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What value should be chosen for the heat transfer coefficient?

2009-02-24View Original

Thread Content

Piped liquid CO2, pressure 2 MPa, inlet temperature -24°C, outlet temperature 10℃; Shell side water, temperature 20°C. The heat exchange tube material is 304. To ultimately vaporize CO2, what is an appropriate value for the heat transfer coefficient to use in the heat transfer calculations?
Reply #22009-02-24
You can refer to what is available in the Chemical Engineering Design Handbook
Reply #32009-02-24
Calculate with TASC for faster and more accurate results! Hehe
Reply #42009-02-24
Calculations can be performed using the HTRI software
Reply #52009-02-25
Just calculate it by yourself. Checking the manual works too
Reply #62009-02-25
Roughly, it can be estimated, but construction design requires precise calculations.
Reply #72009-02-25
I used HTRI for the calculations. I’m not sure what your CO2 flow rate is; I used 1 kg/s in my calculations, which yields approximately 240 W/m2K. The values provided in the manuals are quite rough, so it’s better to do the calculations yourself :)
Reply #82009-02-25
One cannot simply rely on the heat transfer coefficient, as that is very inaccurate and only provides a rough estimate.
Reply #92009-02-25
For stainless steel, in the case of gas flow and vaporization, such scenarios haven’t been taken into account; refer to the value for Freon, which is around 60~
Reply #102009-02-26
You’re being too vague; you haven’t even chosen a structure yet, so how can there be a heat transfer coefficient! There are also factors such as the flow rate of the medium.

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