Compressor aftercooler bypass with integral water separator
US-9283944-B2 · Mar 15, 2016 · US
US9475476B1 · US · B1
| Field | Value |
|---|---|
| Publication number | US-9475476-B1 |
| Application number | US-201514865902-A |
| Country | US |
| Kind code | B1 |
| Filing date | Sep 25, 2015 |
| Priority date | Sep 25, 2015 |
| Publication date | Oct 25, 2016 |
| Grant date | Oct 25, 2016 |
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A system for variably controlling the purge cycle of a locomotive air supply system air dryer pre-filtration state. A sensor in the air inlet of the air dryer provides temperature information to a controller, which calculates an appropriate purge cycle time based on the saturation partial pressure of water vapor at the actual temperature of the air entering the air dryer and the operates the drain valve according to the particular purse cycle time.
Opening claim text (preview).
What is claimed is: 1. A control system for a drain valve of a pre-filtration stage in a locomotive air supply system, comprising: a sensor for positioning in proximity to an inlet of an air dryer that is configured to output a signal corresponding to the actual temperature of an air stream in the inlet; a pre-filtration stage having a drain valve that is opened and closed according to a purge cycle time; and a controller interconnected to the temperature sensor and drain valve that is programmed to calculate the purge cycle time based on the saturation partial pressure of water vapor at the actual temperature indicated by the signal received from the temperature sensor and to operate the drain valve according to the calculated purge cycle time. 2. The system of claim 1 , wherein the controller is programmed to calculate the purge cycle time based on the saturation partial pressure of water vapor at the actual temperature by adjusting a predetermined cycle time according to the relationship between a reference saturation partial pressure and the saturation partial pressure of water vapor at the actual temperature. 3. The system of claim 2 , wherein the controller is programmed to adjust the predetermined cycle time according to the relationship between a reference saturation partial pressure and the saturation partial pressure of water vapor at the actual temperature if the actual temperature is above a predetermined minimum temperature and below a predetermined maximum temperature. 4. The system of claim 3 , wherein the controller is programmed to adjust the predetermined cycle time according to the relationship between a reference saturation partial pressure and the saturation partial pressure of water vapor at the predetermined minimum temperature if the actual temperature is below the predetermined minimum temperature. 5. The system of claim 4 , wherein the controller is programmed to set the purge cycle time at the predetermined minimum cycle time if the actual temperature is above the predetermined maximum temperature. 6. The system of claim 1 , wherein the controller is programmed to open the drain valve if the controller detects that an air compressor of the locomotive air supply system has been turned on. 7. The system of claim 1 , wherein the controller is programmed to open the drain valve if the controller detects that an air compressor of the locomotive air supply system has been turned off. 8. A method of controlling a drain valve of a pre-filtration stage in a locomotive air supply system, comprising the steps of: sensing the temperature of an air steam in an inlet of an air dryer associated with the pre-filtration stage; calculating a purge cycle time based on the saturation partial pressure of water vapor at the actual temperature of the air stream in the inlet of the air dryer; operating the drain valve according to the calculated purge cycle time. 9. The method of claim 8 , wherein the step of calculating the purge cycle time based on the saturation partial pressure of water vapor at the actual temperature comprises adjusting a predetermined cycle time according to the relationship between a reference saturation partial pressure and the saturation partial pressure of water vapor at the actual temperature if the actual temperature is above a predetermined minimum temperature and below a predetermined maximum temperature. 10. The method of claim 9 , wherein the step of calculating the purge cycle time based on the saturation partial pressure of water vapor at the actual temperature further comprises adjusting the predetermined cycle time according to the relationship between the reference saturation partial pressure and the saturation partial pressure of water vapor at the predetermined minimum temperature if the actual temperature is below the predetermined minimum temperature. 11. The method of claim 10 , wherein the step of calculating the purge cycle time based on the saturation partial pressure of water vapor at the actual temperature further comprises setting the purge cycle time as the predetermined cycle time if the actual temperature is above the predetermined minimum temperature. 12. The method of claim 8 , further comprising the steps of: sensing whether an air compressor of the locomotive air supply system has been turned on; and opening the drain valve if the air compressor has been turned on. 13. The method of claim 8 , further comprising the steps of: sensing whether an air compressor of the locomotive air supply system has been turned off; and opening the drain valve if the air compressor has been turned off.
Draining and drying devices · CPC title
Drying gases or vapours · CPC title
for use in transportation means · CPC title
Controlling adsorption (controlling temperature swing adsorption B01D53/0462, controlling pressure swing adsorption B01D53/047) · CPC title
by adsorption · CPC title
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