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including the stream quality desired predict

Including the stream quality desired predict

in the overhead product and maintain slightly less than 2% Ethane in the column bottoms.

On the other hand, if ethane, with 1.5% propane sells for $16/barrel and propane is used as fuel gas, the operating objectives of the de-ethanizer will be different from the above case: to minimize ethane in the column bottoms and keep the propane in the overhead as near 1.5% as possible, without exceeding the sales limit. To achieve either set of the above objectives, a continuous measurement of propane in the column overhead and ethane in the bottoms is necessary.

Process Variable

Tag Range

Tray 27 temperature

TI-6 100-300 °F
Overhead Temperature TI-5 100-300 °F
TI-7 100-300 °F
TI-4 0-200 °F
FI-2 0-20MBD
FI-3 0-10MBD

Feed Rate

FI-6 0-80MBD

Reboiler Steam

FI-4 0-30MPPH
FI-5 0-80MBD
Tag Range

Tray 1 temperature

TI-1 100-400 °F

Bottoms Temperature

TI-3 100-400 °F
TI-8 100-300 °F
TI-4 0-200 °F
Re-boiler Return Temperature TI-2 100-400 °F
FI-3 0-10MBD
FI-6 0-80MBD

Re-boiler Steam

FI-4 0-30MPPH

Bottoms Product

FI-5 0-80MBD

For the naphtha 95% cut point and naphtha Reid vapor pressure stream properties, the plant data, including the stream quality desired to predict, are collected in a Microsoft Excel™ spreadsheet to facilitate data manipulation. The data are then scaled to a fraction of the transmitter range so that they are confined to a sub-interval of [0…1]. A practical region for the data is chosen to be [0.1…0.9]. In this case each input or output parameter p is normalized as pn before being applied to the neural network according to:

pn = [( 0.9 - 0.1 ) / ( pmax - pmin )] * (p - pmin ) + 0.1

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Uploaded by : Kathleen Allen MD

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