Method for modeling a compressor speed
10801356 · 2020-10-13
Assignee
Inventors
Cpc classification
F02B37/18
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F01D17/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02B39/16
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F05D2270/708
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02B2039/168
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F05D2220/40
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F01D17/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F02B39/16
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
A method is provided for modeling the compressor speed of a turbocharger, and includes determining the temperature difference across the compressor, determining the mass flow through the compressor, and calculating a compressor speed value as a function of the temperature difference across the compressor and the mass flow.
Claims
1. A method for modeling the compressor speed of a turbocharger, comprising: determining the temperature difference across the compressor, determining the mass flow through the compressor, and calculating a compressor speed value as a function of the temperature difference across the compressor and the mass flow, wherein the step of calculating the compressor speed value is performed using
2. The method according to claim 1, wherein
3. The method according to claim 2, wherein the step of calculating the compressor speed value is performed by a polynomial representation of
4. The method according to claim 1, comprising: determining if a recovered exhaust gas flow is introduced downstream the compressor, and wherein the step of determining the mass flow is performed by determining the mass flow of the gas exiting the compressor and correcting the determined mass flow by a factor corresponding to recovered exhaust gas flow.
5. The method according to claim 1, wherein the step of determining the temperature difference across the compressor is performed by estimating the temperature downstream the compressor, and by subtracting the estimated temperature from a measured ambient temperature.
6. The method according to claim 5, wherein the step of estimating the temperature downstream the compressor is performed by measuring the temperature in an air inlet manifold, and correcting this temperature by a factor corresponding to the temperature loss across an associated cooler.
7. The method according to claim 1, comprising: determining the pressure ratio across the compressor, and wherein the step of calculating the compressor speed value is performed by calculating the compressor speed value as a function of the pressure ratio.
8. The method according to claim 7, wherein the step of determining the pressure ratio across the compressor is performed by: determining if the ambient pressure is below a preset ambient pressure corresponding to high altitude conditions, and if so, setting the ambient pressure as the preset ambient pressure, and dividing the boost pressure with the ambient pressure.
9. The method according to claim 8, wherein the step of calculating the compressor speed value is performed by estimating a compressor speed value using the pressure ratio as input, and calculating a corrected compressor speed value from the estimated compressor speed value and the actual ambient pressure.
10. A computer comprising a computer program for performing the steps of claim 1 when the program is run on the computer.
11. A non-transitory computer readable medium carrying a computer program for performing the steps of claim 1 when the program product is run on a computer.
12. A controller for modeling the compressor speed of a turbocharger, the controller being configured to perform the steps of the method according to claim 1.
13. A vehicle comprising a controller according to claim 12.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) With reference to the appended drawings, below follows a more detailed description of embodiments of the invention cited as examples.
(2) In the drawings:
(3)
(4)
(5)
(6)
(7)
(8)
DETAILED DESCRIPTION OF EXAMPLE EMBODIMENTS OF THE INVENTION
(9) Starting with
(10) In
(11) The internal combustion engine 100 further comprises an exhaust gas system 120, which system 120 serves the purpose of recovering at least some of the energy in the exhaust gas flow to improve the performance of the internal combustion engine 100. In the shown example the exhaust gas exits the cylinders 104 and enters an exhaust manifold 106 which is further connected to an exhaust inlet 132 of a turbocharger unit 130. The exhaust gas flow causes a turbine 134 arranged inside a turbine housing to rotate, which rotation is translated via a shaft 135 to a corresponding rotation of a compressor 136 arranged inside a compressor housing and being used to compress incoming air before it is introduced in the cylinders 104.
(12) Air is introduced to interact with the compressor 136 via an air inlet 140. Downstream the compressor 136, i.e. after the incoming air is compressed, it is guided by an air conduit 142 to an air inlet manifold 144 being connected with the cylinders 104. A cooler 146, such as a charged air cooler, may be provided in the air conduit 142.
