METHOD OF CONTROLLING AN AIR COMPRESSOR OF A VEHICLE
20230356699 · 2023-11-09
Inventors
Cpc classification
F04B2205/11
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B35/04
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B2205/50
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B49/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B60S5/00
PERFORMING OPERATIONS; TRANSPORTING
F04B39/16
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B49/065
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F04B2205/09
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
Abstract
A method of controlling an air compressor of a vehicle. The absolute humidity is determined for atmospheric air entering the compressor as well as for the compressed air exiting the compressor. A liquid water mass formed or evaporated inside the compressor during a defined period of time is calculated. The above steps are repeated in order to calculate a cumulated liquid water mass inside the compressor. The compressor is stopped when the calculated cumulated liquid water mass has returned to zero and the control unit no longer receives a compressed air request.
Claims
1. A method of controlling an air compressor of a vehicle, comprising: starting the compressor, at the time of starting the compressor: determining, for the atmospheric air entering the compressor, a value H.sub.abs,atm of the absolute humidity, and determining, for the compressed air exiting the compressor, a value H.sub.abs,comp of the absolute humidity, based on the determined values H.sub.abs,atm and H.sub.abs,comp, calculating by means of a control unit a liquid water mass formed or evaporated inside the compressor during a defined period of time, repeatedly performing the determining steps and the calculating step, for each repetition, calculating by means of the control unit a cumulated liquid water mass inside the compressor, and stopping the compressor when the calculated cumulated liquid water mass has returned to zero and the control unit no longer receives a compressed air request.
2. The method of claim 1, wherein the formation or evaporation of liquid water mass is calculated for a series of consecutive periods of time, wherein the start of a next period of time in the series coincides with the end of the previous period of time in the series, wherein the cumulated liquid water mass inside the compressor is calculated by summarizing the calculation for the series of consecutive periods of time.
3. The method of claim 1, comprising storing the most recently calculated value of the cumulated liquid water mass in an electronic memory.
4. The method of claim 3, further comprising, when the vehicle is turned on after having been turned off: restarting the compressor, repeatedly performing the determining steps and the calculating steps, for each repetition, calculating the cumulated liquid water mass inside the compressor and updating the stored value in the electronic memory with a new calculated value of the cumulated liquid water mass, and stopping the compressor when the new calculated value of the cumulated liquid water mass is zero.
5. The method of claim 1, wherein the step of calculating a liquid water mass formed or evaporated inside the compressor for a defined period of time comprises determining the flow rate through the compressor for the defined period of time, wherein the formed or evaporated liquid water mass is calculated based on the determined flow rate during the defined period of time.
6. The method of claim 5, wherein the liquid water mass formed or evaporated in the compressor for the defined period of time is calculated using the formula:
7. The method of claim 6, wherein the cumulated liquid water mass at time t.sub.n is calculated using the formula:
M.sub.c,t.sub.
8. The method of claim 5, wherein the step of determining the flow rate comprises measuring the compressor speed and determining the flow rate based on the measured compressor speed.
9. The method of claim 1, wherein the step of determining the value H.sub.abs,atm of the absolute humidity for the atmospheric air entering the compressor comprises: measuring the relative humidity of the atmospheric air with a humidity sensor, measuring the temperature of the atmospheric air with a first temperature sensor, and determining the value H.sub.abs,atm based on the measured relative humidity and measured temperature of the atmospheric air.
10. The method of claim 1, wherein the step of determining the value H.sub.abs,comp of the absolute humidity for the compressed air exiting the compressor comprises: measuring the temperature of the atmospheric air with a first temperature sensor, determining the atmospheric pressure, such as by measuring the pressure of the atmospheric air with a first pressure sensor or estimating the pressure from the vehicle altitude or estimating the pressure to be 1.013 bar, determining the pressure of the compressed air, such as by measuring the pressure of the compressed air with a second pressure sensor or fixed parameter depending on system pressure, measuring the relative humidity of the atmospheric air with a humidity sensor, measuring the temperature of the compressed air with a second temperature sensor, and determining the value H.sub.abs,comp based on the measured temperature of the atmospheric air, the determined atmospheric pressure, the determined pressure of the compressed air, the measured relative humidity and measured temperature of the compressed air.
