Iolanda DE MARCO | ADVANCES IN UNIT OPERATIONS

cod. 0622200008

ADVANCES IN UNIT OPERATIONS

	0622200008
	DEPARTMENT OF INDUSTRIAL ENGINEERING
	EQF7
	CHEMICAL ENGINEERING
	2024/2025

CURRICULUM INNOVATIVE PROCESSES AND NANOTECHNOLOGIES Cohort 2023/2024

	OBBLIGATORIO
	YEAR OF COURSE 2
	YEAR OF DIDACTIC SYSTEM 2019
	AUTUMN SEMESTER

TEACHING UNITS

SSD	CFU	HOURS	ACTIVITY	TYPE OF ACTIVITY
ING-IND/25	6	60	LESSONS	COMPULSORY SUBJECTS, CHARACTERISTIC OF THE CLASS
ING-IND/25	3	30	EXERCISES	COMPULSORY SUBJECTS, CHARACTERISTIC OF THE CLASS

PROFESSORS

	IOLANDA DE MARCO T Curriculum
	LIBERO SESTI OSSEO Curriculum

	Objectives
	AT THE END OF THE COURSE, THE STUDENT HAS ACQUIRED THE FOLLOWING KNOWLEDGE AND ABILITIES. KNOWLEDGE AND UNDERSTANDING: THE STUDENT WILL KNOW 1) THE CRITERIA FOR THE DESIGN AND OPTIMIZATION OF THE HEAT-EXCHANGE NETWORKS FOR ENERGY INTEGRATION; 2) THE PRINCIPLES OF OPERATION AND DESIGN CRITERIA FOR THE LIQUID-LIQUID EXTRACTION IN STAGES; 3) OPERATING AND DESIGN CRITERIA FOR MULTICOMPONENT DISTILLATION BOTH WITH APPROXIMATE AND EXACT METHODS; 4) THE OPERATION AND DESIGN OF THE HOLED PLATE OF A DISTILLATION COLUMN AND THE DESCRIPTION OF NON-IDEAL OF THE FLOW IN THE PLATE; 5) THE OPERATING PRINCIPLES AND DESIGN CRITERIA FOR A COLUMN ADSORPTION / DESORPTION: 6) THE PRINCIPLES OF OPERATION AND DESIGN CRITERIA FOR INDUSTRIAL CRYSTALLIZERS. APPLYING KNOWLEDGE AND UNDERSTANDING – ENGINEERING ANALYSIS THE STUDENT WILL BE ABLE TO SELECT AND USE THE MOST APPROPRIATE CRITERIA FOR THE DESIGN AND ANALYSIS FOR THE EQUIPMENT OBJECT OF THE COURSE. APPLYING KNOWLEDGE AND UNDERSTANDING – ENGINEERING DESIGN THE STUDENT WILL BE ABLE TO DESIGN A HEAT EXCHANGE NETWORK. BE ABLE TO PROPERLY DESIGN THE EQUIPMENT COVERED BY THE COURSE. MAKING JUDGMENTS - ENGINEERING PRACTICE: THE STUDENT WILL KNOW HOW TO INTEGRATE THE KNOWLEDGE RELATED TO THE SIZING OF A CHEMICAL PLANT EVEN IN COMPLEX INDUSTRIAL SITUATIONS. TRANSVERSAL SKILLS -COMMUNICATION SKILLS : THE STUDENT WILL HAVE A REFINED TECHNICAL LANGUAGE AND WILL BE ABLE TO USE COMMUNICATION PROTOCOLS. TRANSVERSAL SKILLS - LEARNING SKILLS: THE STUDENT WILL KNOW HOW TO APPLY THEIR KNOWLEDGE TO DIFFERENT CONTEXTS FROM THOSE PRESENTED DURING THE COURSE AND DEEPEN THE TOPICS COVERED.

