Blower purge dryer with cooling apparatus and methodology

Patent metadata

Field	Value
Publication number	US-2016288048-A1
Application number	US-201615084857-A
Country	US
Kind code	A1
Filing date	Mar 30, 2016
Priority date	Apr 3, 2015
Publication date	Oct 6, 2016
Grant date	—

Abstract

A multi-tower blower purge dryer system for use with a compressed air stream provided from a compressor is disclosed. In one form the system includes two dryers that can be alternated to dry the compressed air stream. The tower used to dry the compressed air stream can be referred to as the drying tower, and the tower being regenerated can be referred to as the regenerated tower. A number of valves and passages are used to connect the towers to one another and/or to an intake passage from the compressor. A blower purge heater is provided to regenerate the dryers. After a regeneration step in which a tower may be relatively warm, the valves can be actuated to place the warm regenerated tower in fluid communication with the intake passage from the compressor, which can then provide air to the drying tower. In this manner the regenerated tower is cooled.

First claim

1 . An apparatus comprising:
a multi-tower regenerative dryer system having a first drying tower and a second drying tower and structured to remove moisture from a compressed air stream provided through an intake passage from a compressor; a controller configured to selectively place the first drying tower, second drying tower, and intake passage in fluid communication with each other during a regeneration cycle to conduct a cooling flow period in response to a signal associated with a temperature of the first drying tower, the controller structured to configure the multi-tower regenerative dryer system to:
route the compressed air stream from the intake passage to the first drying tower to cool down a drying element of the first drying tower as a result of the drying element having been heated during regeneration thereby creating a first tower outlet air stream; and
convey the first tower outlet air stream from the first drying tower to the second drying tower to absorb moisture in the first tower outlet air stream that has traversed from the intake passage to the first drying tower and then to the second drying tower.

2 . The apparatus of claim 1 , which further includes a cooler situated in fluid communication between the first drying tower and the second drying tower and structured to cool the first tower outlet air stream prior to being received by the second drying tower.

3 . The apparatus of claim 2 , which further includes a purge blower in selective fluid communication with the first drying tower, and a heater structured to heat a stream of air that flows through action of the purge blower such that heated air can be provided to the first drying tower when the purge blower is placed in fluid communication with the first drying tower.

4 . The apparatus of claim 3 , which further includes a pre-heater structured to heat the stream of air provided from action of the purge blower prior to the stream of air being heated by the heater.

5 . The apparatus of claim 3 , which further includes a valve system having a plurality of valves actuatable from the controller and configured to place the first drying tower in selective fluid communication with the intake passage and the first drying tower in selective communication with the purge blower.

6 . The apparatus of claim 5 , wherein the controller is further structured to configure the multi-tower regenerative dryer system to maintain the heater in an off condition while the purge blower provides air to the first drying tower during a preliminary cool down event, wherein the valve system isolates the first drying tower from the intake passage, and wherein the valve system permits discharge of the air provided from the purge blower from the first drying tower.

7 . The apparatus of claim 1 , wherein the controller is further structured to configure the multi-tower regenerative dryer system to:
route the compressed air stream from the intake passage to the second drying tower to cool down a drying element of the second drying tower as a result of the drying element having been heated during regeneration thereby creating a second tower outlet air stream; and convey the second tower outlet air stream from the second drying tower to the first drying tower to absorb moisture in the second tower outlet air stream that has traversed from the intake passage to the second drying tower and then to the first drying tower.

8 . An apparatus comprising:
a twin tower heated purge blower dryer system having an intake conduit structured to receive compressed air from a compressor, a first drying tower with drying element, a second drying tower with drying element, a purge blower heater structured to provide heat to the first drying tower and second drying tower, an actuatable valve network structured to selectively open and close a plurality of fluid pathways; and a controller structured to:
de-energize the purge blower heater after a heating event of the first drying tower used to dry the tower; and
command a plurality of valves of a valve network to initiate a cooling event to reduce temperature of the first drying tower, the valve network configured as a result of the command to place the intake conduit in serial communication with the first drying tower and second drying tower, where the first drying tower is fluidically between the intake conduit and the second drying tower.

9 . The apparatus of claim 8 , wherein the controller is further structured to command the plurality of valves in the valve network to initiate operation in which the second drying tower is fluidically isolated from the intake conduit, the first drying tower is in fluid communication with the intake conduit to dry the compressed air, and the second drying tower is in fluid communication with the purge blower heater to regenerate the second drying tower, wherein the purge blower heater is energized such that heated air is conveyed from the purge blower heater to the second drying tower.

10 . The apparatus of claim 9 , wherein the controller is further structured to:
de-energize the purge blower heater after a heating event of the second drying tower used to dry the tower; and command the plurality of valves of the valve network to initiate a cooling event to reduce temperature of the second drying tower, the valve network configured as a result of the command to place the intake conduit in serial communication with the second drying tower and first drying tower, where the second drying tower is fluidically between the intake conduit and the first drying tower.

11 . The apparatus of claim 10 , wherein the controller is further structured to provide purge air from the purge blower heater in which a heater of the purge blower heater is not activated such that relatively cool air is provided from the purge blower heater, the relatively cool air from the purge blower heater routed to the first drying tower after the purge blower heater has provided heated air to the first drying tower and before the first drying tower is placed in fluidic communication between the intake conduit and the second drying tower to cool the first drying tower.

12 . The apparatus of claim 8 , which further includes a cooler disposed between the first drying tower and the second drying tower and structured to cool a fluid flowing from the first drying tower to the second drying tower when the plurality of valves of the valve network are configured to place the first drying tower fluidically between the intake conduit and the second drying tower.

13 . The apparatus of claim 12 , wherein the controller is further configured to command the plurality of valves to close off flow paths and thereby cease flow from the first drying tower to the second drying tower as a result of a cool down of the first drying tower.

14 . The apparatus of claim 12 , which further includes a moisture separator downstream of the cooler and upstream of the second drying tower.

15 . A method comprising:
upon completion of a regenerative heating process, ceasing a heating of a first dryer of a multi-tower compressed air dryer; while the heating of the first dryer is ceased, routing compressed air from an intake conduit to the first dryer to cool the first dryer during a cooling process; and during the cooling process and after the routing, conveying the compressed air from the first dryer to a second dryer of the multi-tower compressed air dryer.

16 . The method of claim 15 , which further includes cooling the compressed air when it is being conveyed from the first dryer to the second dryer.

17 . The method of

Assignees

• Ingersoll-Rand Company

Inventors

• Mark Henry Y
• Jakop Janez

Classifications

• B01D53/30

  Controlling by gas-analysis apparatus (regulating non electrical variables in general G05D) · CPC title

• B01D53/0454

  Controlling adsorption (controlling temperature swing adsorption B01D53/0462, controlling pressure swing adsorption B01D53/047) · CPC title

• B01D53/261 Primary

  by adsorption · CPC title

• B01D53/0438

  Cooling or heating systems · CPC title

• B01D2257/80

  Water · CPC title