11. The method of claim 10, wherein the second temperature sensor is placed in the coldest area of the compressor.
12. The method of claim 1, wherein the steps of determining the value H.sub.abs,atm further comprises: determining the vehicle's current altitude over sea level by means of a navigation system, determining the atmospheric air pressure based on the determined altitude, and determining the value Habs,comp based on the determined atmospheric air pressure.
13. The method of claim 1, further comprising: using a compressor map to select, by means of the control unit, a compressor speed for which the temperature increase gradient relative to electric power consumption is optimized, and operating the compressor at the selected compressor speed.
14. A computer program comprising program code means for performing the steps of the method of claim 1 when the program is run on a computer.
15. A computer readable medium carrying a computer program comprising program code means for performing the steps of the method of claim 1 when the program product is run on a computer.
16. A control unit for controlling an air compressor of a vehicle, the control unit being configured to perform the steps of the method of claim 1.
17. A vehicle comprising the control unit of claim 16.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0096] With reference to the appended drawings, below follows a more detailed description of embodiments of the invention cited as examples.
[0097] In the drawings:
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DETAILED DESCRIPTION
[0106] The invention will now be described more fully hereinafter with reference to the accompanying drawings, in which certain aspects of the invention are shown. The invention may, however, be embodied in many different forms and should not be construed as limited to the embodiments and aspects set forth herein; rather, the embodiments are provided by way of example so that this disclosure will be thorough and complete, and will fully convey the scope of the invention to those skilled in the art. Accordingly, it is to be understood that the present invention is not limited to the embodiments described herein 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. Like reference numerals refer to like elements throughout the description.
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[0118] Step 1 may, for instance, be initiated by a compressed air request from another part of the vehicle. For example, as illustrated in
[0119] Steps 2 and 3, i.e., determining the absolute humidity of the atmospheric air (H.sub.abs,atm) and the absolute humidity of the compressed air (H.sub.abs,comp) may be accomplished by using the following general method to calculate absolute humidity H.sub.abs [g/m.sup.3]:
[0120] 1/Coefficient
[0121] With: [0122] T=air temperature [K] [0123] Tc=critical temperature of water, Tc=647.096 K
[0124] A first temperature sensor may be used to measure the temperature of the atmospheric air, for determining/calculating the absolute humidity of the atmospheric air. A second temperature sensor provided inside the compressor may be used to measure a temperature of the compressed air, the for determining/calculating the absolute humidity of the compressed air.
[0125] 2/ Water Vapour Saturation Pressure Pws [hPa]
[0126] With: [0127] Pc=critical pressure of water, Pc=220640 hPa [0128] C1 to C6=constants known from literature
[0129] 3/ Water Vapour Partial Pressure Pw [hPa]
[0130] RH is the relative humidity of the atmospheric air. This may, for instance, be measured by means of a humidity sensor.
[0131] 4/ Absolute Humidity H.sub.abs [g/m3]
[0132] With C=2.16679 g.Math.K/J
[0133] Continuing with the method of
[0134] As the compressor is running the above determinations/calculations are repeated (step S5) and the cumulated liquid water mass is calculated in connection with each repetition (step S6). The cumulated liquid water mass may be calculated by using the below formula, which has already been discussed and explained previously in this disclosure.
M.sub.c,t.sub.
[0135] When the sum of the above formula results in zero, and the control unit (e.g., the control unit in
[0136]
[0137] In at least some exemplary embodiments, the control unit may suitably calculate the pressure dew point Tdpres when starting the compressor. This may be based on ambient air temperature, relative humidity, ambient air pressure and compressed air pressure. Furthermore, the control unit may know, or may determine, the maximum temperature, Tmax, that can be reached uniformly and steadily by the air during the compression in the compressor.
[0138] If Tmax>Tdepres, then the control unit may control the compressor according to the above control strategy.
[0139] However, if Tmax≤Tdepres, then there are two different cases, which will here be referred to as Case 1 and Case 2.
[0140] Case 1: Actual relative humidity is known from humidity sensor or other means, (the control strategy of Case 1 can also be used if worst case 100% RH is assumed).
