Method and apparatus for controlling a material treater

• US 3,989,935 A
• Filed: 11/01/1974
• Issued: 11/02/1976
• Est. Priority Date: 11/01/1974
• Status: Expired due to Term

• Current Assignee: Formica Technology, Inc.
• Original Assignee: Formica Corporation (Broadview Holding BV)
• Inventors: Fay, Charles Robert
• Primary Examiner(s): Wise, Edward J.
• Application Number:
  US05/520,075
• Time in Patent Office: 732 Days
• Field of Search: 235/151.13, 235/151.12, 235/151.1, 235/151.11, 235/151.3, 235/151.35, 235/151.33, 73/23, 73/150, 118/8, 118/9, 117/66
• US Class Current: 700/208
• CPC Class Codes: G05B 13/0205 not using a model or a simulator of the controlled system
• CPC Class Codes: G06G 7/122 for optimisation, e.g. least square fitting, linear programming, critical path analysis, gradient method

Abstract

An improved process and apparatus are disclosed wherein the resin treatment of a web on a material treater is conducted at optimal throughput with exacting, self-adaptive, feed forward, feedback control.

Claims

1. A method of controlling the drying of a fibrous host material which has been treated with a resinous solution which comprises:

1. measuring the weight of said host material before treating and providing a signal (A) representative of said weight before treating,

2. measuring the weight of the treated material before drying and providing a signal (B) representative of said weight before drying,

3. measuring the weight of the dried, treated material and providing a signal (C) representative of said weight after drying,

4. providing a signal (D) representative of the resin solids fraction of said resinous solution,

5. determining the actual percent volatiles of said dried, treated material from said signals (A), (B), (C) and (D) and providing a signal (E) representative of said percent volatiles,

5. A method according to claim 1 including providing a signal (R) representative of the moisture content of said host material before treating and using said signal (R) in steps (5), (13), (15) and (17).

7. A method according to claim 1 wherein said actual film coefficient of the material undergoing drying is computed by

a. calculating from said signal (B) the weight of the treated, undried host material on a per square foot basis and providing signal (S) representative of said weight,

b. providing a signal (R) representative of the moisture content of said host material before treating and calculating from said signal (A) and said signal (R) the dry weight of the host material and providing signal (T) representative of said dry weight,

c. calculating from said signal (A) and said signal (B) the amount of resinous solution applied to said host material before drying on a per square foot basis and providing signal (U) representative of said amount of applied solution,

d. calculating the total resin solids in said host material from said signal (U) and said signal (D) and providing signal (V) representative of said total resin solids,

e. calculating the total solids of the treated host material from said signal (T) and said signal (V) and providing a signal (W) representative of said total solids,

f. calculating the final weight of each solvent component from said signal (G), and said signal (U) and providing a signal (X) representative of said final weights and

g. calculating said actual film coefficient from said signals, (E), (H), (I), (J), (K), (L), (M), (S), (T), (W) and (X) and providing said signal (N).

8. A method according to claim 1 wherein said solvent component percentages are provided by continuous on line measurement.

9. A method according to claim 1 wherein said actual film coefficient is computed by convergence.

10. A method according to claim 1 wherein said step signal (P) is determined by convergence.

14. Apparatus according to claim 8 comprising fourth gauge means mounted before said treater and adjacent to said host material so as to measure the average moisture content of said material and provide a signal (R) representative of said moisture content to said means (5), (13), (15) and (17).

15. Apparatus according to claim 8 wherein said means for computing the actual film coefficient of the material undergoing drying includes

a. means responsive to said signal (B) for computing the weight of the treated, host material on a per square foot basis and providing signal (S) representative of said weight,

b. means responsive to said signal (A) and a signal (R) representative of the moisture content of said host material before treating for computing the dry weight of the host material and providing a signal (T) representative of said dry weight,

c. means responsive to said signal (A) and said signal (B) for computing the amount of resinous solution applied to said host material before drying on a per square foot basis and providing a signal (U) representative of said amount of applied solution,

d. means responsive to said signal (U) and said signal (D) for computing the total resin solids in said host material and providing a signal (V) representative of said total resin solids,

e. means responsive to said signal (T) and said signal (V) for computing the total solids of the treated host material and providing a signal (W) representative of said total solids,

f. means responsive to said signal (G), and said signal (U) for computing the final weight of each solvent component and providing signals (X) representative of the final weights, and

g. means responsive to said signals (S), (T), (W), (X), (E), (H), (I), (J), (K), (L) and (M) for computing said actual film coefficient and providing said signal (N).

