'Tube side pressure drop' presentation slideshows

Tube side pressure drop - PowerPoint PPT Presentation

PROPLEM DIFINITION

PROPLEM DIFINITION

PROPLEM DIFINITION.

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543 views • 45 slides
Equipments Design PO/Styrene Plant

Equipments Design PO/Styrene Plant

Equipments Design PO/Styrene Plant. Done By: Salem Alkanaimsh. Prof. M. Fahim Eng. Yousef Ismael. Agenda. Reactor Design. Heat Exchangers Design. Distillation Columns Design. Pumps Design. Compressors Design. Reactor Design. Chemical reactors are the heart of chemical processes.

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944 views • 34 slides
Equipment Design

Equipment Design

Equipment Design. Done by Ahmad Boland Supervised by: Prof. Mohamed Fahim Eng. Yusuf Ismail. Content:. 2 Heat Exchanger ( 1 & 2 ) Cooler (E-100) Compressor (K-102) Trans-alkylation reaction. Shell and tube heat exchanger.

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474 views • 29 slides
MEE 452: Example 3-2

MEE 452: Example 3-2

Shell-and-Tube Heat Exchanger Analysis: [From B.K. Hodge and R.P. Taylor, Analysis and Design of Energy System, 3rd Ed. , Prentice Hall, 1999]

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322 views • 12 slides
Advantages of coiled flow inverter over shell and tube heat exchanger

Advantages of coiled flow inverter over shell and tube heat exchanger

This study addresses the comparison of CFI over shell and tube heat exchanger. Helical coils have been used in place of baffles as well as of tubes by which, cost is decreased for the same heat exchanger. Normal CFI gives higher heat transfer rates, heat transfer coefficient and less pressure drop up to certain range of Reynolds no. Although everything goes in favor of CFI but simultaneously it has a drawback that at higher Reynolds no. its thermal characteristics get down.

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73 views • 2 slides

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