Control of a fractional distillation process

Claim 2

Apparatus comprising: a fractional distillation column; means for passing a feed mixture containing at least first and second components into said fractional distillation column; means for passing a heating fluid to said fractional distillation column; means for withdrawing an overhead vapor stream, having a substantially increased concentration of said first component with respect to the concentration of said first component in said feed mixture, from an upper portion of said fractional distillation column; means for condensing at least a portion of said overhead vapor stream; an accumulator; means for passing the resulting at least partially condensed overhead stream into said accumulator; means for withdrawing condensate from said accumulator and for passing a first portion of the thus withdrawn condensate into an upper portion of said fractional distillation column as an external reflux stream therefor and for passing a second portion of the thus withdrawn condensate as an overhead product stream; means for withdrawing a bottoms product stream, having a substantially increased concentration of said second component with respect to the concentration of said second component in said feed mixture, from a lower portion of said fractional distillation column; means for establishing a first signal which is representative of the concentration of said first component in said bottoms product stream; means for establishing a second signal representative of the concentration of said second component in said overhead product stream; means for establishing a first control signal representative of the desired flow rate of said external reflux stream in response to said first signal and said second signal, wherein said first control signal is periodically increased or decreased by a fixed increment or left unchanged depending upon the relationship between the actual concentration of said first component in said buttoms product stream as represented by said first signal and a high limit and low limit for the actual concentration of said first component in said bottoms product stream, depending upon the relationship between the actual concentration of said second component in said overhead product stream as represented by said second signal and high and low limits for the actual concentration of said second component in said overhead product stream and depending on the relationship between the magnitude of said first control signal and a high limit for the flow rate of said external reflux stream; means for manipulating the flow rate of said external reflux in response to said first control signal so as to maintain the actual external reflux flow rate substantially equal to the desired external reflux flow rate as represented by said first control signal; means for establishing a second control signal representative of the desired temperature at a selected point in said fractional distillation column in response to said first signal and said second signal, wherein said second control signal is periodically increased or decreased by a fixed increment or is left unchanged depending upon the relationship between the actual concentration of said first component in said bottoms product stream as represented by said first signal and said high and low limits for the actual concentration of said first component in said bottoms product stream, depending upon the relationship between the actual concentration of said second component in said overhead product stream as represented by said second signal and said high and low limits for the actual concentration of said second component in said overhead product stream and depending on the relationship between the magnitude of said first control signal and a high limit for the flow rate of said external reflux stream; and means for manipulating the flow rate of heat to said fractional distillation column in response to said second control signal so as to maintain the actual temperature at said selected point substantially equal to the desired temperature represented by said second control signal.

Claim 3

Apparatus in accordance with claim 1 wherein the manner in which said first control signal and said second control signal are changed based on the relationship of said first signal (ACB) to the high (HL1) and low (LL1) limits for the actual concentration of said first component in said bottoms product stream, the relationship of said second signal (ACO) to the high (HL2) and low (LL2) limits for the actual concentration of said second component in said overhead product stream and the relationship of said first control signal to said high limit for the flow rate of said external reflux stream is as set forth in Table I if the magnitude of said first control signal is less than said high limit for the flow rate of said external reflux stream TABLE 1 ______________________________________ Relationships Control Signals First Signal Second Signal Second First ______________________________________ ACB < LL1 ACO < LL2 no change decrease ACB < LL1 LL2 ≦ ACO ≦ decrease decrease HL2 ACB < LL1 ACO > HL2 decrease no change LL1 ≦ ACB ≦ HL1 ACO < LL2 increase decrease LL1 ≦ ACB ≦ HL1 LL2 ≦ ACO ≦ no change no change HL2 LLl ≦ ACB ≦ HL1 ACO > HL2 decrease increase ACB > HL1 ACO < LL2 increase no change ACB > HL1 LL2 ≦ ACO ≦ increase increase HL2 ACB > HL1 ACO > HL2 no change increase ______________________________________ and is as set forth in Table 2 if the magnitude of said first control signal is greater than or equal to said high limit for the flow rate of said external reflux stream: TABLE 2 ______________________________________ Relationships Control Signals First Signal Second Signal Second First ______________________________________ ACB < LL1 ACO < LL2 increase no change ACB < LL1 LL2 ≦ ACO ≦ no change no change HL2 ACB < LLI ACO > HL2 decrease no change LL1 ≦ ACB ≦ HL1 ACO < LL2 increase no change LL1 ≦ ACB ≦ HL1 LL2 ≦ ACO ≦ no change no change HL2 LL1 ≦ ACB ≦ HL1 ACO > HL2 decrease no change ACB > HL1 ACO < LL2 increase no change ACB > HL1 LL2 ≦ ACO ≦ no change no change HL2 ACB > HL1 ACO > HL2 decrease no change ______________________________________

