Method for automatically controlling a stationary gas engine
A method for automatically controlling a stationary gas engine, where an engine speed control deviation is computed from a set engine speed (nSL) and an actual engine speed (nIST), and a set torque is determined as a correcting variable from the speed control deviation by a speed controller, where a set volume flow is determined as a function of the set torque to establish a mixture throttle angle (DKW 1 , DKW 2 ) and a gas throttle angle, and where the set volume flow is varied to adjust the gas throttle angle by a correction factor.
1. A method for automatically controlling a stationary gaseous fueled engine, comprising the steps of:
computing an engine speed control deviation (dn) from a set engine speed (nSL) and an actual engine speed (nIST);
determining a set torque (MSL) as a correcting variable from the speed control deviation (dn) by a speed controller;
determining a set volume flow (VSL) as a function of the set torque (MSL) to establish a mixture throttle angle (DKWI, DKW 2 ) and a gaseous fuel throttle angle;
varying the set volume flow (VSL) to adjust the gaseous fuel throttle angle by a correction factor (k); and
computing the correction factor (k) using a volume correction unit as a function of an actual system output (PAIST) and a limited set torque (MSLB), which is computed by a torque limiter from the set torque (MSL), including converting the actual system output (PAIST) to an actual system torque (MAIST), computing a quotient (Q(i)) from the actual system torque (MAIST) and the limited set torque (MSLB), and determining the correction factor (k) from the quotient (Q(i)) using an I controller.
2. The method in accordance with claim 1 , including computing a mean value (MW) from the quotients (Q(i), i=1, 2, 3, . . . ) within a computation interval, and determining the correction factor (k) with the I controller based on the mean value (MW).
3. The method in accordance with claim 2 , including limiting the correction factor (k).
4. The method in accordance with claim 1 , wherein, in a steady-state operating condition, the correction factor (k) is set as the current value for the correction of the set volume flow (VSL), and in a non-steady-state operating condition, the last correction factor (k) determined during a steady-state operating condition is kept as the current value for the correction of the set volume flow (VSL).