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:
Jun. 25, 1996

Filed:

Feb. 06, 1995
Applicant:
Inventors:

Keith A Carlton, Glens Falls, NY (US);

Mahendra R Doshi, Appleton, WI (US);

Todd A Salvato, Columbus, IN (US);

Erwin D Funk, Queensbury, NY (US);

Joseph R Phillips, Queensbury, NY (US);

Scott M Clum, Columbus, IN (US);

Assignee:

Ahlstrom Machinery, Inc., Glens Falls, NY (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B03D / ; B04C / ; B04C / ;
U.S. Cl.
CPC ...
209170000 ; 209727 ; 209730 ; 209733 ; 2102212 ; 162-4 ;
Abstract

A slurry of recycled cellulose fibers is deinked by introducing the slurry into the first end of a vortex, sparging gas radially inwardly into the slurry to cause gas bubbles to attach to contaminants and ink particles to form an aerated slurry, discharging the aerated slurry from near the second end of the vortex into a separation vessel, effecting separation of a foam of ink laden gas bubbles from the cellulose fiber slurry in the separation vessel, and removing from the separation vessel the foam with associated ink and contaminants in a first stream, and de-inked cellulose fiber slurry in a second stream. The separation vessel is typically a foam separating vessel with separation effected by flotation, and by discharging the foam. The slurry is introduced into the flotation vessel below the liquid level in it. The slurry typically has a consistency of about 0.5-2%, and the gas to slurry volume ratio during sparging may be 0.1-1 to 1.0 (e.g. 0.2-0.7 to 1, or 0.3-0.4 to 1). The foam separating vessel may be cylindrical with a shower head at the top, and rejects therefrom directed to a rejects tank. Sparging takes place in a hydrocyclone with an outlet that may or may not be restricted; a rejects outlet may extend from a first end of the hydrocyclone to a rejects tank.


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