AT THE END OF THE COURSE, THE STUDENT HAS ACQUIRED THE FOLLOWING KNOWLEDGE AND ABILITIES.
KNOWLEDGE AND UNDERSTANDING:
THE STUDENT WILL KNOW 1) THE CRITERIA FOR THE DESIGN AND OPTIMIZATION OF THE HEAT-EXCHANGE NETWORKS FOR ENERGY INTEGRATION; 2) THE PRINCIPLES OF OPERATION AND DESIGN CRITERIA FOR THE LIQUID-LIQUID EXTRACTION IN STAGES; 3) OPERATING AND DESIGN CRITERIA FOR MULTICOMPONENT DISTILLATION BOTH WITH APPROXIMATE AND EXACT METHODS; 4) THE OPERATION AND DESIGN OF THE HOLED PLATE OF A DISTILLATION COLUMN AND THE DESCRIPTION OF NON-IDEAL OF THE FLOW IN THE PLATE; 5) THE OPERATING PRINCIPLES AND DESIGN CRITERIA FOR A COLUMN ADSORPTION / DESORPTION: 6) THE PRINCIPLES OF OPERATION AND DESIGN CRITERIA FOR INDUSTRIAL CRYSTALLIZERS.

APPLYING KNOWLEDGE AND UNDERSTANDING – ENGINEERING ANALYSIS
THE STUDENT WILL BE ABLE TO SELECT AND USE THE MOST APPROPRIATE CRITERIA FOR THE DESIGN AND ANALYSIS FOR THE EQUIPMENT OBJECT OF THE COURSE.

APPLYING KNOWLEDGE AND UNDERSTANDING – ENGINEERING DESIGN
THE STUDENT WILL BE ABLE TO DESIGN A HEAT EXCHANGE NETWORK. BE ABLE TO PROPERLY DESIGN THE EQUIPMENT COVERED BY THE COURSE.

MAKING JUDGMENTS - ENGINEERING PRACTICE:
THE STUDENT WILL KNOW HOW TO INTEGRATE THE KNOWLEDGE RELATED TO THE SIZING OF A CHEMICAL PLANT EVEN IN COMPLEX INDUSTRIAL SITUATIONS.

TRANSVERSAL SKILLS -COMMUNICATION SKILLS :
THE STUDENT WILL HAVE A REFINED TECHNICAL LANGUAGE AND WILL BE ABLE TO USE COMMUNICATION PROTOCOLS.

TRANSVERSAL SKILLS - LEARNING SKILLS:
THE STUDENT WILL KNOW HOW TO APPLY THEIR KNOWLEDGE TO DIFFERENT CONTEXTS FROM THOSE PRESENTED DURING THE COURSE AND DEEPEN THE TOPICS COVERED.

	Prerequisites
	PREREQUISITES ARE THE MASTERY OF THE BASIC CONCEPTS OF CHEMICAL ENGINEERING, WITH PARTICULAR REFERENCE TO THERMODYNAMICS, TO THE MATERIAL, ENERGY AND MOMENTUM BALANCES, TO THE KNOWLEDGE OF THE OPERATION AND DESIGN OF SOME OPERATION UNIT, THE BASE OF PLANT MEASUREMENT AND CONTROL.

