IP Library Granted Patent US 8,668,380
Granted Patent B2
US 8,668,380 · App. 12/476,474 · Granted Mar 11, 2014

Method for operating a calorimeter

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,668,380
App. No.
12/476,474
Granted
Mar 11, 2014
Kind
B2
Abstract

A method for operating a calorimeter and a calorimeter that is operable to perform the method, wherein the calorimeter has a reactor ( 1 ) for receiving a reaction medium, a reactor jacket ( 2 ), an in-reactor heater ( 4 ) controlled by means of a first controller ( 6 ), an outer temperature control unit ( 9 ) in thermal contact with the reactor and controlled by a second controller ( 10 ), and a measurement sensor ( 5 ) arranged in the reactor for determining a reactor temperature (T r ). The reactor temperature is controlled by the heat which is delivered to the reactor by the in-reactor heater and by the heat that is carried in and/or out by the outer temperature control unit. A dynamic control of the heating power of the in-reactor heater and of the outer temperature control unit is used to eliminate any deviation of the reactor temperature from a reactor set-point temperature.

Claims (55)

1. A method for operating a calorimeter comprising a reactor for receiving a reaction medium, a reactor jacket, an in-reactor heater controlled by a first controller, an outer temperature control unit in thermal contact with the reactor and controlled by a second controller, and a measurement sensor arranged in the reactor, the method comprising the steps of:

setting a set-point temperature for the reactor and entering the reactor set-point temperature into the first controller;

determining a reactor temperature using the measurement sensor and determining a deviation of the reactor temperature from the reactor set-point temperature as a control deviation of the first controller, the reactor temperature being controlled by the heat delivered to the reactor by at least one of the in-reactor heater and the outer temperature control unit and by the heat taken away from the reactor by the outer temperature control unit;

splitting the determined control deviation into first and second parts, and dynamically adjusting the power, to compensate for the control deviation, through the substeps of:

delivering the first part as heat to the reactor by the in-reactor heater, and

entering the first and second parts into the second controller for controlling the outer temperature control unit, and

adjusting the reactor temperature to the reactor set-point temperature as a result of the heat carried into and/or out of the reactor.

2. The method of claim 1 , wherein:

the step of determining the reactor temperature occurs at predetermined time intervals or continuously.

3. The method of claim 2 , wherein:

the first part of the control deviation corresponds to a set-point range.

4. The method of claim 2 , wherein:

the first part of the control deviation has the form of a sigmoid function.

5. The method of claim 2 , wherein:

the substep of entering the first and second parts of the control deviation to the second controller, which is configured as a cascade controller, is achieved by:

delivering the first part to a proportional operator of the second controller; and

delivering the second part to an integrating operator of the second controller.

6. The method of claim 5 , wherein:

the substep of delivering the first part of the control deviation power as heat to the reactor is achieved by the in-reactor heater, which is an electrical heater whose power is controlled by the first controller.

7. The method of claim 6 , wherein:

the second controller controls a temperature of a reactor jacket that cooperates with the outer temperature control unit.

8. The method of claim 7 , comprising the step of:

calculating an input for the second controller, using the second part of the control deviation and feeding the calculated input into the second controller.

9. The method of claim 1 , wherein:

the substep of entering the first and second parts of the control deviation to the second controller, which is associated with the first controller as a cascade controller, is achieved by:

delivering the first part to a proportional operator of the second controller; and

delivering the second part to an integrating operator of the second controller.

10. The method of claim 1 , wherein:

the substep of delivering the first part of the control deviation power as heat to the reactor is achieved by the in-reactor heater, which is an electrical heater whose power is controlled by the first controller.

11. The method of claim 1 , wherein:

the second controller controls a temperature of a reactor jacket that cooperates with the outer temperature control unit.

12. The method of claim 1 , wherein:

the step of splitting the determined control deviation occurs in a logic circuit, based upon predetermined inputs, including the maximum power of the in-reactor heater and a proportional part of the first controller.

13. A calorimeter, comprising:

a reactor for receiving a reaction medium;

an in-reactor heater to supply heat to the reactor;

a first controller, in controlling communication with the in-reactor heater;

an outer temperature control unit in thermal contact with the reactor for supplying heat thereto or removing heat therefrom;

a second controller, in controlling communication with the outer temperature control unit and in communication with the first controller;

a first measurement sensor, arranged in the reactor for determining a reactor temperature, the first measurement sensor in communication with at least the first controller so that a deviation of the reactor temperature from a reactor set-point temperature is dynamically adjusted through the heating power of the in-reactor heater and the outer temperature control unit; and

a control unit on which a computer program is stored, the computer program comprising an instruction set that implements an operating method that comprises the steps of:

setting a set-point temperature for the reactor and entering the reactor set-point temperature into the first controller;

determining a reactor temperature using the measurement sensor and determining a deviation of the reactor temperature from the reactor set-point temperature as a control deviation of the first controller, the reactor temperature being controlled by the heat delivered to the reactor by at least one of the in-reactor heater and the outer temperature control unit and by the heat taken away from the reactor by the outer temperature control unit;

splitting the determined control deviation into first and second parts, and dynamically adjusting the power, to compensate for the control deviation, through the substeps of:

delivering the first part as heat to the reactor by the in-reactor heater, and

entering the first and second parts into the second controller for controlling the outer temperature control unit, and

adjusting the reactor temperature to the reactor set-point temperature as a result of the heat carried into and/or out of the reactor.

14. The calorimeter of claim 13 , further comprising:

a reactor jacket that cooperates with the outer temperature control unit.

15. The calorimeter of claim 14 , wherein:

the second controller is in a cascade arrangement with the first controller.

16. The calorimeter of claim 13 , wherein:

the second controller is in a cascade arrangement with the first controller.

17. The calorimeter of claim 13 , further comprising:

a further controller, communicated to each of the first and second controllers, the further controller operating to communicate the first and second controllers with each other.

Assignments (2)
CHANGE OF NAME Recorded Jan 8, 2016
From: METTLER-TOLEDO AG
To: METTLER-TOLEDO GMBH
Reel/Frame 037459/0811 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 2, 2009
From: SCHENKER, BENEDIKT
To: METTLER-TOLEDO AG
Reel/Frame 022765/0987 →