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Load:
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1. komponenta
| Lecture type | Total |
| Lectures |
30 |
| Laboratory exercises |
45 |
* Load is given in academic hour (1 academic hour = 45 minutes)
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Description:
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COURSE OBJECTIVE:
Mastering the basic steps of process synthesis and analysis with the aim of optimal utilization of energy and material within the observed process, ensuring environmental and economical feasibility.
COURSE IMPLEMENTATION PROGRAM:
Week 1.
Product types. Hierarchic approach to process syntesis. Batch vs. continuous processes. Process input/output structure. Synthesis of separation sequences.
Week 2.
Monitoring material flows in a process. Significance of mixer and splitter process units. Tracing water flow in the acrylonitrile production process and selecting treatment methods.
Week 3.
Heat exchange network synthesis. Fundamentals of pinch technology, connection with I and II law of thermodynamics. Basics of a heat exchange network synthesis on a simple example (2 hot and 2 cold streams) using the table method.
Week 4.
Graphic procedure for heat exchanger network synthesis. Composite heat curves. Algebraic procedure and thermal cascade diagram for finding pinch points in a process.
Week 5.
Significanxe of dTmin. Network synthesis rules above and below the pinch. Integration of other energy active units and creation of a grand composite curve. Examples of integration of heat in the living environment: air conditioners, GHPs 4 animations, heat pumps.
Week 6.
Integration of heat and power: heat engines, heat pumps. Integration of distillation columns.
Week 7.
First partial test
Week 8.
Mass integration basics. Influence of minimum driving force on the total cost of a mass exchange system. Graphical procedure to determine mass transfer pinch.
Week 9.
Algebraic mass integration procedure-making interval and cascade diagrams. Example: Removal of phenols from wastewater. Numerical procedure - development of algorithms for mass change system (basis).
Week 10.
Reduction of water consumption by developing process structure (networking of PU - process units, TU - treatment units, MU - mixer units and SU - splitter units). Synthesis of a network of water flows and finding the most acceptable performance. Example: Wastewater from oil refining
Week 11.
Example: Rationalization of water consumption in paper production. WSD method and Wang and Smith method
Week 12.
Optimization-forrmulation of an optimization problems (basics). Graphical approach to the problem with an example: Acid gas scrubbing.
Week 13.
Review of procedures and technologies for pollution prevention and waste reduction according to EPA. CLEANER Design available methods and systems.
Week 14.
Sustainable water management in industrial processes (Case study).
Week 15.
Second partial test
DEVELOPMENT OF GENERAL AND SPECIFIC COMPETENCIES OF STUDENTS:
The acquired knowledge will enable the student to choose the best solution when creating a new process design or modifying existing ones. Environmentally and economically acceptable solutions should be assessed by applying skills and techniques for process integration.
STUDENTS OBLIGATIONS:
Mandatory attendance of lectures and exercises in the computer classroom.
CONDITIONS FOR OBTAINING A SIGNATURE:
Attendance at at least 75% of lectures and 75% of exercises.
TEACHING METHODS:
Classroom for lectures and project assignments.
METHOD OF EXAMINATION OF KNOWLEDGE AND EXAMINATION:
Partial test (2 related to lectures and 1 related to the exercises). Alternatively a written and an oral exam
METHOD OF MONITORING THE QUALITY AND PERFORMANCE OF COURSES:
Student survey
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Learning outcomes:
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- Connect the influence of temperature difference as a heat transfer driving force and wnd law of thermodynamics to heat exchanger network design with the goal of optimal thermal energy utilization in a process.
- Evaluate the impact of the heat transfer pinch to heat exchanger network design
- Select apropriate process utilities.
- Determine similarities and differences between heat transfer and mass transfer network design.
- Assess applicability of simplified phase equilibria and mass transfer models in mass exchanger network synthesis.
- Solve problems scientifically, even if the problem definitions are incomplete or are formulated in an unusual way, thereby providing the spectrum of possible solutions
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Literature:
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Chemical Process Design and Integration, R. Smith, Wiley, 2005.
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Pinch Analyisis and Process Integration, I.C. Kemp, Elsevier, 2007.
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Pollution Prevention Through Process Integration, M.M. El-Halwagi, Academic Press, 2003.
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Analysis, Synthesis and Design of Chemical Processes, R. Turton, R. C. Bailie, W. B. Whiting, J. A. Shaeiwitz, Prentice Hall, 2003.
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Prerequisit for:
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Enrollment
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Attended
:
Chemical plant design I
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