(13) Some of the exhaust gas flow may be re-circulated to the cylinders 104 via the air conduit 142 in order to provide exhaust gas recovery. For this a bypass line 108 may at one end be connected to the exhaust gas flow path at a position between the exhaust gas manifold 106 and the exhaust gas inlet 132 of the turbocharger 130. A second end of the bypass line 108 is connected to the air conduit 142 somewhere downstream the compressor 136.
(14) A controller 200 is also provided for modeling the speed of the compressor 136. The controller 200 comprises a processor 202 and a memory 204, wherein the memory 204 contains instructions executable by the processor 202.
(15) The memory 204 may be implemented by any known memory technology, including but not limited to E(E)PROM, S(D)RAM and flash memory, and it may also include secondary storage such as a magnetic or optical disc. Physically, the memory 204 may consist of or comprise one unit or a plurality of units which together constitute the memory 204 on a logical level. In some embodiments, it may be implemented at least partly by a storage area in another component of the controller 200. The processor 202 is overall responsible for the operation of the controller 200. The processor 202 may e.g. be implemented by means of a PLC, CPU, and/or DSP capable of performing the intended functionality.
(16) The controller 200 is operative to receive a plurality of data inputs, and to model the compressor speed as a function of at least some of the data inputs. For this, a number of sensors 150a-e are provided and configured to measure various parameters of the air flowing into, and out from, the compressor 136. The sensors 150a-e are connected to the controller 200. In one embodiment, a temperature sensor 150a is arranged in the air inlet manifold 144 for providing data corresponding to the boost temperature T.sub.boost. A pressure sensor 150b may be arranged in the air inlet manifold 144 for providing data corresponding to the boost pressure P.sub.boost. A further sensor 150c may be arranged in the air conduit 142 immediately downstream the compressor 136 for providing data corresponding to the mass air flow
(17)
Additional sensors 150d-e may be provided in the air conduit 142 upstream the compressor 136 for providing data corresponding to the ambient temperature T.sub.in and the ambient pressure p.sub.amb.
(18) According to one specific aspect, the sensors 150a, 150d, and 150c are used for allowing the controller to determine the speed of the compressor 136. According to this particular aspect, as is shown in
(19) The third module 214 is preferably calculating the compressor speed value using a relationship in the form of
(20)
where N.sub.turbo is the compressor speed,
(21)
is the mass flow, {tilde over (R)} is a corrected ideal gas constant, and T.sub.boostT.sub.in is the temperature difference across the compressor. The relationship of
(22)
may preferably be calculated using
(23)
as will be further described below.
(24) Calculating the compressor speed value may be performed by forming a polynomial representation of
(25)
according to
(26)
(27) In general, the following relationship between turbo power and gas property before and after the compressor is assumed to be valid:
(28)
(29) As is evident, the mass flow relationship is much simpler than an equivalent volume velocity relationship. Hence, only the mass flow relationship is used in the modeling procedure as presented herein. The power supply needed to maintain a certain level of mass flow at a given temperature increase will also be proportional to the turbo speed, N.sub.turbo according to {dot over (W)}.sub.suppliedN.sub.turbo. Thus,
(30)
applies. The mass flow may either be measured, or calculated by applying the following equation:
.sub.gas after compressor=p.sub.boost/({tilde over (R)}.sub.gasT.sub.boost)
(31) The gas specific ideal gas law constant is calculated as {tilde over (R)}.sub.gas=R /M.sub.gas, while the molar mass of the gas is dependent on and exhaust gas recovery fraction, :
(32)
(33) The parameters, a and b, may be given by a fuel model structure. A common model of diesel which may be used is iso-octane, C.sub.8H.sub.18.
