The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Mar. 11, 2014

Filed:

Apr. 21, 2008
Applicants:

Thomas B. Sprinkle, Rocky River, OH (US);

William J. Daniels, Wadsworth, OH (US);

Thomas A. Drobnak, Olmsted Township, OH (US);

David G. Felty, Parma, OH (US);

Valentine A. Hodos, Cleveland, OH (US);

Martin J. Fabian, Bay Village, OH (US);

Samuel J. Shelnutt, North Ridgevile, OH (US);

Jonathon R. Olszewski, Elyria, OH (US);

Inventors:

Thomas B. Sprinkle, Rocky River, OH (US);

William J. Daniels, Wadsworth, OH (US);

Thomas A. Drobnak, Olmsted Township, OH (US);

David G. Felty, Parma, OH (US);

Valentine A. Hodos, Cleveland, OH (US);

Martin J. Fabian, Bay Village, OH (US);

Samuel J. Shelnutt, North Ridgevile, OH (US);

Jonathon R. Olszewski, Elyria, OH (US);

Assignee:

Invacare Corporation, Elyria, OH (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/02 (2006.01);
U.S. Cl.
CPC ...
Abstract

Various equipment and methods associated with providing a concentrated product gas are provided. In one embodiment, the equipment includes an input device first and second sieve tanks, a variable restrictor, and a controller. In one embodiment, the method includes: a) selecting a desired output setting for the concentrated product gas from a plurality of output settings, b) separating one or more adsorbable components from a pressurized source gaseous mixture via first and second sieve tanks in alternating and opposing pressurization and purging cycles to form the concentrated product gas, and c) selectively controlling a variable restrictor based at least in part on the desired output setting to selectively provide flow between the first and second sieve tanks such that the flow for at least one output setting is different from the flow for at least one other output setting in relation to corresponding pressurization cycles.


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