Method and device for the consideration of varying volume and flow in the control of a continuous flow process

• US 5,428,527 A
• Filed: 08/25/1992
• Issued: 06/27/1995
• Est. Priority Date: 12/28/1989
• Status: Expired due to Term

• Current Assignee: Antti J. Niemi
• Original Assignee: Antti J. Niemi
• Inventors: Niemi, Antti J.
• Primary Examiner(s): Trammell, James P.
• Application Number:
  US07/920,436
• Time in Patent Office: 1,036 Days
• Field of Search: 364/152, 364/509, 364/510, 364/500, 364/501, 364/502, 364/503, 364/160, 55/106, 55/5, 55/210, 137/209, 137/2, 137/1-6, 137/87, 137/88, 137/101.25, 137/101.31, 137/624.11, 137/563, 73/149, 210/662, 210/744, 604/65, 604/67, 604/82, 366/132, 417/26, 417/28
• US Class Current: 700/32
• CPC Class Codes: G05D 11/132 by controlling the flow of the individual components G05D11/133 takes precedence

Abstract

The control method is directed to a quality characteristic of the process material, typically to its outlet concentration. In control of the actuator which is a part of feedforward or feedback control of outlet concentration, one takes account of changes of the material volume and flow, in addition to the inlet concentration or control deviation. With this object, at least two of the quantities of inlet flow, outlet flow and material volume are measured or determined and by means of them a variable is further determined with regard to which the control method is invariant. Two alternative variables are presented, one being typically applicable to control of a process with finite distribution of the flow velocity and the other to control of a process with vigorous mixing. By means of a time-variable control method, the controls can also be implemented with time as the independent variable. The invention also relates to devices which implement the control methods presented.

Claims

1. A method for incorporation of varying volume and flow in the control of other process variables in a continuous flow process, comprising the steps of:

measuring and storing at least two of the process variables of inlet flow (Q_in), outlet flow (Q) and volume (V);

determining a new variable (z) at time (t) wherein said new variable (z) is dependent on said at least two process variables;

determining an output quantity (u(t)) of a controller at the same time (t) based on the new variable (z) by using a method which is invariant with respect to the new variable (z); and

controlling one or more of said other process variables by applying a signal representative of the determined output quantity (u(t)) to a means for controlling said other process variables.

2. The method of claim 1, wherein the step of determining a new variable (z) includes the steps of integrating the inlet flow (Q_in) with respect to time up to a time (t) and dividing the integrated inlet flow by the volume V(t) at the same time (t).

3. The method of claim 2, wherein the step of determining the output quantity (u(t)) comprises the step of determining the output quantity (u(t)) based on a difference between a prescribed value (C_ref) of the output quantity and a measured value (C_o) of the output quantity;

wherein

a) said difference is multiplied by a first coefficient;

b) said difference is multiplied by the value of the inlet flow, the product is integrated with respect to time up to a time (t), the result of the integration is divided by the volume (V(t)), and the quotient is multiplied by a second coefficient,

c) said difference is differentiated with respect to the time (t), the derivative is multiplied by the value of the volume V(t), the product is divided by the value of the inlet flow at the same time (t), and the quotient is multiplied by a third coefficient, and

d) the results obtained either in a) and b) or in a) and c) or in a), b) and c) are summed up, the coefficients stated in a), b) and c) being constants or slowly changing quantities.

4. The method of claim 1, wherein the step of determining a new variable (z) includes the steps of dividing the inlet flow (Q_in) by the volume (V) and integrating the quotient with respect to time up to the time (t).

5. The method of claim 4, wherein the step of determining the output quantity (u(t)) comprises the step of determining the output quantity (u(t)) based on a difference between a prescribed value (C_ref) of the output quantity and a measured value (C_o) of the output quantity;

wherein

a) said difference is multiplied by a first coefficient,

b) said difference is multiplied by the value of the inlet flow, the product is divided by the value of the volume, the quotient is integrated with respect to time up to a time (t), the result of the integration is multiplied by a second coefficient,

c) said difference is differentiated with respect to the time (t), the derivative is multiplied by the value of the volume (V(t)), the product is divided by the value of the inlet flow at the same time (t), and the quotient is multiplied by a third coefficient, and

d) the results obtained either in a) and b) or in a) and c) or in a), b) and c) are summed up, the coefficients stated in a), b) and c) being constants or slowly changing quantities.

6. A method for incorporation of varying mass and flow in the control of other process variables in a continuous flow process in a gas vessel of constant volume comprising the steps of:

measuring and storing at least two of the process variables of inlet flow, outlet flow and mass or pressure,

determining a new variable by integrating the inlet flow with respect to time up to a time (t) and then dividing the integrated value by a quantity that is proportional to the mass at the same time (t);

determining an output quantity of a controller at the same time (t) based on the new variable and using a method which is invariant with respct to the new variable; and

controlling one or more of said other process variables by applying a signal representative of the determined output quantity to a means for controlling said other process variables.

