System and method for controlling the Brix of a concentrated juice product

• US 6,497,912 B2
• Filed: 11/30/2000
• Issued: 12/24/2002
• Est. Priority Date: 11/30/2000
• Status: Expired due to Fees

• Current Assignee: FMC Technologies Incorporated (TechnipFMC, plc)
• Original Assignee: FMC Technologies Incorporated (TechnipFMC, plc)
• Inventors: Milla, Jose D., Mas, Michael, Bunce, Keith
• Primary Examiner(s): HEGGESTAD, HELEN F
• Application Number:
  US09/727,142
• Publication Number:
  US 20020064583A1
• Time in Patent Office: 754 Days
• Field of Search: 426/492, 426/231, 426/599, 426/590
• US Class Current: 426/492
• CPC Class Codes: A23L 2/10 by heating or contact with dry gases

Abstract

A system and method of the present invention controls the Brix of a concentrated juice product. The results of a process change in disturbance variables on the vapor temperature in at least one of the effects of the multi-stage, multi-effect evaporator are predicted and the Brix of the concentrated juice product discharged from the evaporator is controlled based on the predicted results by controlling one of steam or juice fed into the evaporator.

Claims

1. A method of controlling the Brix of a concentrated juice product comprising the steps of:

passing juice through a multi-stage, multi-effect evaporator having juice and steam passing therethrough under vacuum to form a concentrated juice product;

predicting the results of a process change in disturbance variables on the vapor temperature in at least one of the effects of the evaporator; and

controlling the Brix of the concentrated juice product discharged from the evaporator based on the predicted results by controlling one of steam or juice flow into the evaporator.

2. A method according to claim 1, wherein the step of predicting the result of the disturbance variables includes the step of measuring the Brix of the juice fed into the evaporator as a disturbance variable.

3. A method according to claim 1, wherein the step of predicting the result of the disturbance variables includes the step of measuring the pressure of juice fed into the evaporator as a disturbance variable.

4. A method according to claim 1, and further comprising the step of controlling the pressure of steam fed into the evaporator based on the predicted results of a change in the disturbance variables.

5. A method according to claim 1, and further comprising the step of controlling the pressure of juice fed into the evaporator based on the predicted results of a change in the disturbance variables.

6. A method according to claim 1, and further comprising the step of predicting the result of disturbance variables on the vapor temperature in at least one of either the first or second effects of the evaporator.

7. A method according to claim 1, wherein the step of predicting the result of disturbance variables further comprises the step of establishing a steam setpoint.

8. A method according to claim 1, and further comprising the step of applying a cascading predictive model for predictions to establish first a steam setpoint and establish second the steam pressure into the evaporator.

9. A method of controlling the Brix of a concentrated juice product comprising the steps of:

passing juice through a multi-stage, multi-effect evaporator having juice and steam passing therethrough under vacuum to form a concentrated juice product;

predicting the results of a process change in disturbance variables on the vapor temperature in at least one of the effects of the evaporator;

measuring the Brix of the concentrated juice product discharged from the evaporator and forming a predictive feedback model based on the measured Brix and the process change in disturbance variables; and

controlling the Brix of the concentrated juice product discharged from the evaporator based on the predicted results of a process change in disturbance variables and the predictive feedback model by controlling one of steam or juice flow into the evaporator.

10. A method according to claim 9, wherein the step of predicting the result of the disturbance variables includes the step of measuring the Brix of the juice fed into the evaporator as a disturbance variable.

11. A method according to claim 9, wherein the step of predicting the result of the disturbance variables includes the step of measuring the pressure of juice fed into the evaporator as a disturbance variable.

12. A method according to claim 9, and further comprising the step of controlling the pressure of steam fed into the evaporator based on the predicted results of a change in the disturbance variables.

13. A method according to claim 9, and further comprising the step of controlling the pressure of juice fed into the evaporator based on the predicted results of a change in the disturbance variables.

14. A method according to claim 9, and further comprising the step of predicting the result of disturbance variables on the vapor temperature in at least one of either the first or second effects of the evaporator.

15. A method according to claim 9, wherein the step of predicting the result of disturbance variables further comprises the step of establishing a steam setpoint.

16. A method according to claim 9, and further comprising the step of applying a cascading predictive model for predictions to establish first a steam setpoint and establish second the steam pressure.