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Tray Turn down Ratio

Tray Turn down Ratio

Tray Turn down Ratio

(OP)
We are designing a fractionation column that will be operating under wide feed rate operating range.   Therefore, should we go for high or low tray turn down ratio e.g. 60% or 30%?  For example, a valve tray would have turn down ratio of 5 to 1, which means the tray can handle 1/5 of the feed, while meeting specifications.  Does this mean for a fractionation column that will be operating under wide feed rate operating range, I should use (1/5 x100) 20% tray turn down ratio? Or we should not report the turn down ratio in percentage at all?

Thanks for your calrification

RE: Tray Turn down Ratio

I wouldnt' specify the turndown but rather give the tray vendors the various cases with the corresponding vapor and liquid loadings and ask them for a design.  Let them work out how best to fit your range of operating conditions though you'll still want to review their proposal to satisfy yourself it will operate correctly (or acceptably maybe is a better term) at high and low extremes.

RE: Tray Turn down Ratio

TD2K's method is the intelligent and smart manner of going about the preparation of preparing formal specification's when dealing with such a proprietary and specialty item such as distillation or tower internals.  The vendor is clearly the expert - by common sense and definition of the subsequent business bargain.  It it the vendor who holds the key expertise and design decisions on how to meet specifications and expectations and with how much assurance.

The best we, the purchasers, can do is come up to the vendor's level of general knowledge in the design - but we should never assume the position of "expert" - unless we are willing to take on the related liabilities.   That being the case, do the smart thing just as TD2K does: work with the vendors, giving them ALL your scope of work and letting them tell you what they can/can't build and what their limitations are and why.  You basically want to know if they can meet your specifications; if there are any tradeoffs in meeting those specifications, you certainly want to know about them up front - with no post surprises.

This is the technique I've always used in specifying and purchasing major equipment as a project engineer and project manager.  To do otherwise is not to take advantage of the maximum know-how a vendor can lend to a project in the area of special, proprietary design.  Distillation trays and tower internals is that type of design.

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