Claim 4

Apparatus in accordance with claim 1 wherein said means for manipulating the flow rate of said external reflux in response to said first control signal comprises: means for establishing a third signal representative of the actual flow rate of said external reflux; means for comparing said third signal and said first control signal and for establishing a fourth signal which is responsive to the difference between said third signal and said first control signal, wherein said fourth signal is scaled so as to be representative of the position of a first control valve, operably located so as to control the flow rate of said external reflux, required to maintain the actual flow rate of said external reflux substantially equal to the desired flow rate represented by said first control signal; and means for manipulating said first control valve in response to said fourth signal.

Claim 5

Apparatus in accordance with claim 1 wherein said selected point in said fractional distillation column is a selected tray in said fractional distillation column and wherein said means for manipulating the flow rate of heat to said fractional distillation column in response to said second control signal comprises: means for establishing a third signal representative of the actual temperature of said selected tray; means for comparing said third signal and said second control signal and for establishing a fourth signal which is responsive to the difference between said third signal and said second control signal, wherein said fourth signal is scaled so as to be representative of the flow rate of heating fluid to said fractional distillation column required to maintain the actual temperature of said selected tray substantially equal to the desired temperature represented by said second control signal; means for establishing a fifth signal representative of the actual flow rate of said heating fluid; means for comparing said fourth signal and said fifth signal and for establishing a sixth signal which is responsive to the difference between said fourth signal and said fifth signal, wherein said sixth signal is scaled so as to be representative of the position of a second control valve, operably located so as to control the flow rate of said heating fluid to said fractional distillation column, required to maintain the actual flow rate of said heating fluid substantially equal to the desired flow rate represented by said fourth signal; and means for manipulating said second control valve in response to said sixth signal to thereby maintain the actual flow rate of said heating fluid to said fractional distillation column substantially equal to the desired flow rate represented by said fourth signal.

Claim 6

Apparatus in accordance with claim 1 additionally comprising: means for establishing a third signal representative of the actual flow rate of said feed mixture to said fractional distillation column; a lag means; means for passing said third signal through said lag means to establish a fourth signal; a delay means; means for passing said fourth signal through said delay means to establish a fifth signal; means for subtracting said fifth signal from said fourth signal to establish a sixth signal; means for establishing a seventh signal representative of a bias term; means for multiplying said sixth signal and said seventh signal to establish an eighth signal; and means for adding said eighth signal to said first control signal to thereby apply a feedforward compensation for changes in the flow rate of said feed mixture to said fractional distillation column to the desired flow rate of said external reflux.

Claim 7

Apparatus in accordance with claim 1 wherein the high limit for the concentration of said first component in said bottoms product stream is the desired concentration of said first component in said bottoms product stream, wherein the low limit for the concentration of said first component in said bottoms product stream is a percentage of the high limit for the concentration of said first component in said bottoms product stream, wherein the high limit for the concentration of said second component in said overhead product stream is the desired concentration of said second component in said overhead product stream and wherein the low limit for the concentration of said second component in said overhead product stream is a percentage of the high limit for the concentration of said second component in said overhead product stream.

