THOMAS ALEXANDER POOL
Pilots at Fillmore St, Denver, CO

License number
Colorado A1512725
Issued Date
Aug 2016
Expiration Date
Aug 2017
Category
Airmen
Type
Authorized Aircraft Instructor
Address
Address
1650 Fillmore St APT 1304, Denver, CO 80206

Professional information

Thomas Pool Photo 1

Extraction Of Uranium From Wet-Process Phosphoric Acid

US Patent:
2013002, Jan 24, 2013
Filed:
Jul 23, 2012
Appl. No.:
13/555469
Inventors:
Nicholas Warwick Bristow - Wilson WA, AU
Mark S. Chalmers - Littlehampton, AU
James Andrew Davidson - Wattyl Park, AU
Bryn Llywelyn Jones - Oakbank, AU
Paul Robert Kucera - Valrico FL, US
Nick Lynn - Englewood CO, US
Peter Douglas Macintosh - Peppermint Grove, AU
Jessica Mary Page - North Adelaide, AU
Thomas Charles Pool - Golden CO, US
Marcus Worsley Richardson - Goodwood, AU
Karin Helene Soldenhoff - Earlwood, AU
Kelvin John Taylor - West Leederville, AU
Colin Wayrauch - Brandon FL, US
International Classification:
C22B 60/02
US Classification:
423 7, 423 3, 423 15, 423 8
Abstract:
A process for the extraction of uranium compounds from wet-process phosphoric acid includes lowering the iron concentration of the wet-process phosphoric acid and reducing the valency of any remaining ferric iron in the wet-process phosphoric acid to ferrous iron, and then extracting uranium compounds from the wet-process phosphoric acid. The process can include separating a side stream from a feed stream of wet-process phosphoric acid, wherein the side stream has a greater concentration of the uranium compounds than the feed stream by filtration. Extracting uranium compounds from the wet-process phosphoric acid can be by ion exchange process or by solvent extraction.


Thomas Pool Photo 2

Extraction Of Uranium From Wet-Process Phosphoric Acid

US Patent:
2010002, Feb 4, 2010
Filed:
Jul 28, 2009
Appl. No.:
12/510294
Inventors:
Nicholas Warwick Bristow - Wilson WA, AU
Mark S. Chalmers - Littlehampton, AU
James Andrew Davidson - Wattyl Park, AU
Bryn Llywelyn Jones - Oakbank, AU
Paul Robert Kucera - Valrico FL, US
Nick Lynn - Englewood CO, US
Peter Douglas Macintosh - Peppermwt Grove, AU
Jessica Mary Page - North Adelaide, AU
Thomas Charles Pool - Golden CO, US
Marcus Worsley Richardson - Goodwood, AU
Karin Helene Soldenhoff - Earlwood, AU
Kelvin John Taylor - West Leederville, AU
Colin Weyrauch - Brandon FL, US
International Classification:
C01G 43/00
US Classification:
423 6, 423 3, 423 15, 423 8
Abstract:
A process for the extraction of uranium compounds from wet-process phosphoric acid includes lowering the iron concentration of the wet-process phosphoric acid and reducing the valency of any remaining ferric iron in the wet-process phosphoric acid to ferrous iron, and then extracting uranium compounds from the wet-process phosphoric acid. The process can include separating a side stream from a feed stream of wet-process phosphoric acid, wherein the side stream has a greater concentration of the uranium compounds than the feed stream by filtration. Extracting uranium compounds from the wet-process phosphoric acid can be by ion exchange process or by solvent extraction.


Thomas Pool Photo 3

Extraction Of Uranium From Wet-Process Phosphoric Acid

US Patent:
2013002, Jan 24, 2013
Filed:
Jul 23, 2012
Appl. No.:
13/555606
Inventors:
Nicholas Warwick Bristow - Wilson WA, AU
Mark S. Chalmers - Littlehampton, AU
James Andrew Davidson - Wattyl Park, AU
Bryn Llywelyn Jones - Oakbank, AU
Paul Robert Kucera - Valrico FL, US
Nick Lynn - Englewood CO, US
Peter Douglas Macintosh - Peppermint Grove, AU
Jessica Mary Page - North Adelaide, AU
Thomas Charles Pool - Golden CO, US
Marcus Worsley Richardson - Goodwood, AU
Karin Helene Soldenhoff - Earlwood, AU
Kelvin John Taylor - West Leederville, AU
Colin Wayrauch - Brandon FL, US
International Classification:
C22B 60/02
US Classification:
423 6, 423 8
Abstract:
A process for the extraction of uranium compounds from wet-process phosphoric acid includes lowering the iron concentration of the wet-process phosphoric acid and reducing the valency of any remaining ferric iron in the wet-process phosphoric acid to ferrous iron, and then extracting uranium compounds from the wet-process phosphoric acid. The process can include separating a side stream from a feed stream of wet-process phosphoric acid, wherein the side stream has a greater concentration of the uranium compounds than the feed stream by filtration. Extracting uranium compounds from the wet-process phosphoric acid can be by ion exchange process or by solvent extraction.