Means for controlling the temperature of a depropanizer tower

Mineral oils: apparatus – Vaporizing – Automatic control

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Details

202160, 202206, 203 2, 23515112, 23253A, B01D 342, C10G 702, G05B 2102

Patent

active

039649750

ABSTRACT:
The temperature of light straight run gasoline from a depropanizer tower is controlled as the function of the Reid Vapor Pressure change of a crude oil feeding a flash tower which provides an overhead product to the depropanizer tower and flashed crude oil to an atmospheric tower. The Reid Vapor Pressure is determined from the overhead product, the flashed crude, the pressure of the vapor in the flash tower and the temperature of liquid in the flash tower. A control unit includes a network which determines a change in the Reid Vapor Pressure as the quality of the feed crude oil to the flash tower changes. The network determines the change in the Reid Vapor Pressure and when the change exceeds a limit, provides a feed forward signal corresponding to a desired temperature associated with the new Reid Vapor Pressure. The desired temperature signal is determined in accordance with the equations hereinafter disclosed. The desired temperature signal is supplied to a time select circuit which will not implement the desired temperature signal until after the elapse of a predetermined time interval to account for the delay time for the change of feed crude oil to effect the quality of the feed to the depropanizer tower so that the temperature control may be implemented at the proper time.

REFERENCES:
patent: 2378116 (1945-06-01), Whaley
patent: 2456398 (1948-12-01), Gerhold
patent: 2868701 (1959-01-01), Berger
patent: 2974182 (1961-03-01), Van Pool
patent: 3108929 (1963-10-01), Tolin et al.
patent: 3434934 (1969-03-01), Washer
patent: 3686488 (1972-08-01), Woodle
patent: 3881994 (1975-05-01), Fickel
patent: 3901062 (1975-08-01), Lynch et al.

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