16. Apparatus according to claim 10 wherein said means for providing solvent component percentages includes continuous on-line measurement means.

17. Apparatus according to claim 10 wherein said first, second and third gauge means are scanning gauges.

2. providing a signal (F) representative of the specification percent volatiles of said dried, treated material,providing a signal (G) representative of the solvent component percentages and a signal (H) representative of the latent heat of vaporization of each solvent component of said resinous solution,measuring the line speed of said host material and providing a signal (I) representative of said line speed,providing a signal (J) representative of the length of the dryer,measuring the dryer temperature and providing a signal (K) representative of said temperature,

6. A method according to claim 2 wherein said moisture content is continually measured.

3. providing a signal (L) representative of the heat capacity of the host material,measuring the temperature of said host material before treating and providing a signal (M) representative of said temperature before treating,computing the actual film coefficient (h_A) of the material undergoing drying using said signals (A), (B), (C), (D), (E), (G), (H), (I), (J), (K), (L) and (M) and providing a signal (N) representative of said actual film coefficient,providing a signal (O) representative of the specification line speed of said host material,

4. computing the temperature needed in the dryer to achieve said specification percent volatiles at said specification line speed using said signals (A), (B), (D), (F), (G), (H), (J), (L), (M), (N) and (O) and providing a signal (P) representative of said needed temperature,controlling said dryer temperature in accordance with said signal (P),computing the line speed necessary to achieve said specification percent volatiles in accordance with said signal (K) using said signals (A), (B), (D), (F), (G), (H), (J), (K), (L), (M) and (N) and providing signal (Q) representative of said necessary line speed andcontrolling said line speed in accordance with said signal (Q).

11. In a fibrous host material treating process wherein said material is treated with a resinous solution in a treater and dried in a dryer, apparatus for controlling the drying of said treated material comprisingfirst gauge means adjacent to said material for measuring the weight of said material before treating and providing a signal (A) representative of said weight before treating,second gauge means mounted before said dryer and adjacent to said material for measuring the treated, undried weight of said material and providing a signal (B) representative of said treated, undried weight,

12. third gauge means mounted after said dryer and adjacent to said material for measuring the dried weight of said material and providing a signal (C) representative of said dried weight,means for providing a signal (D) representative of the resin solids fraction of said resinous solution,means responsive to said signals (A), (B), (C) and (D) for computing the actual percent volatiles of the dried, treated material and providing a signal (E) representative of said percent volatiles,means for providing a signal (F) representative of the specification percent volatiles of said dried, treated material,means for providing a signal (G) representative of the solvent component percentages and a signal (H) representative of heat of vaporization of each solvent component of said resinous solution,means for measuring the line speed of said material and providing a signal (I) representative of said line speed,means for providing a signal (J) representative of the dryer length,means for measuring the temperature of said dryer and providing a signal (K) representative of said temperature,means for providing a signal (L) representative of the heat capacity of the host material,means for measuring the temperature of said host material before treating and providing a signal (M) representative of said temperature before treating,

13. means responsive to said signals (A), (B), (C), (D), (E), (G), (H), (I), (J), (K), (L) and (M) for computing the actual film coefficient of the material undergoing drying and providing a signal (N) representative of the actual film coefficient,means for providing a signal (O) representative of the specification line speed of said host material,means responsive to said signals (A), (B), (D), (F), (G), (H), (J), (L), (M), (N) and (O) for computing the temperature needed in the dryer to achieve said specification percent volatiles at said specification line speed and providing a signal (P) representative of said needed temperature,means responsive to said signal (P) for controlling the dryer temperature,means responsive to said signals (A), (B), (D), (F), (G), (H), (J), (K), (L), (M) and (N) for computing the line speed necessary to achieve said specification percent volatiles in accordance with said signal (K) and providing a signal (Q) representative of said necessary line speed andmeans responsive to said signal (Q) for controlling said line speed.