US3964975A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Means for controlling the temperature of a depropanizer tower
Assignee: Texaco Inc
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Filing: 1974-08-19
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Granted: 1976-06-22
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Expires: 1994-08-19
Abstract
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.
Inventors
- 👤 Charles W. Harrison
- 👤 Glenn A. Senters
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 00:53
CPC Classifications
B; B01; B01D; B01D3/00; B01D3/42; B01D3/4211; B01D3/4227; C; C10; C10G; C10G7/00; C10G7/02; C10G7/12
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
321 words
A refining unit comprising a flash tower receiving raw crude oil, an atmospheric tower receiving a flashed crude oil from said flash tower, a depropanizer tower receiving a light component vapor from said flash tower and producing gasoline, recirculating means including a heater for withdrawing, heating to a desired temperature and recirculating a portion of said gasoline back to said depropanizer tower, said refining unit further including a control system comprising flow rate sensing means for sensing the flow rates of the vapor and the flashed crude oil and providing signals corresponding thereto, pressure sensing means for sensing the pressure in the flash tower and providing a corresponding signal, first temperature sensing means for sensing the temperature of a liquid in the flash tower and providing a signal related thereto, Reid Vapor pressure signal means sampling the flashed crude oil and receiving the flow rate signals, the pressure signal and the temperature signal, for providing a signal corresponding to the current Reid Vapor Pressure of the raw crude oil, second temperature sensing means for sensing the temperature of the gasoline being recirculated back to the depropanizer tower and providing a signal corresponding thereto, desired temperature signal means for providing a signal corresponding to the desired temperature for the gasoline being recirculated back to the depropanizer tower, change signal means connected to the desired temperature signal means and to the Reid Vapor Pressure signal means for providing a change signal to the desired temperature signal means so as to cause the desired temperature signal means to change the amplitude of the desired temperature signal at some predetermined time after a change in the Reid Vapor Pressure has occurred and in accordance with the current Reid Vapor Pressure signal, and control means receiving the desired temperature signal and the sensed gasoline temperature signal for controlling the heater so as to control the temperature of the gasoline being recirculated back to the depropanizer tower.
Claim 2
Dependent Claim
321 words
A refining unit comprising a flash tower receiving raw crude oil, an atmospheric tower receiving a flashed crude oil from said flash tower, a depropanizer tower receiving a light component vapor from said flash tower and producing gasoline, recirculating means including a heater for withdrawing, heating to a desired temperature and recirculating a portion of said gasoline back to said depropanizer tower, said refining unit further including a control system comprising flow rate sensing means for sensing the flow rates of the vapor and the flashed crude oil and providing signals corresponding thereto, pressure sensing means for sensing the pressure in the flash tower and providing a corresponding signal, first temperature sensing means for sensing the temperature of a liquid in the flash tower and providing a signal related thereto, Reid Vapor pressure signal means sampling the flashed crude oil and receiving the flow rate signals, the pressure signal and the temperature signal, for providing a signal corresponding to the current Reid Vapor Pressure of the raw crude oil, second temperature sensing means for sensing the temperature of the gasoline being recirculated back to the depropanizer tower and providing a signal corresponding thereto, desired temperature signal means for providing a signal corresponding to the desired temperature for the gasoline being recirculated back to the depropanizer tower, change signal means connected to the desired temperature signal means and to the Reid Vapor Pressure signal means for providing a change signal to the desired temperature signal means so as to cause the desired temperature signal means to change the amplitude of the desired temperature signal at some predetermined time after a change in the Reid Vapor Pressure has occurred and in accordance with the current Reid Vapor Pressure signal, and control means receiving the desired temperature signal and the sensed gasoline temperature signal for controlling the heater so as to control the temperature of the gasoline being recirculated back to the depropanizer tower.
Claim 3
Dependent Claim
59 words
A refining unit as described in claim 1 in which the desired temperature signal means includes target temperature means for providing a signal corresponding to a target temperature, and combining means connected to the target temperature means and to the change signal means for combining the change signal and the target temperature signal to provide the desired temperature signal.
Claim 4
Dependent Claim
269 words
A refining unit as described in claim 2 in which the change signal means includes first storing means connected to the Reid Vapor Pressure signal means for storing the Reid Vapor Pressure signal in response to a control pulse, difference signal means connected to the first storing means and to the Reid Vapor Pressure signal means for providing a signal corresponding to a difference between the current Reid Vapor Pressure signal and the stored Reid Vapor Pressure signal, comparing means connected to the difference signal means receiving direct current voltages corresponding to predetermined limits for a change in the Reid Vapor Pressure for comparing the difference signal with the reference voltages and providing a signal corresponding to the comparison, pulse means connected to the comparing means for providing sequentially a first and a second control pulse in response to the comparison signal indicating that the difference signal has exceeded a predetermined limit, the second control pulse being provided to the first storing means, second storing means connected to the pulse means and to the difference signal means for storing the difference signal in response to the second control pulse provided by the pulse means, ΔT signal means connected to the two storing means for providing a signal corresponding to a current change ΔT in temperature for the light straight run gasoline in accordance with the signals from the storing means and the following equations: ##EQU2## where ΔRVP c and ΔRVP B are the changes in the Reid Vapor Pressures for the raw crude oil and the gasoline, respectively, and K 1 , K 2 and K 3 are constants.
Claim 5
Dependent Claim
190 words
A refining unit as described in claim 3 in which the change signal means includes ΔT storing means connected to the ΔT signal means for storing the current ΔT signal in response to the second pulse from the pulse means, switching means connected to the combining means, to the ΔT signal means and to the ΔT storing means for passing the current ΔT signal from the ΔT signal means as the change signal while blocking the stored ΔT signal when a control signal is of one amplitude and passing the stored ΔT temperature as the change signal while blocking the current ΔT signal when the control signal is of another amplitude, delay circuit means connected to the pulse means for providing the control signal of the other amplitude in response to the second pulse from the pulse means so as to cause the switching means to pass the stored ΔT signal to the combining means as the change signal providing the control signal of the one amplitude after a predetermined time delay to cause the switching means to pass the current ΔT signal to combining means as the change signal.
Claim 6
Dependent Claim
154 words
A refining unit as described in claim 4 in which the delay circuit means includes a flip-flop providing the control signal of the other amplitude in response to the second pulse from the pulse means and of the one amplitude in response to a reset pulse, means for providing timing pulses, and AND gate receiving the control signal and the timing pulses passes the timing pulses when the control signal is of the other amplitude and blocks the timing pulses when the control signal is of the one amplitude, counting means connected to the AND gate for counting the timing pulses passed by the AND gate, means connected to the counting means for presetting a count corresponding to a desired time delay in the counting means, and means connected to the count down counting means for providing the reset pulse to the flip-flop when the count in the counting means reaches a predetermined count.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-06-22 | 1979-12-22 | 1980-06-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-06-22 | 1983-12-22 | 1984-06-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-06-22 | 1987-12-22 | 1988-06-22 | $7700.00 | Window Closed / Lapsed |