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A Falling Film Evaporator (FFE) is a vertical shell and tube heat exchanger with a vapor- liquid separator mounted at the bottom. The liquid flows as a thin film on the inside of heated vertical tubes, driv-en by gravity. 0000001066 00000 n 0000001250 00000 n 1) Falling film evaporator: In this paper falling film evaporator is taken and it consists of head, calandria, calandria lower part and separator as shown in the fig.1. The resulting vapor normally flows cocurrently with the liquid, in the centre of the tubes. 0000017141 00000 n

The liquid to be concentrated is fed at the top of the heated tubes and distributed in such a way that it flows down on the inside surface of the tubes as a thin film. 0000001834 00000 n coefficients in falling film evaporator usable for evaporator design. 0000006913 00000 n

A falling film evaporator is an industrial device to concentrate solutions, especially with heat sensitive components. 0000007483 00000 n

x�bbR``b``Ń3� ����C7> gI� endstream endobj 381 0 obj <>/ViewerPreferences<>/Metadata 37 0 R/Pages 36 0 R/StructTreeRoot 39 0 R/Type/Catalog>> endobj 382 0 obj <>/ProcSet[/PDF/Text]/Properties<>>>/ExtGState<>>>/Type/Page>> endobj 383 0 obj <> endobj 384 0 obj <> endobj 385 0 obj <> endobj 386 0 obj <>stream Falling Film Evaporator Design Our falling film evaporator is the simplest and most commonly used type of film evaporator. 0000003680 00000 n 4) Plate evaporator. 0000015283 00000 n

In this paper, the mathematical model and the physical model were established.

0000001397 00000 n The falling film evaporators have many advantages over flooded and vertical tubes that make them best candidate for processes industries application.

Falling film evaporators utilized in sub-atmospheric, high vapor quality MED (multi effect desalination) units are analyzed. A full evaporation stage consists of the �C�?r7�� >�u� �D�jI��߾�� �ɝ�%��v�ۏ�j����jN��/�:ݖΛ�?c����1��ݥ��4���_��iJ�ڤ?��u]��i�OG���ߗ�/�x6O���g�n���_����4���)}m�o�ś4����0?������}����f���׹��Ҏg��YxS���I���7/Î��O�$u�%,�2��n�0~�Wa\dq>�_ɯ���lɈ/v�����%uJ�99�\�K�%[�#;��� l�c�c�c�c�c�ckk�,`�bQ�e-�X�bQ�e-�8�w���!�c.�\����j The high performance evaporators are important for process industries such as food, desalination and refineries.

0000002762 00000 n Introduction. 1. 0000004466 00000 n In this case, however, evaporator liquid is pumped to the top of the heat exchanger and flows in a downward direction through the tubes.

The thermal performance curves of the MED units are extracted and analyzed. Copyright © 2015 Elsevier Ltd. All rights reserved. and Processing. A Falling Film Evaporator (FFE) is a combination of vertical shell and tube heat exchanger and vapor- liquid separator mounted at bottom. The feed is given at top of shell & tube type heat exchanger having distributor. The essential feature of the falling film evaporator is calandria which comprises a bundle of tubes. 0000009559 00000 n 2009; 48 (5):961-968 [4] Chun KR, Seban RA. The heat transfer area is the key parameter in designing of an evaporator and many correlations are available to estimate the size … %PDF-1.4 %���� 0000002238 00000 n 4��M��@S�)�y���5Y��.a]���&�7y#��Yo�B��}P�ҿ¿ҿ¿ҿ¿ҿ¿ҿ¿ҿ¿ҿ¿ҿ¿ҿ¿ҿ��\E����$�eɻx�7-:�|�Ww[��Z��cO����t�.

endstream endobj 403 0 obj <>/Size 380/Type/XRef>>stream Existing heat transfer correlations poorly predict the thermal performance of falling film evaporators utilized in MED (multi effect desalination) units. H�\��n�0��z 380 0 obj <> endobj xref 380 25 0000000016 00000 n Boiling of water in the evaporator … Therefore, research on the bilateral heat transfer of falling film evaporation needs to be solved, which will provide theoretical guidance for the design of falling film evaporator. The present study aims to elucidate the thermal transport processes of the falling film evaporators utilized in these MED units. 0000005701 00000 n The interconnected effects of the wall superheat and the inlet mass flow rate are elucidated. The liquid falling on distributor get distributed in such a way that it flow down as a thin film on inside surface of the tube. 0000006330 00000 n Evaporation of falling two-phase flows over a tube bundle, falling film evaporation, is an important problem taking place in many industrial devices such as evaporators, condensers and sea water desalination units , .Falling film evaporation is also a common phenomenon in the petrochemical industries as well as large heat pump systems . By continuing you agree to the use of cookies. In addition, strong interconnected effects of the wall superheat and the mass flow rate on the thermal performance are often unavoidable in the MED units. At typical operating conditions of these units, most correlations suggest that the two-phase heat transfer coefficient increases with the mass flow rate and is independent of the wall superheat. Heat transfer to evaporating liquid films. ScienceDirect ® is a registered trademark of Elsevier B.V. ScienceDirect ® is a registered trademark of Elsevier B.V. A general guide to design of falling film evaporators utilized in multi effect desalination units operating at high vapor qualities under a sub-atmospheric condition. https://doi.org/10.1016/j.energy.2015.02.099.

Falling Film Evaporator Like the rising film evaporator, the heat exchanger in a falling film evaporator is vertically mounted. x�b```e``I�MaB ��ea�h`Y��7m��j�ݻ��F"��^��8h)@ .� &��d��2l�5@Z�%�"��L{X���r�]�����`�1E�A�C����8D6h��8���p���9���P 4XD�j5�ۑ@��7 �)! Copyright © 2020 Elsevier B.V. or its licensors or contributors.

0000003593 00000 n Although these correlations are valid within their particular range of parameters, they are not suitable prediction tools for MED units as they operate at high vapor qualities under a sub-atmospheric condition. Chemical Engineering. Result also indicate the wall superheat for this transition increases at higher values of ΔT/m˙f. 0000008955 00000 n 0000000796 00000 n trailer <]>> startxref 0 %%EOF 404 0 obj <>stream Results show, at a constant value of ΔT/m˙f which is a design characteristic of these units, the average heat transfer coefficient first decreases and then increases as the inlet mass flow rate increases. The detailed thermo-hydrodynamic physics of the involved transport processes is elucidated using the VOF (volume of fluid) multiphase model in the curvilinear coordinate. The evaporator is a special type of heat exchanger General. 0000004354 00000 n 0000003940 00000 n 0000005102 00000 n 0000007597 00000 n 0000003013 00000 n We use cookies to help provide and enhance our service and tailor content and ads.

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