(34) The ideal mass flow may thus be calculated, for a four-stroke diesel engine of size V.sub.engine and engine speed N.sub.engine, as:
(35)
(36) In a real application, the ideal mass flow above may not be a realistic quantity. For providing a better estimation, the volumetric efficiency could also be considered. A simple model of the volumetric efficiency is
(37)
For reasons of simplicity, a decomposition of the engine speed and pressure dependency may preferably be made according to (c.sub.r: compression ratio):
(38)
(39) The engine speed dependency, g(N.sub.engine), may be semi-empirically derived (linearized).
(40) Following the conclusion derived by from the equations above, a simple assumption would be:
(41)
(42) The coefficients are preferably derived by application of a least squares criterion
(43)
The pseudo-inverse may thereafter be applied and the coefficients
(44) A good fit may be achieved for the function having the form
(45)
(46) As is realized
(47)
will not only be gas exiting the compressor, but also exhaust gas recovery (EGR). However, if the EGR fraction, (or equivalently, the EGR mass flow) is known the relationship may be formulated as
(48)
(49) The controller 200 may thus include a further module configured to determine if a recovered exhaust gas flow is introduced downstream the compressor. The module 212 for determining the mass flow may thus be configured to determine the mass flow of the gas exiting the compressor and correcting the determined mass flow by a factor corresponding to recovered exhaust gas flow.
(50) The module 210 may in some embodiments be configured to determine the temperature difference across the compressor by estimating the temperature downstream the compressor, and by subtracting the estimated temperature from a measured ambient temperature.
(51) For the controller shown in
(52)
applies.
(53) The temperature difference, T.sub.boostT.sub.in, can be used by itself. As described above, an even better approach may be to model the temperature just after the compressor. In order to do this the impact of EGR (with a given temperature T.sub.EGR and a given mass flow dm.sub.EGR/dt should be taken into account.
(54) The signal T.sub.boost can then be used to model the temperature after the charged air cooler 146 as
(55)
is either measured or estimated in the EMS. In order to retrieve the temperature of the gas leaving the compressor, T.sub.compressor, the temperature loss in the charger air cooler 146 could be accounted for. This may be done by using a map/function/model, f, that describes the temperature drop in the charger air cooler as
(56)
(57) In such case there may be yet another expression for T.sub.CAC, namely
(58)
(59) As the T.sub.CAC is already known from the calculation after the charger air cooler, it is possible to determine a unique value T.sub.compressor for a given
(60)
(61) According to another aspect a controller 200 is provided for modeling the compressor speed. The controller 200 is shown in
(62)
The fourth module 226 is configured to calculate the compressor speed value by estimating a compressor speed value using the pressure ratio as input, and a fifth module 228 is configured to calculate a corrected compressor speed value from the estimated compressor speed value and the actual ambient pressure. A sixth module 230 may be provided for communicating the modeled compressor speed communicate the modeled compressor speed to an associated unit for monitoring the current status of the turbocharger components, especially in terms of service and maintenance. The associated unit may either be arranged on-board the vehicle, or remote from the vehicle.
(63) The real measured ambient pressure p.sub.amb may consequently be used in the last step, when an estimated turbo speed N.sub.Turbo has been modeled, according to N*.sub.Turbo=p.sub.amb,measured*N.sub.Turbo. This gives extremely good model performance which can fulfil the accuracy requirements defined by either cost aspects or engine performance (removing unnecessary torque derate at high altitudes).
(64) This aspect may preferably be combined with the first mentioned aspect describing the use of the temperature difference with respect to
(65) Now turning to
(66) A suggested approach to calibrate the polynomial for the compressor speed model is given by the diagram in
(67) In
(68) In
(69) In step 410 a corrected compressor speed value is calculated from the estimated compressor speed value and the actual ambient pressure. Additional steps may be performed, e.g. in which the modeled speed value is communicated to a unit, in line what has been previously described for the controller 200. The method may perform additional steps as has been described above.
(70) The methods 300, 400 of
(71) It is to be understood that the present invention is not limited to the embodiments described above and illustrated in the drawings; rather, the skilled person will recognize that many changes and modifications may be made within the scope of the appended claims.