NICHOLAS JOHN LOMBARDO
Pilots at Owl Ln, Boulder, CO

License number
Colorado A1141514
Issued Date
Jul 2015
Expiration Date
Jul 2017
Category
Airmen
Type
Authorized Aircraft Instructor
Address
Address
9400 Owl Ln, Boulder, CO 80301

Personal information

See more information about NICHOLAS JOHN LOMBARDO at radaris.com
Name
Address
Phone
Nicholas Lombardo
6445 Ace Ct, Longmont, CO 80503
Nicholas Lombardo, age 71
9400 Owl Ln, Boulder, CO 80301
Nicholas Lombardo, age 81
7067 W 70Th Ave, Arvada, CO 80003
(303) 421-9604
Nicholas Lombardo
14890 Pecos St, Broomfield, CO 80023
Nicholas Lombardo
9400 Owl, Lafayette, CO 80026
(720) 890-7351
(303) 926-0103

Professional information

See more information about NICHOLAS JOHN LOMBARDO at trustoria.com
Nicholas Lombardo Photo 1
Recovery Of Alumina Values From Alunite Ore

Recovery Of Alumina Values From Alunite Ore

US Patent:
4618480, Oct 21, 1986
Filed:
Aug 15, 1984
Appl. No.:
6/641020
Inventors:
Wayne W. Hazen - Denver CO
David L. Thompson - Golden CO
James E. Reynolds - Golden CO
Nicholas J. Lombardo - Boulder CO
Paul B. Queneau - Golden CO
John P. Hager - Golden CO
Assignee:
Resource Technology Associates - Boulder CO
International Classification:
C01F 706
US Classification:
423127
Abstract:
A novel process for the recovery of alumina and potassium sulfate from alunite is provided comprising leaching the alunite with potassium hydroxide to which no sodium materials have been added, said leach solution being saturated with potassium sulfate. Aluminum values are solubilized into the leachate, and potassium and sulfur values are rendered soluble, but remain in the residue. The leachate is desilicated if necessary, preferably with lime, and aluminum trihydroxide is precipitated therefrom, followed by calcining to alumina product. The residue is leached to solubilize potassium sulfate in a secondary leach and the potassium sulfate product crystallized therefrom. Potassium hydroxide is regenerated from a portion of the potassium sulfate secondary leachate by several methods. Novel procedures for regenerating alkali metal hydroxides from the corresponding sulfates are also provided including routes involving formates and carbonates as intermediates and pyrohydrolysis.


Nicholas Lombardo Photo 2
Process For Removing Uranium And Other Metals From Wastes

Process For Removing Uranium And Other Metals From Wastes

US Patent:
5354358, Oct 11, 1994
Filed:
Aug 31, 1993
Appl. No.:
8/114670
Inventors:
John Litz - Lakewood CO
Nicholas J. Lombardo - Boulder CO
Robert L. Schwartz - Denver CO
Assignee:
IC Technologies - Wheat Ridge CO
International Classification:
C01G 4300
US Classification:
75711
Abstract:
A process for removing metals from a waste including uranium and a second metal comprising dissolving the uranium and the second metal in a first aqueous solution, removing the dissolved uranium from the first aqueous solution by redissolving in an organic solvent, stripping the uranium from the organic solvent by redissolving in a second aqueous solution, precipitating the uranium from the second aqueous solution, and removing the second metal from the first aqueous solution.


Nicholas Lombardo Photo 3
Manganese And Zinc Solvent Extraction Process

Manganese And Zinc Solvent Extraction Process

US Patent:
4423012, Dec 27, 1983
Filed:
Dec 31, 1981
Appl. No.:
6/336502
Inventors:
James E. Reynolds - Golden CO
Nicholas J. Lombardo - Boulder CO
Assignee:
Hazen Research Incorporated - Golden CO
International Classification:
C01G 900, C01G 4500
US Classification:
423 49
Abstract:
Improvement in electrowinning manganese dioxide, or zinc in which the relative concentration of manganese or zinc ions to impurities is enhanced by selectively extracting manganese or zinc ions from a bleed taken from the electrowinning feed stream with an organic extractant, while rejecting impurities, stripping the loaded organics with spent electrolyte, and recycling loaded strip to the electrowinning feed. Stripped organic may be regenerated with an alkaline agent such as calcium oxide or magnesium oxide prior to recycle, and pH may be controlled during extraction by the same means.