how to generate barcode in rdlc report CHEMICAL, ENVIRONMENTAL, PETROLEUM AND GAS ENGINEERING in Software

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CHEMICAL, ENVIRONMENTAL, PETROLEUM AND GAS ENGINEERING
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of 1000 Btu / (h ft2 F / ft) [186 kW / (h large-scale experiments
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C / m)] have been measured in
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MECHANICAL SEPARATIONS AND PHASE COLLECTION
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14 Filtration Filtration is the mechanical phase separation of a uid-solid suspension or slurry by passage of the liquid through a porous septum, or lter medium, which retains the solids The clari ed liquid product is called the ltrate, and the retained solids are called the lter cake
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Types of Filters Gravity lters are the simplest and are always intermittent in operation They are usually in the form of a false-bottomed tank; the false bottom is perforated and supports the lter medium The plate-and-frame lter press is an intermittent-pressure lter The plates are solid with channeled or ribbed faces; the lter medium (eg, lter cloth) is laid over the faces of each plate The frames are hollow and of the same outer dimensions as the plates but are made in a variety of thicknesses Leaf lters are also intermittent-pressure lters The leaf is a hollow frame covered with a wire support screen and the lter medium There are several continuous-vacuum lter designs, but all are similar in basic principle The lter medium is carried on a rotating drum or disk mounted on a hollow horizontal shaft Vacuum is applied to the plenum behind the medium and the cake is formed during that part of the revolution when the medium is immersed in the slurry Rate of Filtration The rate of ltration is the rate at which the ltrate can be forced through the cake and lter medium The ow resistance of the cake is a function of its particle-size distribution, compressibility, thickness, and the viscosity of the ltrate The volumetric ow rate through a hard, granular, noncompressible cake can be related to the operating conditions and cake properties: dV d A Pc gc(W/ A ) (1540) is a
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where is the speci c cake resistance (constant) For compressible cakes, function of pressure drop, often correlated by Ps c
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(1541)
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where and S are empirical constants depending on the particular solids being ltered The compressibility S varies from zero for a hard, granular, noncompressible cake to unity for a soft, readily deformed, compressible cake; for most industrial slurry solids, S ranges from 01 to 08 For compressible cakes, the ltration rate is given by dV d A P (1 s) c gc(W/ A ) (1542)
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The sizing of a lter for a particular slurry starts with laboratory or pilot-plant-
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CHAPTER FIFTEEN
scale tests followed by scale-up to the desired capacity The choice of the type of lter involves a variety of factors and is best made with the advice of lter manufacturers
15 Settling and Sedimentation The separation of suspended solids from a uid by gravitational forces is termed settling or sedimentation; differentiation between the two terms is not precise Settling usually refers to very dilute suspensions of discrete rigid particles or discrete liquid droplets Sedimentation is applied to higher concentrations of solids and to solids that occulate (ie, agglomerate to form rigid lattices) In the free or unhindered settling of discrete particles, the particle will accelerate until drag forces offered by the liquid exactly balance the net gravitational forces (ie, particle weight minus buoyant forces) and thereafter will settle at a constant terminal velocity expressed by vt
4gDp ( p 3 CD
(1543)
where the drag coef cient CD is a function of particle shape and the Reynolds Dpvt / At very low NRe ( 03), number based on particle diameter, NRe Stokes law is valid for spherical or near-spherical rigid particles, and CD 24 / NRe; at higher NRe, the coef cient decreases with increasing NRe, but becomes less dependent on NRe, becoming essentially constant; as the sphericity of a particle decreases, the drag coef cient increases Nonrigid particles exhibit similar behavior, but droplet deformation and internal circulation affect the relationship between CD and NRe
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