JOSE LOPEZ, JR
Pharmacy at Robertson St, Brandon, FL
License number
Florida 42864
Issued Date
May 21, 2012
Effective Date
Jan 4, 2017
Expiration Date
Dec 31, 2016
Category
Health Care
Type
Registered Pharmacy Technician
Address
Address
2
427 W Robertson St, Brandon, FL 33511
5010 S Florida Ave, Lakeland, FL 33813
5010 S Florida Ave, Lakeland, FL 33813
Phone
(813) 767-5226
Professional information
Jose Quinones Lopez - Lakeland, FL
Work:
DEL MONTE COMPANY
DATA COLLECTOR URGE MOBILE - Haines City, FL
DIRECT ENROLLMETN ANALYST Direct Costumer Service
CLERK RECORD ROOM AUXILIO MUTUO HOSPITAL - San Juan, PR KMART - Caguas, PR
WAREHOUSE ASSOCIATE
DATA COLLECTOR URGE MOBILE - Haines City, FL
DIRECT ENROLLMETN ANALYST Direct Costumer Service
CLERK RECORD ROOM AUXILIO MUTUO HOSPITAL - San Juan, PR KMART - Caguas, PR
WAREHOUSE ASSOCIATE
Education:
Interamerican University
BS in Psychology International Junior College
Associates in Technology Systems
BS in Psychology International Junior College
Associates in Technology Systems
Method To Maintain A High Fe.sup.+2 /Fe.sup.+3 Ratio In The Stripping System For The Recovery Of Uranium From Wet Process Phosphoric Acid
US Patent:
4397820, Aug 9, 1983
Filed:
Jul 24, 1980
Appl. No.:
6/171699
Inventors:
Regis R. Stana - Lakeland FL
Jose G. Lopez - Lakeland FL
Jose G. Lopez - Lakeland FL
Assignee:
Wyoming Mineral Corporation - Lakewood CO
International Classification:
C01G 4300
US Classification:
423 8
Abstract:
A process to maintain a high iron +2/iron +3 concentration in the reductive stripping system for recovering uranium from wet-process phosphoric acid, comprises contacting partially oxidized strip acid, containing substantial amounts of iron +3, which had just previously stripped uranium values from an organic solvent, with elemental iron to reduce iron +3 to iron +2 and provide a Fe. sup. +2 /Fe. sup. o conversion ratio of from about 1. 5 to 3.
Humic Flotation Of Wet Process Phosphoric Acid As A Pretreatment Step In The Recovery Of Uranium
US Patent:
4402920, Sep 6, 1983
Filed:
Mar 27, 1981
Appl. No.:
6/248125
Inventors:
Jose G. Lopez - Lakeland FL
Victor J. Barnhart - Lakeland FL
Victor J. Barnhart - Lakeland FL
Assignee:
Wyoming Mineral Corporation - Lakewood CO
International Classification:
B01D 1100, C01G 5600, C01G 5700, C01B 2516
US Classification:
423 8
Abstract:
An acidic solution containing metal values and also containing humic acid impurities, is purified by: (1) forming a gas in the acid solution, (2) adding high molecular weight anionic organic flocculant in a volume ratio of gas containing acid solution: flocculant of 1,000:0. 002 to 0. 10, to form a bottom, purified, aqueous acidic phase containing metal values and a top flocculated humic acid impurities froth phase and (3) removing the humic acid froth phase.
Uranium Extraction Coefficient Control In The Process Of Uranium Extraction From Phosphoric Acid
US Patent:
4356154, Oct 26, 1982
Filed:
Jan 23, 1980
Appl. No.:
6/114465
Inventors:
Jose G. Lopez - Lakeland FL
Kenneth W. Gould - Winter Haven FL
Kenneth W. Gould - Winter Haven FL
Assignee:
Wyoming Mineral Corporation - Lakewood CO
International Classification:
C01G 4300
US Classification:
423 10
Abstract:
Controlling the uranium extraction coefficient in uranium extraction processes involving wet process phosphoric acid feed is accomplished by monitoring the oxidation potential of the raffinate acid stream exiting the extractor, and maintaining the oxidation potential of the raffinate at a value above 350 mV.
Maintaining Reductive Strip Efficiency In Uranium Recovery Processes
US Patent:
4311675, Jan 19, 1982
Filed:
Jan 23, 1980
Appl. No.:
6/114466
Inventors:
Regis R. Stana - Lakeland FL
Edward Mitchell - Pittsburgh PA
Joseph S. Rudolph - North Huntingdon PA
Jose G. Lopez - Lakeland FL
Edward Mitchell - Pittsburgh PA
Joseph S. Rudolph - North Huntingdon PA
Jose G. Lopez - Lakeland FL
Assignee:
Westinghouse Electric Corp. - Pittsburgh PA
International Classification:
B01D 1104
US Classification:
423 8
Abstract:
Wet process phosphoric acid is oxidized with nitric acid so that uranium values therein are in the +6 state. The organic extractant which contacts the acid extracts the +6 uranium and nitrate and/or nitrite ions. Urea is added to the oxidized acid to react with the nitrate and/or nitrite ions so that the organic does not extract them. The organic is reductively stripped with an aqueous solution containing ferrous ions. The efficacy of the ferrous ions is not lost through reaction with nitrate and/or nitrite ions.