Gauri:
You cite the “F Factor” and I presume you mean the LMTD correction factor used in multiple tube pass shell & tube heat exchangers. If so, then I believe you are seriously mixed up in regards to your heat exchanger background and application.
The F Factor is defined as the mean effective temperature difference divided by the LMTD. It cannot have a value of zero. Please refer to the attached information on the Mean Temperature Difference, page 27. It is used in design to avoid a temperature cross in the exchanger.
Additionally, note that there is no mention of the nozzle orientations on a heat exchanger having any effect on the F Factor. In fact, the only way to determine the F Factor is to employ the terminal temperatures as indicated on page 28. Clearly, the terminal temperatures set the F Factor, and not the nozzle orientations.
I have fabricated shell and tube exchangers with the bonnet (or channel) partition baffle oriented in both vertical and horizontal positions – all depending on my piping configuration needs. The operational results gave no problems. I always located my nozzles on the bonnet such that they were perpendicular to the bonnet partition baffle. I don’t recognize any of the problems you describe.
There may be a problem with inert gas accumulation in your channel or bonnet when using horizontal oriented nozzles. For this effect, you need to have vent valves at the top of the channel or bonnet - one on either side of the partition baffle.
The Mean Temperature Difference.pdf 390.66KB
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