	Contents
	0. INTRODUCTION (2 H TH): 1. HEAT EXCHANGE NETWORK INTEGRATION (LINNHOFF OPTIMIZATION) (12 H TH, 8 H EX): 1.1 PLANT, PROCESS, UTILITIES. COLD AND HOT STREAMS. COMPOSITE CURVES. PLANT OVERALL BALANCE. CORRELATION BETWEEN TEMPERATURE DIFFERENCE AND EXTERNAL ENERGY REQUIREMENTS . 1.2 PINCH POINT DETERMINATION. GRAPHS AND PLANT STREAMS. GOLDEN RULES. SOLUTION OF THE HEAT EXCHANGE NETWORK FOR MAXIMUM ENERGY RECOVERY (MER). 1.3 ALREADY EXISTING PLANTS. REMOVAL OF HEAT EXCHANGERS FROM A NETWORK AND ENERGY COST. ECONOMIC OPTIMIZATION BETWEEN PLANT AND OPERATIVE COSTS. 2. LIQUID-LIQUID EXTRACTION (10 H TH, 8 H EX): 2.1 EXTRACTION PRINCIPLES. EXPERIMENTAL PLOT OF A TERNARY DIAGRAM. 2.2 EXTRACTION DESIGN: ANALYTICAL AND GRAPHICAL SET UP. PROBLEM CHECK. 3. MULTICOMPONENT DISTILLATION (14 H TH, 8 H EX): 3.1 BINARY AND MULTICOMPONENT SYSTEMS. REMIND OF IDEAL MIXTURE DISTILLATION. FLASH. 3.2 HEIGTH OF DISTILLATION COLUMNS. STAGE NUMBERS AT INFIITE REFLUX (FENSKE) AND AT PINCH CONDITION (UNDERWOOD). GILLILAND CORRELATION. “FUG” INTEGRATED METHOD AND NUMBER OF STAGES ESTIMATION. 3.3 CROSS SECTION DESIGN. FLUID DYNAMIC E DESIGN PARAMETERS FOR A PLATE. OPERATIVE FLEXIBILITY. EFFICIENCY. 4. ADSORPTION / DESORPTION (10 H TH, 2 H EX): 4.1 DESCRIPTION AND TYPICAL APPLICATIONS. THE ISOTHERMS OF EQUILIBRIUM. DESCRIPTIVE AND MECHANISMS EQUATIONS 4.2 DESIGN OF A SORPTION / DESORPTION. THE BALANCE SHEETS OF MATTER. BREAKTHROUGH CURVES. DESORPTION. CYCLES OF ADSORPTION / DESORPTION. PRESSURE SWING ABSORPTION (PSA). 5. CRYSTALLIZATION (12 H TH, 4 H EX): 5.1 DESCRIPTION OF THE CRYSTALLIZATION. CRYSTALLIZATION INDUCED BY PRESSURE, TEMPERATURE. NUCLEATION AND GROWTH. THE CRYSTALLIZATION MODELS. HOMOGENEOUS AND HETEROGENEOUS DESCRIPTIVE MODELS. 5.2 POPULATION BALANCE OF CRYSTALS. SIZING OF A CRYSTALLIZER. CRITICAL EVALUATION OF THE PROJECT LIMITS.

Contents

0. INTRODUCTION (2 H TH):
1. HEAT EXCHANGE NETWORK INTEGRATION (LINNHOFF OPTIMIZATION) (12 H TH, 8 H EX):
1.1 PLANT, PROCESS, UTILITIES. COLD AND HOT STREAMS. COMPOSITE CURVES. PLANT OVERALL BALANCE. CORRELATION BETWEEN TEMPERATURE DIFFERENCE AND EXTERNAL ENERGY REQUIREMENTS .
1.2 PINCH POINT DETERMINATION. GRAPHS AND PLANT STREAMS. GOLDEN RULES. SOLUTION OF THE HEAT EXCHANGE NETWORK FOR MAXIMUM ENERGY RECOVERY (MER).
1.3 ALREADY EXISTING PLANTS. REMOVAL OF HEAT EXCHANGERS FROM A NETWORK AND ENERGY COST. ECONOMIC OPTIMIZATION BETWEEN PLANT AND OPERATIVE COSTS.
2. LIQUID-LIQUID EXTRACTION (10 H TH, 8 H EX):
2.1 EXTRACTION PRINCIPLES. EXPERIMENTAL PLOT OF A TERNARY DIAGRAM.
2.2 EXTRACTION DESIGN: ANALYTICAL AND GRAPHICAL SET UP. PROBLEM CHECK.
3. MULTICOMPONENT DISTILLATION (14 H TH, 8 H EX):
3.1 BINARY AND MULTICOMPONENT SYSTEMS. REMIND OF IDEAL MIXTURE DISTILLATION. FLASH.
3.2 HEIGTH OF DISTILLATION COLUMNS. STAGE NUMBERS AT INFIITE REFLUX (FENSKE) AND AT PINCH CONDITION (UNDERWOOD). GILLILAND CORRELATION. “FUG” INTEGRATED METHOD AND NUMBER OF STAGES ESTIMATION.
3.3 CROSS SECTION DESIGN. FLUID DYNAMIC E DESIGN PARAMETERS FOR A PLATE. OPERATIVE FLEXIBILITY. EFFICIENCY.
4. ADSORPTION / DESORPTION (10 H TH, 2 H EX):
4.1 DESCRIPTION AND TYPICAL APPLICATIONS. THE ISOTHERMS OF EQUILIBRIUM. DESCRIPTIVE AND MECHANISMS EQUATIONS
4.2 DESIGN OF A SORPTION / DESORPTION. THE BALANCE SHEETS OF MATTER. BREAKTHROUGH CURVES. DESORPTION. CYCLES OF ADSORPTION / DESORPTION. PRESSURE SWING ABSORPTION (PSA).
5. CRYSTALLIZATION (12 H TH, 4 H EX):
5.1 DESCRIPTION OF THE CRYSTALLIZATION. CRYSTALLIZATION INDUCED BY PRESSURE, TEMPERATURE. NUCLEATION AND GROWTH. THE CRYSTALLIZATION MODELS. HOMOGENEOUS AND HETEROGENEOUS DESCRIPTIVE MODELS.
5.2 POPULATION BALANCE OF CRYSTALS. SIZING OF A CRYSTALLIZER. CRITICAL EVALUATION OF THE PROJECT LIMITS.

