Fractionating column control apparatus and methods

Claim 1

Apparatus for separating a mixture of hydrocarbons into discrete products, comprising: a fractionating column; means for providing heat to said fractionating column; means for feeding a stream of said mixture of hydrocarbons to said fractionating column whereby said stream is fractionated into an overhead product stream and a bottoms product stream; and means for controlling the Reid vapor pressure of said bottoms product stream, including: means for establishing a first signal representative of the actual temperature of said bottoms product stream; means for establishing a second signal representative of the actual vapor pressure of said bottoms product stream; means for establishing a third signal representative of the actual rate of flow of said bottoms product stream; means for establishing a fourth signal representative of the actual rate of flow of said overhead product stream; means for establishing a fifth signal representative of the actual Reid Vapor Pressure of said bottoms product stream in response to said first, second, third and fourth signals without an analysis of said bottoms product stream; means for establishing a sixth signal representative of the desired Reid Vapor Pressure of said bottoms product stream; means for comparing said fifth signal and said sixth signal and for establishing a seventh signal responsive to the difference between said fifth signal and said sixth signal; and means responsive to said seventh signal for varying the rate at which heat is provided to said fractionating column to maintain said actual Reid Vapor Pressure of said bottoms product stream.

Claim 4

A method for determining the Reid Vapor Pressure of a bottoms product stream of a fractionating column used for fractionating a multi-component hydrocarbon feed stream into an overhead product stream and a bottoms product stream, comprising: establishing a first signal representative of the temperature of said bottoms product stream; establishing a second signal representative of the vapor pressure of said bottoms product stream; establishing a third signal representative of the rate of flow of said bottoms product stream; establishing a fourth signal representative of the rate of flow of said overhead product stream; determining said Reid Vapor Pressure of said bottoms product stream in response to said first, second, third and fourth signals without an analysis of said bottoms product stream; wherein said step of determining said Reid Vapor Pressure of said bottoms product stream in response to said first, second, third and fourth signals without an analysis of said bottoms product stream comprises the step of determining said Reid Vapor Pressure of said bottoms product stream in response to said first, second, third and fourth signals without an analysis of said bottom product stream based on the following relationship; Reid Vapor Pressure=A+B (X.sup.E -C(Y)+D/Z wherein: X equals the temperature of said bottoms product stream as represented by said first signal; Y equals the vapor pressure of said bottoms product stream as represented by said second signal; Z equals the rate of flow of said overhead product stream as represented by said fourth signal divided by the rate of flow of said bottoms product stream as represented by said third signal; and A, B, C, D, and E equal fitted constants.

Claim 5

A method for determining the Reid Vapor Pressure of a bottoms product stream of a fractionating column used for fractionating a multi-component hydrocarbon feed stream into an overhead product stream and a bottoms product stream, comprising: establishing a first signal representative of the temperature of said bottoms product stream; establishing a second signal representative of the vapor pressure of said bottoms product stream; establishing a third signal representative of the rate of flow of said bottoms product stream; establishing a fourth signal representative of the rate of flow of said overhead product stream; determining said Reid Vapor Pressure of said bottoms product stream in response to said first, second, third and fourth signals without an analysis of said bottoms product stream; wherein said step of determining said Reid Vapor Pressure of said bottoms product stream in response to said first, second, third and fourth signals without an analysis of said bottoms product stream comprises the step of determining said Reid Vapor Pressure of said bottoms product stream in response to said first, second, third and fourth signals without an analysis of said bottom product stream based on the following relationship; Reid Vapor Pressure=A+B (X.sup.E -C(Y)+D/Z wherein: X equals the temperature of said bottoms product stream as represented by said first signal; Y equals the vapor pressure of said bottoms product stream as represented by said second signal; Z equals the rate of flow of said overhead product stream as represented by said fourth signal divided by the rate of flow of said bottoms product stream as represented by said third signal; and A, B, C, D, and E equal fitted constants.

Claim 6

A method of controlling the Reid Vapor Pressure of a bottoms product stream of a fractionating column used for fractionating a multi-component hydrocarbon feed stream into an overhead product stream and a bottoms product stream wherein heat is provided to said column, said method comprising: establishing a second signal representative of the vapor pressure of said bottoms product stream; establishing a third signal representative of the rate of flow of said bottoms product stream; establishing a fourth signal representative of the rate of flow of said overhead product stream; establishing a fifth signal representative of the actual Reid vapor Pressure of said bottoms product stream in response to said first, second, third and fourth signals without an analysis of said bottoms product stream; establishing a sixth signal representative of the desired Reid vapor Pressure of said bottoms product stream; comparing said fifth signal and said sixth signal and establishing a seventh signal responsive to the difference between said fifth signal and said sixth signal; varying the rate at which heat is provided to said fractionating column in response to said seventh signal to maintain the actual Reid Vapor Pressure of said bottoms product stream substantially equal to the desired Reid Vapor Pressure of said bottoms product stream: wherein said fifth signal representative of the actual Reid Vapor Pressure of said bottoms product stream is established in response to said first, second, third, and fourth signals without an analysis of said bottoms product stream based on the following relationship: Reid Vapor Pressure=A+B (X.sup.E -C(Y))+D/Z wherein: X equals the temperature of said bottoms product stream as represented by said first signal; Y equals the vapor pressure of said bottoms product stream as represented by said second signal; Z equals the rate of flow of said overhead product stream as represented by said fourth signal divided by said rate of flow of said bottoms product stream as represented by said third signal; and A, B, C, D, and E equal fitted constants.

Claim 7

A method of controlling the Reid Vapor Pressure of a bottoms product stream of a fractionating column used for fractionating a multi-component hydrocarbon feed stream into an overhead product stream and a bottoms product stream wherein heat is provided to said column, said method comprising: establishing a second signal representative of the vapor pressure of said bottoms product stream; establishing a third signal representative of the rate of flow of said bottoms product stream; establishing a fourth signal representative of the rate of flow of said overhead product stream; establishing a fifth signal representative of the actual Reid vapor Pressure of said bottoms product stream in response to said first, second, third and fourth signals without an analysis of said bottoms product stream; establishing a sixth signal representative of the desired Reid vapor Pressure of said bottoms product stream; comparing said fifth signal and said sixth signal and establishing a seventh signal responsive to the difference between said fifth signal and said sixth signal; varying the rate at which heat is provided to said fractionating column in response to said seventh signal to maintain the actual Reid Vapor Pressure of said bottoms product stream substantially equal to the desired Reid Vapor Pressure of said bottoms product stream: wherein said fifth signal representative of the actual Reid Vapor Pressure of said bottoms product stream is established in response to said first, second, third, and fourth signals without an analysis of said bottoms product stream based on the following relationship: Reid Vapor Pressure=A+B (X.sup.E -C(Y))+D/Z wherein: X equals the temperature of said bottoms product stream as represented by said first signal; Y equals the vapor pressure of said bottoms product stream as represented by said second signal; Z equals the rate of flow of said overhead product stream as represented by said fourth signal divided by said rate of flow of said bottoms product stream as represented by said third signal; and A, B, C, D, and E equal fitted constants.