Control scheme for rapid pulp delignification and bleaching

• US 5,672,247 A
• Filed: 03/03/1995
• Issued: 09/30/1997
• Est. Priority Date: 03/03/1995
• Status: Expired due to Fees

• Current Assignee: Union Camp Patent Holding, Inc.
• Original Assignee: Union Camp Patent Holding, Inc.
• Inventors: Falcone, Ronald A. Jr., Bosch, Gregory J., Mayo, William L., Pangalos, George
• Primary Examiner(s): Weier, Anthony J.
• Application Number:
  US08/399,717
• Time in Patent Office: 942 Days
• Field of Search: 162/238, 162/49, 162/62, 162/65
• US Class Current: 162/65
• CPC Class Codes: D21C 9/1052 Controlling the process
• CPC Class Codes: D21C 9/153 with ozone

Abstract

A process control for adjusting bleaching agent application in response to the pulp brightness and/or K number is realized by utilizing a coupled control feedforward and/or feedback control system or combination thereof wherein brightness measurements are made between successive K number measurements and adjustments made to the bleaching agent application in response to a comparison value.

Claims

1. A coupled control method for controlling a continuous ozone bleaching process for paper pulp to a desired degree of bleaching, which comprises:

(a) adding feed ozone at a desired amount to the pulp;

(b) passing the pulp continuously into and out of a bleaching reactor;

(c) measuring ingoing pulp brightness between successive ingoing pulp K number measurements; and

(d) adjusting the quantity of feed ozone required to reach a desired degree of bleaching in response to the measured brightness and K number values.

2. The method of claim 1, wherein the brightness values are measured periodically between successive K number measurements.

3. The method of claim 1, wherein the brightness values are measured continuously between successive K number measurements.

4. The method of claim 1, wherein the brightness values of multiple measurements are averaged together to derive a brightness value which is used to initiate an adjustment in the quantity of feed ozone.

5. The method of claim 1, wherein the quantity of feed ozone is also adjusted by a moving average of at least three K number measurements.

6. The method of claim 1, wherein the adjusting step comprises:

(a) periodically measuring the K number of the incoming pulp as it passes into the reactor and adjusting the amount of feed ozone to obtain the desired degree of bleaching;

(b) measuring the pulp brightness between periodic K number measurements, and making a moving average of several pulp brightness measurements;

(c) comparing the average brightness measurement with the brightness representing the K number for that period prior to the next K number measurement to initiate a change in feed ozone; and

(d) adjusting the quantity of feed ozone in response to the comparison value.

7. The method of claim 6, wherein step (b) is repeated periodically.

8. The method of claim 6, wherein the step (b) is repeated continuously.

9. The method of claim 6, wherein the pulp brightness is measured about every second to about ten minutes between K number measurements.

10. The method of claim 6, wherein the ingoing measured pulp property is the pulp K number-In (K_In) and the outgoing measured pulp property is the pulp K number-Out (K_Out) and the desired degree of bleaching is the target K number-Out (target K_Out) and the expected K number entering the ozone stage is the target K number-In (target K_In).

11. The method of claim 6, wherein the ozone application required to bleach the pulp is calculated from the formula:

space="preserve" listing-type="equation">O.sub.3app =C.sub.1 +C.sub.2 ( K.sub.In !- target K.sub.In !)+C.sub.3 ( captured GEB.sub.In !- GEB.sub.In !)+C.sub.4 ( K.sub.Out !- target K.sub.Out !)+C.sub.5 ( captured GEB.sub.Out !- GEB.sub.Out !)

wherein O_3app is the calculated ozone application necessary to achieve the desired degree of bleaching, and C₁ through C₅ are constants.

12. The method of claim 6, wherein the amount of ozone is further adjusted by correcting for at least the pH of the ingoing pulp, the temperature of the ingoing pulp, or the residence time of the pulp in the reactor.

13. A coupled control method for controlling a continuous ozone bleaching process for paper pulp to a desired degree of bleaching, which comprises:

(a) adding feed ozone at a desired amount to the pulp;

(b) passing the pulp continuously into and out of a bleaching reactor;

(c) measuring the brightness value of the pulp between successive K number measurements; and

(d) adjusting the quantity of feed ozone required to reach a desired degree of bleaching in response to the measured brightness and K number values;

wherein the measured pulp property is an ingoing pulp property; and

the adjusting step comprises;

(e) periodically measuring the K number of the incoming pulp as it passes into the reactor and adjusting the amount of feed ozone to obtain the desired degree of bleaching;

(f) measuring the pulp brightness between periodic K number measurements, and making a moving average of several pulp brightness measurements;

(g) comparing the moving average brightness measurement with the brightness representing the K number for that period prior to the next K number measurement to initiate a change in feed ozone; and

(h) adjusting the quantity of feed ozone in response to the comparison value.

14. The method of claim 13, wherein the ingoing measured pulp property is the pulp K number-In (K_In) and the outgoing measured pulp property is the pulp K number-Out (K_Out) and the desired degree of bleaching is the target K number-Out (target K_Out) and the expected K number entering the ozone stage is the target K number-In (target K_In) and the "GEB_In " and "GEB_Out " are the pulp brightness values measured between consecutive K number measurements at the entrance and exit of the ozone reactor respectively and with each K number measurement, a new brightness of the ingoing pulp and/or outgoing pulp is captured and these captured brightnesses are referred to as "captured GEB_In " and "captured GEB_Out ".

15. The method of claim 13, wherein the ozone application required to bleach the pulp comprises the formula:

space="preserve" listing-type="equation">O.sub.3app =C.sub.1 +C.sub.2 ( K.sub.In !- target K.sub.In !)+C.sub.3 ( captured GEB.sub.In !- GEB.sub.In !)+C.sub.4 ( K.sub.Out !- target K.sub.Out !)+C.sub.5 ( captured GEB.sub.Out !- GEB.sub.Out !)

wherein O_3app is the calculated ozone application necessary to achieve the desired degree of bleaching, and C₁ through C₅ are constants.

16. The method of claim 13, wherein the amount of ozone is further adjusted by correcting for at least the pH of the ingoing pulp, the temperature of the ingoing pulp, or the residence time of the pulp in the reactor.