IP Library Granted Patent US 10,519,814
Granted Patent B2
US 10,519,814 · App. 13/695,639 · Granted Dec 31, 2019

Control of a thermal cyclic process

Inventor: Sylvain Quoilin (Liege, BE)
Assignee: ORCAN ENERGY AG
F01K13/02F01K25/08G05B19/4155G05B2219/49204
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Quick Facts
Patent No.
US 10,519,814
App. No.
13/695,639
Granted
Dec 31, 2019
Kind
B2
Abstract

The invention relates to a method for controlling a thermal cyclic process, in particular an Organic Rankine Cycle (ORC), which is operated with a working medium in conjunction with a dynamic heat source, whereby the method comprises the following steps: (a) determination of a setpoint value of a process variable of the thermal cyclic process from a value of an input parameter or respective values of a plurality of input parameters of the thermal cyclic process; (b) control of the thermal cyclic process with the determined setpoint value of the process variable as a target variable of the control; and (c) repeated execution of steps (a) and (b) when at least one value of the input parameters changes.

Claims (22)

1. A method for controlling a thermal Organic Rankine Cycle (ORC) process, which is operated with a working medium in conjunction with a dynamic heat source, comprising:

(a) determination of a setpoint value of a process variable of the thermal cyclic process from a value of an input parameter or respective values of a plurality of input parameters of the thermal cyclic process;

(b) control of the thermal cyclic process with the determined setpoint value of the process variable as a target variable of the control; and

(c) repeated execution of steps (a) and (b) when at least one value of the input parameters changes,

wherein the determination of the setpoint value of the process variable of the thermal cyclic process comprises a calculation of the setpoint value from a predetermined function into which the input parameters are input as variables.

2. The method according to claim 1 wherein the determination of the setpoint value of the process variable of the thermal cyclic process comprises the calculation of the setpoint value from a polynomial function.

3. The method according to claim 2 with, carried out before the step (a), the additional step:

designation of the function for calculating the setpoint value of the process variable by means of carrying out trials and/or from model equations.

4. The method according to claim 3 wherein the designation of the function for calculating the setpoint value of the process variable comprises a maximisation of the product of an efficiency of the heat transfer from the heat source to the cyclic process and an efficiency of the cyclic process.

5. The method according to claim 1 wherein at least one further process variable is controlled in a corresponding manner.

6. The method according to claim 1 wherein the process variable is or the process variables are the vaporisation temperature or the vaporisation pressure of the working medium and/or the condensation temperature or the condensation pressure in a condenser of the thermal cyclic process and/or the vapour temperature or the vapour pressure at the outlet of an expansion machine of the thermal cyclic process.

7. The method according to claim 1 wherein the input parameter comprises or the input parameters comprise a mass flow of a gas from the heat source or a quantity that is representative for this mass flow and/or a temperature of the exhaust gas and/or a temperature of the outside air and/or a condensation temperature of the working medium of the cyclic process.

8. The method according to claim 1 wherein the control of the thermal cyclic process is carried out by means of model predictive control (MPC).

9. The method according to claim 1 wherein the control of the thermal cyclic process takes place by means of setting a rotational speed of a feeding pump and/or of an expansion machine and/or of a condenser fan.

10. The method according to claim 1 wherein the control comprises a repeated or continuous comparison of an actual value with the setpoint value of the process variable.

11. A device comprising:

a thermal Organic Rankine Cycle (ORC) process with one or more heat exchangers for transferring heat from one or more heat sources to a working medium of the thermal cyclic process; and a microprocessor for carrying out the method according to claim 1 for controlling the thermal cyclic process.

12. A computer program product comprising at least one non-transitory computer-readable medium with instructions that can be executed by a computer and that are for carrying out a method for controlling an Organic Rankine Cycle (ORC) process during operation on a computer, the instructions when executed by the computer cause the computer to:

(a) determine a setpoint value of a process variable of the thermal cyclic process from a value of an input parameter or respective values of a plurality of input parameters of the thermal cyclic process;

(b) control of the thermal cyclic process with the determined setpoint value of the process variable as a target variable of the control; and

(c) repeat execution of steps (a) and (b) when at least one value of the input parameters changes,

wherein the determination of the setpoint value of the process variable of the thermal cyclic process comprises a calculation of the setpoint value from a predetermined function into which the input parameters are input as variables.

Assignments (2)
CHANGE OF NAME Recorded Apr 25, 2016
From: ORCAN ENERGY GMBH
To: ORCAN ENERGY AG
Reel/Frame 038506/0948 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 30, 2012
From: QUOILIN, SYLVAIN
To: ORCAN ENERGY GMBH
Reel/Frame 029383/0962 →
Priority Claims (1)
DE 10 2010 019 718 · May 7, 2010 · national
Continuity (1)
Related Publication 20180328232A1 · Nov 15, 2018
Cited By (5)
US 12,305,624 US 12,312,981 US 12,385,474 US 12,454,896 US 12,534,990