[0141] If Tmax≤Tdepres, this means that no matter for how long time the compressor is running, the compressed air temperature will never exceed Tdpres, so there is no possibility to evaporate liquid water and condensation will occur during all the time that the compressor is running. In this case, the control unit may suitably limit the running time of the compressor to what is needed by the vehicle, and avoid any extra time, as Tdpres cannot be passed and condensation is occurring. Thus, the control unit may suitably stop the compressor when the vehicle no longer needs any more compressed air, i.e., no compress air request received. Accordingly, in this Case 1, the control unit stops the compressor even though there is liquid water, simply because not stopping the compressor would increase the accumulation of liquid water.
[0142] The control unit may store in an electronic memory the cumulated liquid water mass that was created during this running phase when Tmax≤Tdepres. The liquid water mass may then be eliminated the next time conditions allow to have compressed air temperature greater than the pressure dew point temperature, i.e., when conditions allow Tmax>Tdepres and evaporation can occur. The compressor may be restarted to evaporate liquid water either during vehicle needs or whenever the conditions (such as relative humidity, ambient temperature) are such that Tmax>Tdepres.
[0143] Case 1 is illustrated in
[0144] Case 2: Actual relative humidity is not known, and worst-case scenario is assumed, i.e., 100% RH. In this case the control unit may calculates the pressure dew point for worst case 100% RH, Tdpres_100.
[0145] If Tmax<Tdpres_100 this means that no matter for how long time the compressor is running, the air temperature will never reach the dew point Tdpres_100 and therefore there is no possibility to evaporate liquid water inside the compressor and condensation will continue as long as the compressor is running. However, this is the worst-case scenario and since the actual relative humidity (RH) is not known, the actual RH may be lower than 100%.
[0146] In this case the control unit may base the anti-condensation function on the max Tdpres that can be reached by the compressor with Tdpres_max=Tmax−ΔT (where ΔT is strictly positive, e.g., 1° C.).
[0147] From Tdpres_max and the below equations and the above equations [(7).fwdarw.(6).fwdarw.(1).fwdarw.(2).fwdarw.(3)], the control unit can calculate the RH corresponding to Tdpres_max and base the ant-condensation function on this RHmax.
[0148] 1/ Compressed Air Absolute Pressure Ppres [hPa]
P.sub.pres=P.sub.amb+P.sub.rel_pres (5)
[0149] 2/ Water Vapour Partial Pressure of Compressed Air Pwpres [hPa]
[0150] 3/ Pressure Dew Point Tdpres [° C.]
[0151] where A, m and T.sub.n are constants for calculating the dew point temperature over different temperature ranges and are listed in commercially available lookup tables.
[0152] The control unit stops the compressor when the cumulated liquid water mass (Tdepress_max; RHmax)=0 g. This allows to cover and avoid condensation in cases where the actual RH≤RHmax and actual Tdpres≤Tdpres_max.
[0153] In parallel, the control unit may calculate and keep in memory the cumulated liquid water mass (Tdpres_100; 100% RH) as well as RHmax and the date and time that this occurs. The cumulated liquid water mass (Tdpres_100; 100% RH) is incremented each time Tmax<Tdpres_100, and if it reaches a defined maximum value, the control unit can warn the driver/user with a message. The driver/user can check actual RH and reset the cumulated liquid water mass (Tdpres_100; 100% RH) if actual RH<Hmax, or drain and exchange compressor oil if actual RH>RHmax.
[0154] Case 2 is illustrated in
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[0156] Particularly, the processing circuitry 710 is configured to cause the control unit 10 to perform a set of operations, or steps, such as the method discussed in connection to
[0157] The storage medium 730 may also comprise persistent storage, which, for example may be any single one or combination of magnetic memory, optical memory, solid state memory or even remotely mounted memory.
[0158] The control unit 10 may further comprise an interface 720 for communications with at least one external device such as the compressor 2, the sensors 14 and the tank 18 discussed herein. As such, the interface 720 may comprise one or more transmitters and receivers, comprising analogue and digital components and a suitable number of ports for wireline or wireless communication.
[0159] The processing circuitry 710 controls the general operation of the control unit 10, e.g., by sending data and control signals to the interface 720 and the storage medium 730, by receiving data and reports from the interface 720, and by retrieving data and instructions form the storage medium 730. Other components, as well as the related functionality, of the control unit 10 are omitted in order not to obscure the concepts presented herein.
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