The ninth lecture in the module Particle Technology, delivered to second year students who have already studied basic fluid mechanics. The different mechanisms for the removal of dust from gases are covered and the design equations used for control, modelling and understanding of the equipment are presented and derived. Examples of industrial equipment for gas cleaning are included.
1. Gas Cleaning Chapter 13 in Fundamentals Watch this lecture at www.vimeo.com Also visit; http://www.midlandit.co.uk/particletechnology.htm for further resources. Course details: Particle Technology, module code: CGB019 and CGB919, 2nd year of study. Professor Richard Holdich R.G.Holdich@Lboro.ac.uk
7. Dyson vacuum cleaner The animated images shown above are reproduced by permission of Dyson Limited.
8. Inertia - rate of change of momentum How long does it take to reach the terminal settling velocity (gas or liquid)? Inertial collecting devices Stokes’ law and STOKES NUMBER - note the difference!
11. Where m is actual mass of particle - not buoyed mass.
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13. Acceleration & Inertia Particles reach 99% of their terminal settling velocity very quickly. Can use similar approach to characterise the inertia within a system. Inertia can be used in gas cleaning systems.
14. Inertial collection Gas streamlines/flow bend easily round target. Flow Target Dust Inertia carries heavier particles onto target - if they stick this is inertial collection.
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17. It has both particle and collection device properties in its definition.
20. Diffusional collection Small particles move randomly across flow. Flow Target Dust Diffusion means that particles can be captured even behind the target.
21. Material Balance Applicable to any device with a concentration gradient within the collection device. Example quoted is for a fibrous filter of the HEPA (high efficiency particulate air) type - this has a packing density of 2% (ish) fibres, 98% porosity.
22. Accumulation -1 ): Accumulation is (SI units of kg s Collection Interstitial . Projected . Mass . concentration efficiency target area velocity of the dust
23. Projected target area a AdL a AdL 2 p ( / ) d 4 f mass input - mass output = accumulation volume of fibres in height dL is The length of fibres in dL is fibre volume over fibre area, i.e.
24. Projected target area a AdL 4 p d f a AdL 2 p ( / ) d 4 f Projected area to the gas flow is the product of the length and diameter of the fibre d = f
25. Accumulation -1 ): Accumulation is (SI units of kg s Collection Interstitial . Projected . Mass . concentration efficiency target area velocity of the dust U a AdL 4 g r h . . . C s s - a p d 1 f
26. Mass Balance r CU A g s ¶ C é ù + r CU U dL A ê ú g g s ¶ L ë û - r U dC A g s rate of dust input into layer is rate of dust output from layer is hence accumulation is
27. Mass Balance U a AdL 4 g r h . . . C s s - a p d 1 f accumulation U dC A r g s =
28. Mass Balance & Accumulation é ù h a L 4 C s h = - = - - exp 1 1 ê ú p a - C d ( ) 1 ë û o f Hence, dL h a 4 dC s - = - p a C d ( ) 1 f at L=0 to C=C at L=L to give OVERALL C=C o efficiency of m Single target efficiency minimum at approx 0.4 m.
29. In turbulent flow: Critical trajectory within a boundary layer Particle Collection Efficiency
30. Hence, and Thus, equating the times Particle Collection Efficiency
31. Model based on fraction particles removed = fraction volume particles are being removed from: Particle Collection Efficiency Negative sign as removal
32. Particle Collection Efficiency Integrate over full length, and we want fractioncollected – not fraction remaining, hence: Deutch Equation – forelectrostatic precipitators, where Upis function of electric field strength
33. Scrubber and Venturi Scrubber Image located at http://en.wikipedia.org/wiki/File:Adjthroatplunger.jpg
38. Electrostatic Precipitator Image removed for copyright reasons. For a suitable example see http://www.alentecinc.com/company_profile.htm#Electrostatic%20precipitation.
39. Equipment Combined - Flowsheet Image located at http://www.tfhrc.gov/hnr20/recycle/waste/images/cfa.gif
40. Industrial SME NotesThe gas cyclone uses INERTIAL collection of dust whereas the hydrocyclone uses a centrifugal field force - it operates in a much higher viscosity medium. The two have very different operating principles.