Oxygen concentrating method and apparatus having condensate water removing function

Patent metadata

Field	Value
Publication number	US-9675926-B2
Application number	US-201514848629-A
Country	US
Kind code	B2
Filing date	Sep 9, 2015
Priority date	Sep 9, 2015
Publication date	Jun 13, 2017
Grant date	Jun 13, 2017

Abstract

An oxygen concentrating apparatus includes: at least one adsorption bed which is filled with absorbent capable of selectively adsorbing nitrogen relative to oxygen; an air supplier which supplies pressurized air to the adsorption bed; a flow channel regulating valve unit which regulates flow channels by allowing the pressurized air to be supplied to the adsorption bed from the air supplier and by allowing the air to be discharged from the adsorption bed to be depressurized such that a nitrogen adsorption process and a nitrogen desorption process are alternately performed; and a water removing unit which separates water from the pressurized air supplied from the air supplier and removes the separated water. The flow channel regulating unit and the water removing unit are at least partially housed within a single housing.

First claim

The invention claimed is:

1. An oxygen concentrating method using an oxygen concentrating apparatus comprising a first adsorption bed and a second adsorption bed which are respectively formed to allow air supplied at lower portions thereof move upwardly and are respectively filled with absorbent capable of selectively adsorbing nitrogen relative to oxygen and performing oxygen centration by alternatively performing a pressurization process and a depressurization process of the first adsorption bed and the second adsorption bed, comprising:
performing a nitrogen adsorption in the first adsorption bed by supplying pressurized air to the first adsorption bed so as to increase pressure of the first adsorption bed and at the same time removing nitrogen from the second adsorption bed;
equalizing pressures of upper portions of the first adsorption bed and the second adsorption bed by moving air of the upper portion of the first adsorption bed to the upper portion of the second adsorption bed when pressure of the first adsorption bed becomes a predetermined pressure;
equalizing pressures of upper and lower portions of the first adsorption bed and the second adsorption bed by moving air of the upper portion of the first adsorption bed to the upper portion of the second adsorption bed and by moving air of the lower portion of the first adsorption bed to the lower portion of the second adsorption bed;
performing a nitrogen adsorption in the second adsorption bed by supplying pressurized air to the second adsorption bed so as to increase pressure of the second adsorption bed and at the same time removing nitrogen from the first adsorption bed;
equalizing pressures of upper portions of the first adsorption bed and the second adsorption bed by moving air of the upper portion of the second adsorption bed to the upper portion of the first adsorption bed when pressure of the second adsorption bed becomes a predetermined pressure;
equalizing pressures of upper and lower portions of the first adsorption bed and the second adsorption bed by moving air of the upper portion of the second adsorption bed to the upper portion of the first adsorption bed and by moving air of the lower portion of the second adsorption bed to the lower portion of the first adsorption bed; and
removing water separated from the pressurized air which will be supplied to the first adsorption bed and the second adsorption bed for a predetermined time.

2. The oxygen concentrating method of claim 1 , wherein the removing of the separated water is initiated at the starting point of the equalizing the pressure of the upper portions and is performed for the predetermined time.

3. The oxygen concentrating method of claim 1 , wherein the removing of the separated water is initiated during the supplying of the pressurized air to the first adsorption bed and the second adsorption bed and is performed for the predetermined time, and wherein the equalizing of the pressure of the upper portions is initiated after termination of the removing the separated water.

4. The oxygen concentrating method of claim 1 , wherein the predetermined time is set between 0.1 to 1 second.

5. An oxygen concentrating apparatus comprising:
at least one adsorption bed which is filled with absorbent capable of selectively adsorbing nitrogen relative to oxygen;
an air supplier which supplies pressurized air to the adsorption bed;
a flow channel regulating valve unit which regulates flow channels by allowing the pressurized air to be supplied to the adsorption bed from the air supplier and by allowing the air to be discharged from the adsorption bed to be depressurized such that a nitrogen adsorption process and a nitrogen desorption process are alternately performed; and
a water removing unit which separates water from the pressurized air supplied from the air supplier and removes the separated water,
wherein the flow channel regulating unit and the water removing unit are at least partially housed within a single housing,
wherein the water removing unit comprises a water separation tank which defines a water separation space in which water is separated from the pressurized air supplied from the air supplier,
wherein the housing comprises a first air inlet which is extruded to the outside thereof so as to supply the pressurized air of the air supplier to the water separation space, a second air inlet which is extruded to the outside thereof so as to supply the pressurized air of the air supplier to the flow channel regulating unit, and an air moving passage which is formed so as to discharge the air having passed the water separation space to the outside,
and further comprising a cover which is selectively connected to cover the second air inlet and an outlet of the air moving passage so as to selectively form an air moving space including the second air inlet and the outlet of the air moving passage.

6. The oxygen concentrating apparatus of claim 5 , wherein the water removing unit comprises a water removing regulating valve which operates to selectively remove the water which is stored in the water separation space.

7. An oxygen concentrating apparatus comprising:
at least one adsorption bed which is filled with absorbent capable of selectively adsorbing nitrogen relative to oxygen;
an air supplier which supplies pressurized air to the adsorption bed;
a flow channel regulating valve unit which regulates flow channels by allowing the pressurized air to be supplied to the adsorption bed from the air supplier and by allowing the air to be discharged from the adsorption bed to be depressurized such that a nitrogen adsorption process and a nitrogen desorption process are alternately performed; and
a water removing unit which separates water from the pressurized air supplied from the air supplier and removes the separated water,
wherein the flow channel regulating unit and the water removing unit are at least partially housed within a single housing,
wherein the at least one adsorption bed comprises a first adsorption bed and a second adsorption bed,
and further comprising:
an on/off valve which is disposed to selectively connect upper communication ports of the first adsorption bed and the second adsorption bed; and
an orifice which is disposed in a flow channel connecting the upper communication ports,
wherein the flow channel regulating valve unit selectively regulates flow channels of the air supplier, lower communication ports of the first adsorption bed and the second adsorption bed, and a nitrogen discharging passageway,
wherein the pressurized air is supplied to the first adsorption bed in a state that the on/off valve is off so that a nitrogen adsorption process is performed in the first adsorption bed,
wherein the water removing unit operates to remove water separated from the pressurized air in a state that the on/off valve is on after the nitrogen adsorption process in the first adsorption bed is terminated or while the nitrogen adsorption process in the first adsorption bed is being performed,
wherein the pressurized air is supplied to the second adsorption bed in a state that the on/off valve is off so that a nitrogen adsorption process is performed in the second adsorption bed, and
wherein the water removing unit operates to remove water separated from the pressurized air in a state that the on/off valve is on after the nitrogen adsorption process in the second adsorption bed is terminated or while the nitrogen adsorption process in the second adsorption bed is being performed.

Assignees

• Univ Sogang Res Foundation
• Oxus Co Ltd

Inventors

• Lee Tae Soo
• Kim Hyun Seong
• Han Shin Kyu
• Oh Seung Kwon
• Lee Kang Han

Classifications

• B01D53/261

  by adsorption · CPC title

• C01B13/0262 Primary

  characterised by the adsorbent · CPC title

• C01B13/027

  Zeolites · CPC title

• B01D53/047 Primary

  Pressure swing adsorption · CPC title

• B01D2257/40

  Nitrogen compounds · CPC title