U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Oxygen concentration system and method

Patent 7771511 Issued on August 10, 2010. Estimated Expiration Date: Icon_subject December 8, 2026. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

Pressure swing adsorption system using product gas as replacement for purge gas
Patent #: 4475930
Issued on: 10/09/1984
Inventor: Asztalos

Method and apparatus for concentrating oxygen
Patent #: 4502873
Issued on: 03/05/1985
Inventor: Mottram ,   et al.

Oxygen concentrator and test apparatus
Patent #: 4627860
Issued on: 12/09/1986
Inventor: Rowland

Apparatus and method for controlling output of an oxygen concentrator
Patent #: 5746806
Issued on: 05/05/1998
Inventor: Aylsworth, et al.

Oxygen concentrator
Patent #: 5858062
Issued on: 01/12/1999
Inventor: McCulloh, et al.

Closed-loop feedback control for oxygen concentrator
Patent #: 5906672
Issued on: 05/25/1999
Inventor: Michaels, et al.

Gas concentration sensor and control for oxygen concentrator utilizing gas concentration sensor
Patent #: 5917135
Issued on: 06/29/1999
Inventor: Michaels, et al.

Molecular sieve type gas separation apparatus
Patent #: 6383256
Issued on: 05/07/2002
Inventor: Phillips

Method of controlling a gas adsorption apparatus Patent #: 7087101
Issued on: 08/08/2006
Inventor: Murley, et al.

Inventor

Assignee

Application

No. 11636233 filed on 12/08/2006

US Classes:

95/96Plural pressure varying steps (e.g., pressure swing adsorption, etc.)

Examiners

Primary: Hopkins, Robert A

Attorney, Agent or Firm

Foreign Patent References

  • 05277322 JP 10/01/1993

International Class

B01D 53/02

Abstract

The present system is an adsorption system for separating air into a concentrated gas component, which has an air supply, a compressor for receiving and compressing the air supply, providing a compressed air supply, and molecular sieve material for separating the compressed air supply into a concentrated gas component. The adsorption system delivers at least 5 liters per minute (LPM) of concentrated gas component from the molecular sieve material in which the system has a specific total weight per LPM <9 lbs/LPM. Additionally, an output quantity of the concentrated gas is delivered by the adsorption system and a purging quantity of the concentrated gas is dispensed into a sieve chamber of the adsorption system undergoing a purge cycle. The purging quantity has a value equal to or less than the difference between the maximum quantity and the output quantity, and the purging quantity is controlled based on the output quantity.

Other References

  • PCT Search Report and Written Opinon, Jan. 25, 2008.
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