0000002483 00000 n 0000026406 00000 n # F! " *Ö¾lónşóM¾hóå1QƒA4—M8l…=Jé´½�‘R‰\P6¢7:ı’¨è%EÂ]Š±� y�áãɶ¦4¹P™ÓwmGd¢“qB%�ğ‚~AcŸÙ³�d (^�j%8 2.2.1. trailer 0000009558 00000 n endobj <>>> �0�K��C�r��~�����u��U*�ÇDx�ח���c� ����S��[9�S`SH�(������9����F����!�r����bo����Eư�tx��2��kH��_5�|���.�7�l:)|,���X� �c�&C�6U ������b��\PA:Oʒs�*rܷA� Assume tube diameter and BWG, Assume tube length, the shell or tube side flow rate. © 2008-2020 ResearchGate GmbH. 0000006023 00000 n refer to cold and hot streams. It uses low-cost materials, is easy to construct, and gives ample scope for individual initiative and the application of engineering analysis to the optimization of the design. ~�ɩ�5NXŦ�cՐ���ֈ����9�r+ޫ���h�t�� �~�-�ȼ Since the exchanger is custom designed, the tube size can be smaller than NPS 1/8 (DN 6 mm) that is the smallest size in Table C.6 in Appendix C, wherein the tube pitch ratio of 1.25 and the diameter ratio of 1.3 can be applied. 5 0 obj Phase Change 7. Heat Exchanger –Example 3 Heat 291,800 lb/hr cold C2+ NGL feed from 80oF using 191,600 lb/hr hot C3+ bottoms @ 240oF. 0000001443 00000 n Design the shell-and-tube heat exchanger. ��:�oѩ��z�����M |/��&_?^�:�� ���g���+_I��� pr;� �3�5����: ���)��� ����{� ��|���tww�X,��� ,�˺�ӂ����z�#}��j�fbˡ:��'�Z ��"��ß*�" ʲ|xx���N3�~���v�"�y�h4Jծ���+䍧�P �wb��z?h����|�������y����畃� U�5i��j�1��� ��E&/��P�? The design of shell and tube heat exchanger using Kern method for water and steam combination is validated by well-known Dittus-Boelter equation of turbulent flow inside tube. endobj Heat Exchanger Design Handbook SECOND EDITION KuppanThulukkanam CRCPress Taylor&Francis Group Boca Raton London NewYork CRCPress is an imprintof the Taylor &FrancisCroup, an informabusiness. Heat exchanger description 2. 0000000016 00000 n In the evaporator the refrigerant evaporates by extracting the rejected heat from refrigerated space and later flows back to the absorber. |%�}���9����xT�ud�����EQ��i�' pH���j��>�����9����Ӳ|�Q+EA�g��V�S�bi�zq��dN��*'^�g�46Yj�㓚��4c�J.HV�5>$!jWQ��l�=�s�=��{���ew.��ϡ?~{�}��������{��e�. endstream Using the information from performance charts and tables, a basic design for the shell and tube heat exchanger can be readily formulated.

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