	Teaching Methods
	THE COURSE CONSISTS IN FRONT LESSONS (60 H) AND EXERCISES (30 H) FOR A TOTAL AMOUNT OF 90 HOURS WHICH ARE WORTH 9 CREDITS. ATTENDANCE TO THE LECTURES IS STRONGLY RECOMMENDED

	Verification of learning
	THE EVALUATION OF THE ACHIEVEMENT OF THE EXPECTED OUTCOMES WILL BE VERIFIED THROUGH A WRITTEN AND ORAL EXAM. THE WRITTEN EXAM TYPICALLY LASTS 4 HOURS AND CONSISTS OF TWO EXERCISES, WHILE THE ORAL EXAM HAS A TYPICAL DURATION OF 20 MINUTES. THE ASSESSMENT OF THE LEARNING OUTCOMES, CARRIED OUT IN THE FINAL EXAMINATION, WILL TAKE INTO ACCOUNT THE FOLLOWING EQUIVALENT CRITERIA: A) KNOWLEDGE AND ABILITY TO SOLVE MAJOR ISSUES THAT REQUIRE THE APPLICATION OF EXPRESSED CONCEPTS; B) KNOWLEDGE OF THE BASIC ASSUMPTIONS AND LOGIC OF THE DISCIPLINE; C) ABILITY TO EXTEND THE APPLICATION OF BASIC CONCEPTS TO SOLVE ISSUES IN NEW APPLICATIONS, D) PROPERTY OF LANGUAGE WITH PARTICULAR REFERENCE TO THE SPECIFIC TERMINOLOGY OF THE DISCIPLINE. THE EXAM WILL BE EVALUATED SUFFICIENT WHEN THE STUDENT IS ABLE TO SET THE DESIGN OF THE OPERATIONS UNIT, USING PROPERLY ALTHOUGH NOT READILY PHYSICAL AND CHEMICAL-PHYSICAL VARIABLES INVOLVED, AND IF IT SHOWS SUFFICIENT KNOWLEDGE OF THE VOCABULARY OF THE SUBJECT. THE STUDENT WHO SUCCESSFULLY PROJECTS, WHICH HAS FULL AND READY PERCEPTION OF THE EFFECTS OF THE DESIGN VARIABLES AND SHOWING MASTERY OF THE SUBJECT LEXICON IS RATED AS EXCELLENT

