Control system for delayed coker

• US 5,024,730 A
• Filed: 06/07/1990
• Issued: 06/18/1991
• Est. Priority Date: 06/07/1990
• Status: Expired due to Fees

• Current Assignee: Texaco Incorporated (Chevron Corp.)
• Original Assignee: Texaco Incorporated (Chevron Corp.)
• Inventors: Colvert, James H.
• Primary Examiner(s): Woodard, Joye L.
• Application Number:
  US07/534,808
• Time in Patent Office: 376 Days
• Field of Search: 196/132, 208/131, 208/DIG. 1, 202/227, 202/241, 202/253, 202/270, 422/108
• US Class Current: 196/132
• CPC Class Codes: B01D 3/42 Regulation; Control
• CPC Class Codes: C10B 55/00 Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material cracking oils C10G
• CPC Class Codes: Y10S 208/01 Automatic control

Abstract

A system controls a delayed coker in which a heavy liquid hydrocarbon feedstock is thermally decomposed to a solid coke product in a cyclical process. When the coking portion of the cycle is completed, the coke in the drum is cooled by quench water, and the quench water is then passed from the coke drum through a manifold to a drain conduit. Hot vapor is passed through the coke drum, via the same manifold to warm the coke drum. A temperature controller, valve actuator and ball valve allow passage of vapor to the coker fractionator at a manifold temperature at which all water is in the vapor state. Manifold temperatures at which liquid water may exist causes the ball valve to close, preventing liquid water from flowing into the coker fractionator. Upset of the coker fractionator is prevented.

Claims

1. A control system in combination with a delayed coker apparatus in which a heavy liquid hydrocarbon feedstock is converted to solid coke and fluid hydrocarbons in a coke drum and from which coke drum coke and fluid hydrocarbons are removed, said coker apparatus comprising:

the coke drum,

a manifold connected to said coke drum,

a coker fractionator conduit connected to said manifold for providing the flow of fluids from said manifold to a coker fractionator,

said control system comprising, a temperature sensor and transmitter positioned to sense the temperature of fluids in said manifold and to transmit a temperature signal corresponding thereto,

a valve means positioned to regulate fluid flow in said coker fractionator conduit,

a valve actuator being operable to adjust said valve means between fully open and fully closed positions,

comparing means for receiving a set point temperature and said temperature signal, being operable to impress a comparing means signal into said valve actuator for activating said valve means to the fully closed position in response to a temperature less than said set point temperature.

2. The control system of claim 1, including a manually operated on/off switch providing a signal to an AND gate wherein said comparing means impresses said comparing means signal into said AND gate and said AND gate impresses said comparing means signal into said valve actuator

3. A control system in combination with a delayed coker apparatus in which a heavy liquid hydrocarbon feedstock is converted to solid coke and fluid hydrocarbons in a coke drum and from which coke drum coke, fluid hydrocarbons and water are removed, said coker apparatus comprising:

the coke drum,

a manifold connected to said coke drum,

a coker fractionator conduit connected to said manifold for providing the flow of fluids from said manifold to a coker fractionator,

said control system comprising, a temperature sensor and transmitter positioned to sense the temperature of fluids in said manifold and to transmit a temperature signal corresponding thereto,

a valve means positioned to regulate fluid flow in said coker fractionator conduit,

a valve actuator being operable to adjust said valve means between fully open and fully closed positions,

comparing means for receiving a set point temperature and said temperature signal, being operable to impress a comparing means signal into said valve actuator for activating said valve means to the fully closed position in response to a temperature less than said set point temperature,

said set point temperature selected at a temperature above the temperature at which water can exist in the liquid state in the manifold, the control system thereby preventing the flow of liquid water into the coker fractionator by way of the coker fractionator conduit.