انت هنا الان : شبكة جامعة بابل > موقع الكلية > نظام التعليم الالكتروني > مشاهدة المحاضرة

Lec-26 Adsorption.

Share |
الكلية كلية الهندسة     القسم هندسة الكيمياوية     المرحلة 3
أستاذ المادة ساطع كاظم احمد عجام       4/13/2011 7:55:07 AM

ADSORPTION EQUIPMENT

The scale and complexity of an adsorption unit varies from a laboratory chromatographic

column a few millimeters in diameter, as used for analysis, to a fluidised bed several

metres in diameter, used for the recovery of solvent vapours, from a simple container

in which an adsorbent and a liquid to be clarified are mixed, to a highly-automated

moving-bed of solids in plug-flow.

All such units have one feature in common in that in all cases the adsorbent becomes

saturated as the operation proceeds. For continuous operation, the spent adsorbent must

be removed and replaced periodically and, since it is usually an expensive commodity, it

must be regenerated, and restored as far as possible to its original condition.

In most systems, regeneration is carried out by heating the spent adsorbent in a suitable

atmosphere. For some applications, regeneration at a reduced pressure without increasing

the temperature is becoming increasingly common. The precise way in which adsorption

and regeneration are achieved depends on the phases involved and the type of fluid–solid

contacting employed. It is convenient to distinguish three types of contacting:

(a) Those in which the adsorbent and containing vessel are fixed whilst the inlet and

outlet positions for process and regenerating streams are moved when the adsorbent

becomes saturated. The fixed bed adsorber is an example of this arrangement. If

continuous operation is required, the unit must consist of at least two beds, one of

which is on-line whilst the other is being regenerated.

(b) Those in which the containing vessel is fixed, though the adsorbent moves with

respect to it. Fresh adsorbent is fed in and spent adsorbent removed for regeneration

at such a rate as to confine the adsorption within the vessel. This type of arrangement

includes fluidised beds and moving beds with solids in plug flow.

(c) Those in which the adsorbent is fixed relative to the containing vessel which moves

relative to fixed inlet and outlet positions for process and regenerating fluids. The

rotary-bed adsorber is an example of such a unit

---------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------------follows the attached file-----------------------------------------------------------------.


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 .
الرجوع الى لوحة التحكم