Claim 10

A method in accordance with claim 7 wherein the manner in which said first control signal and said second control signal are changed based on the relationship of said first signal (ACB) to the high (HL1) and low (LL1) limits for the actual concentration of said first component in said bottoms product stream and the relationship of said second signal (ACO) to the high (HL2) and low (LL2) limits for the actual concentration of said second component in said overhead product stream and the relationship of said first control signal to said high limit for the flow rate of said external reflux stream is as set forth in Table 1 if the magnitude of said first control signal is less than said high limit for the flow rate of said external reflux stream: TABLE 1 ______________________________________ Relationships Control Signals First Signal Second Signal Second First ______________________________________ ACB < LL1 ACO < LL2 no change decrease ACB < LL1 LL2 ≦ ACO ≦ decrease decrease HL2 ACB < LL1 ACO > HL2 decrease no change LL1 ≦ ACB ≦ HL1 ACO < LL2 increase decrease LL1 ≦ ACB ≦ HL1 LL2 ≦ ACO ≦ no change no change HL2 LLl ≦ ACB ≦ HL1 ACO > HL2 decrease increase ACB > HL1 ACO < LL2 increase no change ACB > HL1 LL2 ≦ ACO ≦ increase increase HL2 ACB > HL1 ACO > HL2 no change increase ______________________________________ and is as set forth in Table 2 if the magnitude of said first control signal is greater than or equal to said high limit for the flow rate of said external reflux stream: TABLE 2 ______________________________________ Relationships Control Signals First Signal Second Signal Second First ______________________________________ ACB < LL1 ACO < LL2 increase no change ACB < LL1 LL2 ≦ ACO ≦ no change no change HL2 ACB < LLI ACO > HL2 decrease no change LL1 ≦ ACB ≦ HL1 ACO < LL2 increase no change LL1 ≦ ACB ≦ HL1 LL2 ≦ ACO ≦ no change no change HL2 LL1 ≦ ACB ≦ HL1 ACO > HL2 decrease no change ACB > HL1 ACO < LL2 increase no change ACB > HL1 LL2 ≦ ACO ≦ no change no change HL2 ACB > HL1 ACO > HL2 decrease no change ______________________________________

Claim 11

A method in accordance with claim 7 wherein said step of manipulating the flow rate of said external reflux in response to said first control signal comprises: establishing a third signal representative of the actual flow rate of said external reflux; using computing means to compare said third signal and said first control signal and to establish a fourth signal which is responsive to the difference between said third signal and said first control signal, wherein said fourth signal is scaled so as to be representative of the position of a first control valve, operably located so as to control the flow rate of said external reflux, required to maintain the actual flow rate of said external reflux substantially equal to the desired flow rate represented by said first control signal; and manipulating said first control valve in response to said fourth signal.

Claim 12

A method in accordance with claim 7 wherein said selected point in said fractional distillation column is a selected tray in said fractional distillation column and wherein said step of manipulating the flow rate of heat to said fractional distillation column in response to said second control signal comprises: establishing a third signal representative of the actual temperature of said selected tray; using computing means to compare said third signal and said second control signal and to establish a fourth signal which is responsive to the difference between said third signal and said second control signal, wherein said fourth signal is scaled so as to be representative of the flow rate of heating fluid to said fractional distillation column required to maintain the actual temperature of said selected tray substantially equal to the desired temperature represented by said second control signal; establishing a fifth signal representative of the actual flow rate of said heating fluid; using computing means to compare said fourth signal and said fifth signal and to establish a sixth signal which is responsive to the difference between said fourth signal and said fifth signal, wherein said sixth signal is scaled so as to be representative of the position of a second control valve, operably located so as to control the flow rate of said heating fluid to said fractional distillation column, required to maintain the actual flow rate of said heating fluid substantially equal to the desired flow rate represented by said fourth signal; and manipulating said second control valve in response to said sixth signal to thereby maintain the actual flow rate of said heating fluid to said fractional distillation column substantially equal to the desired flow rate represented by said fourth signal.

Claim 13

A method in accordance with claim 7 additionally comprising the steps of: establishing a third signal representative of the actual flow rate of said feed mixture to said fractional distillation column; lagging said third signal to establish a fourth signal; delaying said fourth signal to establish a fifth signal; substracting said fifth signal from said fourth signal to establish a sixth signal; establishing a seventh signal representative of a bias term; multiplying said sixth signal and said seventh signal to establish an eighth signal; and adding said eighth signal to said first control signal to thereby apply a feedforward compensation for changes in the flow rate of said feed mixture to said fractional distillation column to the desired flow rate of said external reflux.

Claim 14

A method in accordance with claim 7 wherein the high limit for the concentration of said first component in said bottoms product stream is the desired concentration of said first component in said bottoms product stream, wherein the low limit for the concentration of said first component in said bottoms product stream is a percentage of the high limit for the concentration of said first component in said bottoms product stream, wherein the high limit for the concentration of said second component in said overhead product stream is the desired concentration of said second component in said overhead product stream and wherein the low limit for the concentration of said signal component in said overhead product stream is a percentage of the high limit for the concentration of said second component in said overhead product stream.