Live steam determination of an expansion engine
The present invention provides a method for open-loop controlling or closed-loop controlling and/or monitoring a device with an expansion engine which is supplied live steam of a working medium that is expanded to exhaust steam in the expansion engine comprising the steps: determining at least one physical parameter of the exhaust steam; determining at least one physical parameter of the live steam based on the determined at least one physical parameter of the exhaust steam; and open-loop controlling or closed-loop controlling and/or monitoring the device based on the at least one determined physical parameter of the live steam. A thermal power plant is also provided in which the method is realized.
1. A method for open-loop controlling or closed-loop controlling and/or monitoring a device having an expansion engine, the method comprising:
supplying said expansion engine with live steam of an organic working medium in a supercritical state or in a wet steam region that is expanded to exhaust steam in said expansion engine;
determining at least one physical parameter of said exhaust steam;
determining an isentropic degree of efficiency of said expansion engine;
determining at least one physical parameter of said live steam based on the determined at least one physical parameter of said exhaust steam and the determined isentropic degree of efficiency;
open-loop controlling or closed-loop controlling and/or monitoring said device based on said at least one determined physical parameter of said live steam; and
operating said device within a framework of an Organic Rankine Cycle (ORC) process for generating electrical energy.
2. The method according to claim 1 , further comprising the step of determining a compression ratio of said organic working medium applied to said expansion engine and a mass flow of said organic working medium, and in which said isentropic degree of efficiency of said expansion engine is determined based on the determined applied compression ratio of said organic working medium and the mass flow of said organic working medium.
3. The method according to claim 1 , in which said expansion engine is a displacement engine, and further comprising the step of determining a rotational speed of said expansion engine, and in which the isentropic degree of efficiency of said expansion engine is determined based on said determined rotational speed of said expansion engine.
4. The method according to claim 3 , wherein supplying said expansion engine further comprises supplying said expansion engine defined as one of a piston expansion engine, a scroll expander or a screw expander.
5. The method according to claim 1 , comprising the step of modeling an operation of said expansion engine with said organic working medium based on thermodynamic equations and empirically determined parameters values, and in which said isentropic degree of efficiency of said expansion engine is determined based on a result of modeling the operation of said expansion engine.
6. The method according to claim 1 , in which said at least one determined physical parameter of said exhaust steam comprises a temperature and/or a pressure of said exhaust steam.
7. The method according to claim 6 , comprising the step of determining a temperature of said live steam based on the determined temperature and the determined pressure of said exhaust steam.
8. The method according to claim 1 , further comprising the step of determining a pressure of said live steam which differs from said at least one determined physical parameter of said live steam being determined based on said at least one determined physical parameter of said exhaust steam, and in which said at least one physical parameter of said live steam is determined based on said determined pressure of said live steam.
9. The method according to claim 1 , in which said at least one determined physical parameter of said live steam comprises a temperature and/or an enthalpy and/or an entropy and/or a volume ratio of a gaseous to a liquid phase and/or a steam content and/or a density ratio of the gaseous to the liquid phase of said live steam.
10. The method according to claim 1 , wherein operating said device further comprises operating said device, wherein said device is a steam power plant or a component thereof.
11. A thermal power plant, comprising:
an expansion engine operated within a framework of an Organic Rankine Cycle (ORC) process for generating electrical energy, which is supplied live steam of an organic working medium in a supercritical state or in a wet steam region that is expanded to exhaust steam in said expansion engine; and
an open-loop or closed-loop controller configured to:
determine at least one physical parameter of said exhaust steam;
determine an isentropic degree of efficiency of said expansion engine;
determine at least one physical parameter of said live steam based on said determined at least one physical parameter of said exhaust steam and the determined isentropic degree of efficiency; and
open-loop control or closed-loop control and/or monitoring said thermal power plant based on said at least one determined physical parameter of said live steam.