TRANSFER PROCESSES - 2017/8
Module code: ENG2109
Chemical and Process Engineering
HARE C Dr (Chm Proc Eng)
Number of Credits
FHEQ Level 5
Module cap (Maximum number of students)
Overall student workload
Lecture Hours: 34
Tutorial Hours: 11
|Assessment type||Unit of assessment||Weighting|
|Examination||EXAMINATION (2 HOURS)||80|
Prerequisites / Co-requisites
Completion of the progression requirements to FHEQ Level 5 of the degree courses in Chemical Engineering, Chemical and Bio-Systems Engineering and Chemical and Petroleum Engineering, or equivalent.
Mass Transfer: Mass transfer is essential knowledge for chemical engineers, governing the underlying operations in many industrial processes involving, for example, separation and reaction. The purpose of the module is to introduce students to mechanistic and semi-empirical descriptions of mass transfer, and to apply such understanding to the design of process such as gas absorption and drying.
Fluid mechanics: The main part of the syllabus concentrates on developing the student’s understanding of internal flows. Knowledge of turbulent flow is extended by the introduction of the Universal Velocity Profile. Furthermore, more complex flows, which may include multiple phases or compressibility, are introduced. The issues of drag and terminal velocity of particles is tackled and the features and flow of some non-Newtonian fluids discussed.
A short introduction is given on the simulation of real-life Mass-Transfer and Fluid Mechanics problems using commercial software.
Introduce the key concepts of mass transfer operations in Chemical Engineering, with a specific focus on gas-liquid and gas-solid systems.
Provide the knowledge and skills to undertake the specification and design of absorption columns (i.e. continuous diffusional contact devices).
Provide an introduction to the selection and design of solids drying equipment.
Provide students further and deeper understanding of fluid flows in Chemical Engineering.
|Describe the key principles of, and modelling approaches to, mass transfer in fluid-fluid and fluid-solid system.||KC|
|Design absorption and stripping equipment based on continuous diffusional contact.||KCP|
|Develop general mathematical models for mass transfer in different phase-contact and phase-flow situations.||KC|
|Describe the drying mechanisms of particulate solids and the classification of drying operations.||KC|
|Analyse batch and continuous drying operations.||KCP|
|Explain the physics behind turbulent flow in a pipe and how that affects the velocity profile, the fluid friction at a pipe wall||KC|
|Distinguish between regimes in industrially important flows (such as two-phase and compressible flow) and calculate the size and driving force for such flows||KCP|
|Relate the forces occurring at a molecular level in colloidal suspensions to non-Newtonian flow behaviour||KC|
C - Cognitive/analytical
K - Subject knowledge
T - Transferable skills
P - Professional/Practical skills
Indicative content includes:
Introduction to mass transfer
Molecular diffusion: Fick's law
General case of diffusion with bulk (convective) flow
Diffusivity determination and prediction
Mass transfer coefficients; mass transfer correlations
Momentum, heat and mass transfer analogies; J-factor analogy
Mass transfer across interfaces
Whitman two-film theory
Gas-liquid equilibria; Henry's law
Overall driving force and overall mass transfer coefficients
Film control and design implications
Absorber and stripper design
Industrial processes: staged vs. continuous contact equipment
Hydrodynamic considerations: loading, flooding, pressure drop
Absorber / stripper design equations: height and number of gas-transfer units; graphical and analytical solutions
Other contact configurations: well-mixed flow; co-current flow; extension of concepts to liquid-liquid systems
Diffusion in solids
Pore diffusion: molecular, Knudsen, configurational
Diffusion through non-porous solids; membranes
Drying of particulate solids
Mechanisms of drying
Drying rate curves
Kinetics of drying
Characterisation of wet gas streams: humidity definitions; humid heat; enthalpy; humid volume; adiabatic saturation and wet-bulb temperatures; psychrometric ratio; psychrometric charts
Turbulent flow in a pipe
Revision of 1/7th power law
The universal velocity profile.
Eddy viscosity and its link to eddy diffusivity
Mixing of fluids
Two phase gas-liquid flow in pipes
Flow pattern maps in horizontal and vertical flow
Pressure differences (incl. Method of Lockhart and Martinelli)
Equipment for pumping gases
Types and their characteristics
Reminder of inter-cooling
Surge and recycle
Compressible flow of gases
Reminder of basic equations (Continuity, Ideal Gas law, adiabatic equations, steady flow energy equation)
Isothermal compressible flow in pipelines (density changes, speed of sound, choking)
Isentropic compressible flow through valves (density changes, speed of sound, choking, existence of shock waves). How to predict whether a valve is choked. Calculation of relief valve capacity
When is a flow likely to be isothermal or isentropic? Mention of polytropic flows.
Brief discussion of convergent-divergent nozzles.
Drag coefficients for a sphere
Force balance for a sphere in free fall
Equations for terminal velocity
Non-Newtonian Fluids including Colloids
Types of non-Newtonian behaviour
Van der Waals’ forces and colloidal rheology
Internal flow of non-Newtonian fluids
Methods of Teaching / Learning
The learning and teaching strategy is designed to:
Carefully cover in lectures the necessary fundamental material and analytical techniques, and demonstrate concepts with appropriate (and where possible practical) examples
Allow students adequate time to practice the techniques using a large number of carefully selected tutorial problems.
The learning and teaching methods include:
Lectures 3 hours per week for 11 weeks
Tutorial/Problem Classes 1 hour per week for 11 weeks
Independent learning 8 hours per week for 12 weeks (average)
The assessment strategy is designed to provide students with the opportunity to demonstrate the full range of learning outcomes though the balanced mixture of lecture and tutorial/problem classes coupled with the carefully graded tutorial problems which reflect current industrial practice.
Thus, the summative assessment for this module consists of:
Examination – 80% (weighted 48% to Mass Transfer and 32% to Fluid Mechanics), 2 hours (LO1 – LO9)
Coursework – 20% (Mass Transfer). Absorption column design calculations (LO2).
Mass transfer class test (LO1, LO2, LO4, LO5)
Randomised multiple choice tests on SurreyLearn (LO6, LO7, LO8)
Weekly verbal feedback during tutorial classes (LO1 – LO9)
Written feedback on Coursework (LO2)
Verbal feedback at the end of the formative class tests (LO1, LO2, LO4, LO5)
Reading list for TRANSFER PROCESSES : http://aspire.surrey.ac.uk/modules/eng2109
Programmes this module appears in
|Chemical and Petroleum Engineering BEng (Hons)||2||Compulsory||A weighted aggregate mark of 40% is required to pass the module|
|Chemical and Petroleum Engineering MEng||2||Compulsory||A weighted aggregate mark of 40% is required to pass the module|
|Chemical Engineering BEng (Hons)||2||Compulsory||A weighted aggregate mark of 40% is required to pass the module|
|Chemical Engineering MEng||2||Compulsory||A weighted aggregate mark of 40% is required to pass the module|
Please note that the information detailed within this record is accurate at the time of publishing and may be subject to change. This record contains information for the most up to date version of the programme / module for the 2017/8 academic year.