7. The method of claim 6, wherein the step of determining the output quantity includes the step of determining the output quantity based on a difference between a prescribed value of the output quantity and a measured value of the output quantity;

wherein

a) said difference is multiplied by a first coefficient,

b) said difference is multiplied by the value of the inlet flow, the product is integrated with respect to time up to a time (t), the result of integration is divided by the value of the pressure at the same time (t) and the quotient is multiplied by a second coefficient,

c) said difference is differentiated with respect to the time (t), the derivative is multiplied by the value of the pressure at the same time (t), the product is divided by the value of the inlet flow at the same time (t), and the quotient is multiplied by a third coefficient, and

d) the results obtained either in a) and b) or in a) and c) or in a), b) and c) are summed up, the coefficients stated in a), b) and c) being constants or slowly changing quantities.

8. A method for incorporation of varying mass and flow in the control of other process variables in a continuous flow process in a gas vessel of constant volume comprising the steps of:

measuring and storing at least two of the process variables of inlet flow, outlet flow and mass or pressure,

determining a new variable by dividing the inlet flow by a quantity which is proportional to the mass and integrating the quotient with respect to time up to a time (t);

determining an output quantity of a controller at the same time (t) based on the new variable and using a method which is invariant with respect to the new variable; and

controlling one or more of said other process variables by applying a signal representative of the determined output quantity to a means for controlling said other process variables.

9. The method of claim 8, wherein the step of determining the output quantity includes the step of determining the output quantity based on a difference between a prescribed value of the output quantity and a measured value of the output quantity;

wherein

a) said difference is multiplied by a first coefficient,

b) said difference is multiplied by the value of the inlet flow, the product is divided by the value of the pressure, the quotient is integrated with respect to time up to a time (t), and the result of integration is multiplied by a second coefficient,

c) said difference is differentiated with respect to the time (t), the derivative is multiplied by the value of the pressure at the same time (t), the product is divided by the value of the inlet flow at the same time (t), and the quotient is multiplied by a third coefficient,

d) the results obtained either in a) or b) or in a) and c) or in a), b) and c) are summed up, the coefficients stated in a), b) and c) being constants or slowly changing quantities.

10. An apparatus for incorporation of varying volume and flow in the control of other process variables in a continuous flow process, comprising:

means for measuring and storing at least two of the process variables of inlet flow (Q_in), outlet flow (Q) and volume (V);

means for determining a new variable (z) at time (t) wherein said new variable (z) is dependent on said at least two process variables;

means for determining an output quantity (u(t)) of a controller at the same time (t) based on the new variable (z) by using a method which is invariant with respect to the new variable (z); and

means for controlling said other process variables based on the determined output quantity (u(t)).

11. The apparatus of claim 10 wherein the means for determining the output quantity (u(t)) includes means for determining the output quantity (u(t)) based on a difference between a prescribed value (C_ref) of the output quantity and a measured value (C_o) of the output quantity;

wherein

a) said difference is multiplied by a first coefficient;

b) said difference is multiplied by the value of the inlet flow, the product is integrated with respect to time up to a time (t), the result of the integration is divided by the volume (V(t)), and the quotient is multiplied by a second coefficient;

c) said difference is differentiated with respect to the time (t), the derivative is multiplied by the value of the volume V(t), the product is divided by the value of the inlet flow at the same time (t), and the quotient is multiplied by a third coefficient; and

d) results obtained in either in a) and b) or in a) and c) or in a), b) and c) are summed up, the coefficients stated in a), b) and c) being constants or slowly changing quantities.

12. The apparatus of claim 10 wherein said means for determining the output quantity (u(t)) includes means for determining the output quantity (u(t)) based on a difference between a prescribed value (C_ref) of the output quantity and a measured value (C_o) of the output quantity;

wherein

a) said difference is multiplied by a first coefficient,

b) said difference is multiplied by the value of the inlet flow, the product is divided by the value of the volume, the quotient is integrated with respect to time up to a time (t), the result of the integration is multiplied by a second coefficient,

c) said difference is differentiated with respect to the time (t), the derivative is multiplied by the value of the volume (V(t)), the product is divided by the value of the inlet flow at the same time (t), and the quotient is multiplied by a third coefficient, and

d) the results obtained either in a) and b) or in a) and c) or in a), b) and c) are summed up, the coefficients stated in a), b) and c) being constants or slowly changing quantities.

13. An apparatus for incorporation of varying mass and flow in the control of other process variables in a continuous flow process in a gas vessel of constant volume, comprising:

means for measuring and storing at least two of the process variables of inlet flow, outlet flow and mass or pressure;

means for determining a new variable by integrating the inlet flow with respect to time up to a time (t) and then dividing the integrated value by a quantity that is proportional to the mass at the same time (t);

means for determining an output quantity of a controller at the same time (t) based on the new variable by using a method which is invariant with respect to the new variable; and

means for controlling said other process variables based on the determined output quantity.

14. An apparatus for incorporation of varying mass and flow in the control of other process variables in a continuous flow process in a gas vessel of constant volume, comprising:

means for measuring and storing at least two of the process variables of inlet flow, outlet flow and mass or pressure;

means for determining a new variable by dividing the inlet flow by a quantity which is proportional to the mass and integrating the quotient with respect to time up to a time (t);

means for determining an output quantity of a controller at the same time (t) based on the new variable by using a method which is invariant with respect to the new variable; and

means for controlling said other process variables based on the determined output quantity.