Method and an apparatus for automatically tuning a process regulator

• US 4,758,943 A
• Filed: 12/03/1986
• Issued: 07/19/1988
• Est. Priority Date: 04/03/1985
• Status: Expired due to Fees

• Current Assignee: Hightech Network AB
• Original Assignee: Hightech Network AB
• Inventors: Astrom, Karl J., Hagglund, Tore
• Primary Examiner(s): RUGGIERO, JOSEPH F
• Assistant Examiner(s): Hoang, Steve
• Application Number:
  US06/946,569
• Time in Patent Office: 594 Days
• Field of Search: 364/148, 364/149, 364/151, 364/157-163, 364/178, 364/179, 364/553, 318/561, 318/569, 318/610, 318/620, 318/636
• US Class Current: 700/37
• CPC Class Codes: G05B 13/045 using a perturbation signal

Abstract

Method for adjusting the setting of a digital process regulator on the basis of the result obtained from a simple relay feedback experiment. When an adjustment of the regulator setting is to be made, the relay feedback is connected in the control feedback circuit instead of the regulator in order to cause self-oscillation. The self-oscillation signal is utilized to calculate the new setting of the regulator.

Claims

1. A method for tuning automatically a process regulator (2), in which a relay feedback (4) can be connected alternatively to the regulator (2) in the control feedback circuit of the process, and wherein, whenever retuning of the regulator is required, the relay feedback is connected in the circuit instead of the regulator in order to cause self-oscillation of the system process/relay feedback circuit, and in which said self-oscillation is used to calculate the setting of the regulator, said process comprising the steps of

(a) indicating within one period of self-oscillation a time point (t_max) at which a local signal peak value first occurs;

(b) dividing the signal obtained within a half period into a selected number of n sampling intervals with intervals h_i therebetween;

(c) calculating the regulator control setting successively from various sampling intervals within the first half period of the oscillating period with a starting point from a model of the process beginning from the sampling interval occurring after said time point (t_max);

(d) comparing the result of the calculations with given compatibility conditions; and

(e) terminating the successive calculations, and applying the calculated control setting to the regulator (2) immediately upon reaching a calculation which satisfies the aforesaid compatability conditions.

2. A method according to claim 1, including the steps of

(a) selecting the number of samplings n within a half-period successively, commencing with n equals at least 2;

(b) making successive calculations with increasing values of n and calculating model parameters for all sampling intervals after t_max within the first half-period for each n, until a calculation is reached which provides model parameters which fulfill set compatibility conditions.

3. A method according to claim 1 or 2, including making the calculations with the aid of z-transforms and a process model of the form

4. A method according to claim 3, wherein the process model incorporates one of the following combinations of m and l:

m=1 and l=2;

m=2 and l=1;

m=2 and l=2.

5. A method according to claim 4, including the steps of using the values of the input and output signals of the process with relay feedback at the sampling points as the basis for constructing a z-transform of the input signal and the output signal;

and by calculating the constants a₁ -a_m, b₁ -b_m from the z-transformed process model so as to express the resultant sampled values y_i on the output signal at different sampling points.

6. A method according to claim 5, including the steps of (a) applying a characteristic polynomial of the type

7. A method according to claim 1, wherein the curve shape of the period of self--oscillation on which the calculations are made is obtained by producing a mean value curve on several periods of the self-oscillation obtained through relay feedback.

8. A method according to claim 1 wherein with relay feedback a comparison is made in a manner known per se between a set-point value y_ref and the process output signal;

and the input signal to the process is switched from a value which is lower than the set-point value to a value which is higher than the set-point value and vice versa at a pre-selected level subsequent to the value of the process output signal having passed the set-point value y_ref, i.e. has effected its reversal with a pre-selected hysteresis.

9. Apparatus for automatically tuning a process regulator with the aid of a relay feedback (4) which can be alternatively connected to the regulator (2) in the feedback circuit of the process (1), said apparatus comprising (a) a computer and control unit (5) which when coupled to relay feedback, is effective to (a) detects a self-oscillating period of the system, (b) divide said period into half-periods at a selected number n of the sampling points, (c) detect a time point t_max within one of the oscillation half-periods at which a local signal peak value occurs for the first time and effect successively a calculation of a process model for each sampling moment during the first half-period after t_max, and (d) to compare each calculation with stored compatability conditions, and immediately upon reaching a calculation which satisfies set compatability conditions inhibit calculation of the model for the next sampling period in line, and with control to the regulator (2) adjust the calculated model for control in the regulator.

10. Apparatus according to claim 9, wherein the computer and control means (5) includes a microprocessor in which there are stored calculating sequencies for computing models which are individual for each theoretically possible sampling interval for each theoretically possible sampling interval division of the self-oscillating signal obtained when engaging the relay feedback (4).

11. Apparatus according to claim 9 or 10, wherein an analogue filter (9) and a digital filter (10) which can be tuned individually to each particular calculating process and which are incorporated in a regulator/process feedback loop, at least when the regulator is in its active mode.