of separation processes;
- Choose the process (or processes) more adequate to attain the desired separation/purification;
- Do the simplified design of the equipment for solvent extraction, distillation, evaporation and drying, identifying the influence of the main operating and design variables in the final separation.
- Present alternatives for energy conservation in distillation processes.
Knowledge of solution thermodynamics and mass end energy balances.
INTRODUCTION: Characterization and classification of separation processes. Notion of separating agent, recovery and purity.
SOLVENT EXTRACTION: The importance of solvent extraction. Liquid-Liquid and solid-liquid extraction processes. Description of the liquid-liquid and solid-liquid equilibrium. Extraction in a single equilibrium stage and in units with several equilibrium stages operating in cross and counter-current flow. Analysis of the influence of the different operating and design variables in the separation using algebraic and graphic methods. Brief introduction to supercritical extraction and aqueous two phase systems. Reference to the use of ionic liquids as solvents.
BINARY DISTILLATION: The importance of distillation in the chemical and related industries. Brief revision on the design of flash units and calculation of vapour-liquid equilibrium. Design of conventional and complex distillation columns by the McCabe-Thiele method. Notion of overall, stage and point efficiency. Application of the Murphree and vaporization efficiencies to the design of distillation columns.
MULTICOMPONENT DISTILLATION: Distinction between simulation and design methods. Rigorous and shortcut design methods. Design of multicomponent distillation columns by the shortcut method of Gilliland - Underwood - Fenske –Kirkbride. Derivation of the MESH equations for rigorous design and simulation of distillation columns. The open access simulator COCO. Reference to extractive, azeotropic and reactive distillation. Approximate design of distillation columns for binary heterogeneous azeotropic mixtures.
BATCH DISTILLATION: Comparison between batch and continuous distillation. Analysis of the simple distillation process (Rayleigh distillation), distillation units operating at constant reflux, constant distillate composition and total reflux.
ENERGY CONSERVATION IN DISTILLATION PROCESSES: Analysis of the different strategies for energy conservation in distillation processes including the optimization of the operating conditions, energy integration of the distillation columns, intermediate reboilers and condensers and vapour recompression.
EVAPORATION: Types of industrial evaporators and their applications. Economy and capacity of a system of evaporators. Calculation of the temperature of liquid solutions. Notion of boiling point rise (BPR) and the use of Duhring diagrams. Analysis of a single effect evaporator. Design of multiple-effect evaporators operating in counter and co-current.
DRYING AND HUMIDIFICATION: Types of industrial dryers and their applications. Definition of absolute humidity, relative humidity, adiabatic saturation temperature, and wet bulb temperature. Use of the psychrometric diagram. Drying velocity laws. Design of dryers. Brief introduction to the liofilization process.
Exposition of the theoretical concepts and analysis of problems exemplifying their application.
Designation | Weight (%) |
---|---|
Exame | 33,00 |
Teste | 67,00 |
Total: | 100,00 |
Designation | Time (hours) |
---|---|
Estudo autónomo | 99,00 |
Frequência das aulas | 63,00 |
Total: | 162,00 |
According to FEUP's regulations.
1) The student may choose between distributed evaluation or final exam.
2) If the student chooses distributed evaluation, the final grade will be the average of the classifications obtained in the 3 midterm exams.
3) If the student misses one of the midterm exams, or wants to improve the classification obtained in one of the midterm exams, he/she may, on the date of the 3rd midterm exam, choose to take the 3rd+1st or 3rd+2nd midterm exams, which will have a weight of 2/3 in the final grade.
4) The final grade of 20 will only be given if the student attains the grade of 20,0 in all evaluation components.
Three mid-term exams of 90 minutes.
Not applicable
By final exam.
By final exam.