Adsorption type air dryer and method of controlling the same

Patent metadata

Field	Value
Publication number	US-2024316493-A1
Application number	US-202418611133-A
Country	US
Kind code	A1
Filing date	Mar 20, 2024
Priority date	Mar 24, 2023
Publication date	Sep 26, 2024
Grant date	—

Abstract

An air dryer includes a first adsorption tower configured to perform any one of a compressed air dehumidification process and a regeneration process of a first adsorbent provided therein, a second adsorption tower configured to perform a regeneration process of a second adsorbent or alternately perform a compressed air dehumidification process, in response to an operation of the first adsorption tower, and a controller configured to (i) control the operation of the first adsorption tower for the first adsorption tower to perform either the compressed air dehumidification process or the regeneration process of the first adsorbent and (ii) control the operation of the second adsorption tower for the second adsorption tower to perform either the compressed air dehumidification process or the regeneration process of the second adsorbent.

First claim

What is claimed is:

1 . An air dryer comprising:
a first adsorption tower configured to perform any one of a compressed air dehumidification process and a regeneration process of a first adsorbent provided therein; a second adsorption tower configured to perform a regeneration process of a second adsorbent or alternately perform a compressed air dehumidification process, in response to an operation of the first adsorption tower; and a controller configured to: (i) control the operation of the first adsorption tower for the first adsorption tower to perform either the compressed air dehumidification process or the regeneration process of the first adsorbent; and (ii) control the operation of the second adsorption tower for the second adsorption tower to perform either the compressed air dehumidification process or the regeneration process of the second adsorbent, wherein the controller is configured to control at least one of the first adsorption tower and the second adsorption tower by using: a first moisture load rate, which is a ratio of a pre-set moisture removal amount with respect to a first accumulated moisture removal amount accumulated in the first adsorption tower; and a second moisture load rate, which is a ratio of the pre-set moisture removal amount with respect to a second accumulated moisture removal amount accumulated in the second adsorption tower.

2 . The air dryer of claim 1 , wherein, based on determining that the first moisture load rate exceeds a pre-set moisture load rate upper limit, the controller is configured to stop the compressed air dehumidification process of the first adsorption tower and switch to the compressed air dehumidification process of the second adsorption tower, and,
wherein based on determining that the second moisture load rate exceeds the pre-set moisture load rate upper limit, the controller is configured to stop the compressed air dehumidification process of the second adsorption tower and switch to the compressed air dehumidification process of the first adsorption tower.

3 . The air dryer of claim 1 , wherein, based on determining that the first moisture load rate or the second moisture load rate exceeds a pre-set moisture load rate upper limit, the controller is configured to reduce a time for the compressed air dehumidification process.

4 . The air dryer of claim 1 , wherein, based on determining that the first moisture load rate or the second moisture load rate is less than a pre-set moisture load rate lower limit, the controller is configured to extend a time for the compressed air dehumidification process.

5 . The air dryer of claim 1 , wherein the controller is configured to calculate the first accumulated moisture removal amount or the second accumulated moisture removal amount accumulated inside the first adsorption tower or the second adsorption tower, respectively, in real time.

6 . The air dryer of claim 1 , wherein the pre-set moisture removal amount is calculated by using a pre-set temperature, a pre-set flow rate, a pre-set relative humidity, and a pre-set pressure of compressed air passing through an inlet and an outlet of the air dryer.

7 . The air dryer of claim 1 , wherein the first accumulated moisture removal amount and the second accumulated moisture removal amount are calculated by using a temperature, a flow rate, and a pressure of compressed air passing through the inlet of the air dryer.

8 . A method of controlling an air dryer using a first adsorption tower and a second adsorption tower, the method comprising:
inputting a pre-set moisture removal amount of the air dryer; controlling operations of the first adsorption tower and the second adsorption tower, such that the first adsorption tower and the second adsorption tower perform any one of a compressed air dehumidification process or an adsorbent regeneration process; calculating a first accumulated moisture removal amount accumulated in the first adsorption tower or a second accumulated moisture removal amount accumulated in the second adsorption tower; and calculating a first moisture load rate, which is a ratio of the pre-set moisture removal amount with respect to the first accumulated moisture removal amount, or a second moisture load rate, which is a ratio of the pre-set moisture removal amount with respect to the second accumulated moisture removal amount, wherein, in the controlling of the operations of the first adsorption tower and the second adsorption tower, the compressed air dehumidification process of the first adsorption tower or the second adsorption tower is controlled based on the first moisture load rate or the second moisture load rate, respectively.

9 . The method of claim 8 , wherein, in the inputting of the pre-set moisture removal amount, the pre-set moisture removal amount is calculated by using a pre-set temperature, a pre-set flow rate, a pre-set relative humidity, and a pre-set pressure of compressed air passing through an inlet and an outlet of the air dryer.

10 . The method of claim 8 , wherein the controlling of the operation of the first adsorption tower and the second adsorption tower further comprises determining whether the first adsorption tower or the second adsorption tower is operating.

11 . The method of claim 8 , wherein, in the controlling of the operation of the first adsorption tower and the second adsorption tower, the first adsorption tower and the second adsorption tower are controlled to alternately perform the adsorbent regeneration process or the compressed air dehumidification process in correspondence with each other.

12 . The method of claim 8 , wherein, in the calculating of the first accumulated moisture removal amount and the second accumulated moisture removal amount, a moisture removal amount accumulated inside the first adsorption tower or the second adsorption tower is calculated in real time.

13 . The method of claim 8 , wherein, in the calculating of the first accumulated moisture removal amount and the second accumulated moisture removal amount, the first accumulated moisture removal amount or the second accumulated moisture removal amount is calculated by using a temperature, a flow rate, and a pressure of compressed air passing through an inlet of the air dryer.

14 . The method of claim 8 , wherein the controlling of the compressed air dehumidification process of the first adsorption tower or the second adsorption tower based on the first moisture load rate or the second moisture load rate, respectively, comprises adjusting a time for the compressed air dehumidification process of the first adsorption tower and the second adsorption tower.

15 . The method of claim 14 , wherein the controlling of the compressed air dehumidification process of the first adsorption tower or the second adsorption tower based on the first moisture load rate or the second moisture load rate, respectively, further comprises comparing the first moisture load rate or the second moisture load rate with a pre-set moisture load rate upper limit and a pre-set moisture load rate lower limit.

16 . The method of claim 15 , wherein, in the controlling of the compressed air dehumidification process of the first adsorption tower or the second adsorption tower based on the first moisture load rate or the second moisture load rate, respectively,
wherein, based on determining that the first moisture load rate exceeds the pre-set moisture load rate upper limit, the compressed air dehumidification process of the first adsorption tower is stopped and is switched to the compressed air dehumidification process of the sec

Assignees

• Samsung Electronics Co Ltd

Inventors

• Ko Yujin
• Yun Hyunho
• Kang Jungsoo
• Jang Sungmin
• Jeong Hyunmin

Classifications

• B01D53/261 Primary

  by adsorption · CPC title

• B01D53/0454 Primary

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

• B01D2257/80

  Water · CPC title

• B01D2259/40088

  by heating · CPC title