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Lec-20 Crystallisation.

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الكلية كلية الهندسة     القسم هندسة الكيمياوية     المرحلة 3
أستاذ المادة ساطع كاظم احمد عجام       4/13/2011 7:36:50 AM

Quenching the vapour with cold air in the chamber may increase the rate of heat removal

although excessive nucleation is likely and the product crystalswill be very small. Condenser

walls may be kept free of solid by using internal scrapers, brushes, and other devices, and

all vapour lines in sublimation units should be of large diameter, be adequately insulated,

and if necessary, be provided with supplementary heating to minimise blockage due to

the buildup of sublimate. One of the main hazards of air-entrainment sublimation is the

risk of explosion since many solids that are considered safe in their normal state can form

explosive mixtures with air. All electrical equipment should therefore be flame-proof, and

all parts of the plant should be efficiently earthed to avoid build-up of static electricity.

The method of calculating the density of deposited layers of sublimate and of other

variables and the optimisation of sublimate condenser design, has been discussed by

WINTERMANTEL et al.(113). It is generally assumed that the growth rate of sublimate layers is

governed mainly by heat and mass transfer. The model which is based on conditions in the

diffusion boundary layer takes account of factors such as growth rate, mass transfer, and

concentrations in the gas. The model shows a reasonably good fit to experimental data.

In a variant of the large-chamber de-sublimation condenser, the crystallisation chamber

may be fitted with gas-permeable walls as described by VITOVEC et al.(101). The vapour and

the entrainer gas are cooled by evaporation of water dispersed in the pores of the walls, and

an inert gas passes through the porous walls into the cooling space and protects the internal

walls from solid deposits. Crystallisation takes place in the bulk vapour–gas mixture as

a result of direct contact with the dispersed water. This arrangement has been used, for

example, for the partial separation of a mixture of phthalic anhydride and naphthalene by

using nitrogen as the entrainer. Although fluidised-bed condensers have been considered for

large-scale application, most of the published reports are concerned with laboratory-scale

investigations

FRACTIONAL CRYSTALLISATION

A single crystallisation operation performed on a solution or a melt may fail to produce a

pure crystalline product for a variety of reasons including:

(a) the impurity may have solubility characteristics similar to those of the desired pure

component, and both substances consequently co-crystallise,

(b) the impurity may be present in such large amounts that the crystals inevitably become

contaminated.

(c) a pure substance cannot be produced in a single crystallisation stage if the impurity

and the required substance form a solid solution.


المادة المعروضة اعلاه هي مدخل الى المحاضرة المرفوعة بواسطة استاذ(ة) المادة . وقد تبدو لك غير متكاملة . حيث يضع استاذ المادة في بعض الاحيان فقط الجزء الاول من المحاضرة من اجل الاطلاع على ما ستقوم بتحميله لاحقا . في نظام التعليم الالكتروني نوفر هذه الخدمة لكي نبقيك على اطلاع حول محتوى الملف الذي ستقوم بتحميله .
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