Verification of learning

THE EVALUATION OF THE ACHIEVEMENT OF THE EXPECTED OUTCOMES WILL BE VERIFIED THROUGH A WRITTEN AND ORAL EXAM. THE WRITTEN EXAM TYPICALLY LASTS 4 HOURS AND CONSISTS OF TWO EXERCISES, WHILE THE ORAL EXAM HAS A TYPICAL DURATION OF 20 MINUTES.
THE ASSESSMENT OF THE LEARNING OUTCOMES, CARRIED OUT IN THE FINAL EXAMINATION, WILL TAKE INTO ACCOUNT THE FOLLOWING EQUIVALENT CRITERIA: A) KNOWLEDGE AND ABILITY TO SOLVE MAJOR ISSUES THAT REQUIRE THE APPLICATION OF EXPRESSED CONCEPTS; B) KNOWLEDGE OF THE BASIC ASSUMPTIONS AND LOGIC OF THE DISCIPLINE; C) ABILITY TO EXTEND THE APPLICATION OF BASIC CONCEPTS TO SOLVE ISSUES IN NEW APPLICATIONS, D) PROPERTY OF LANGUAGE WITH PARTICULAR REFERENCE TO THE SPECIFIC TERMINOLOGY OF THE DISCIPLINE.
THE EXAM WILL BE EVALUATED SUFFICIENT WHEN THE STUDENT IS ABLE TO SET THE DESIGN OF THE OPERATIONS UNIT, USING PROPERLY ALTHOUGH NOT READILY PHYSICAL AND CHEMICAL-PHYSICAL VARIABLES INVOLVED, AND IF IT SHOWS SUFFICIENT KNOWLEDGE OF THE VOCABULARY OF THE SUBJECT. THE STUDENT WHO SUCCESSFULLY PROJECTS, WHICH HAS FULL AND READY PERCEPTION OF THE EFFECTS OF THE DESIGN VARIABLES AND SHOWING MASTERY OF THE SUBJECT LEXICON IS RATED AS EXCELLENT

	Texts
	FOR HEAT EXCHANGER NETWORK: INTRODUCTION TO PINCH TECHNOLOGY, LINNHOFF MARCH, WWW.LINNHOFFMARCH.COM IAN C KEMP, PINCH ANALYSIS AND PROCESS INTEGRATION, SECOND EDITION (2007), ELSEVIER PROFESSOR NOTES FOR EXTRACTION: TREYBAL, MASS TRANSFER OPERATION, MC GRAW HILL FOR MULTISTAGE DISTILLATION AND PLATE DESIGN: TREYBAL, MASS TRANSFER OPERATION, MC GRAW HILL J.H. PERRY ET AL., CHEMICAL ENGINEERS’ HANDBOOK , MC GRAW HILL FOR ADSORBTION/DESORPTION: D.M. RUTHVEN ET AL., PRESSURE SWING ADSORPTION; PRINCIPLES OF ABSORPTION AND DESORPTION PROCESSES FOR CRYSTALLIZATION: J.W. MULLIN, CRYSTALLIZATION, FOURTH ED.

Texts

FOR HEAT EXCHANGER NETWORK:
INTRODUCTION TO PINCH TECHNOLOGY, LINNHOFF MARCH, WWW.LINNHOFFMARCH.COM
IAN C KEMP, PINCH ANALYSIS AND PROCESS INTEGRATION, SECOND EDITION (2007), ELSEVIER
PROFESSOR NOTES
FOR EXTRACTION:
TREYBAL, MASS TRANSFER OPERATION, MC GRAW HILL
FOR MULTISTAGE DISTILLATION AND PLATE DESIGN:
TREYBAL, MASS TRANSFER OPERATION, MC GRAW HILL
J.H. PERRY ET AL., CHEMICAL ENGINEERS’ HANDBOOK , MC GRAW HILL
FOR ADSORBTION/DESORPTION:
D.M. RUTHVEN ET AL., PRESSURE SWING ADSORPTION; PRINCIPLES OF ABSORPTION AND DESORPTION PROCESSES

FOR CRYSTALLIZATION:
J.W. MULLIN, CRYSTALLIZATION, FOURTH ED.

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Iolanda DE MARCO | ADVANCES IN UNIT OPERATIONS