Thomas S. Snyder - Oakmont PA Richard A. Stoltz - Plano TX
Assignee:
Westinghouse Electric Corp. - Pittsburgh PA
International Classification:
B01D 1508
US Classification:
210656
Abstract:
Scandium and yttrium present in sand is recovered from the residue pulled from sand chlorinators. The residue is digested with an acid to produce a liquid containing scandium, yttrium, sodium, calcium and at least one radioactive metal of the group consisting of radium, thorium and uranium. The metal-containing liquid is then fed through a cation exchanger. The cation exchanger is eluted with an acid to produce eluate functions containing at least partially separated metals. A first eluate fraction contains at least half of the calcium and the sodium, a second eluate fraction contains at least half of the radioactive metals, a third eluate fraction contains at least half of the scandium and a fourth eluate fraction contains at least half of the yttrium which were contained in the metal-containing feed.
Electrochemical Decomposition Of Complexes Of Zirconium Or Hafnium
Thomas S. Snyder - Oakmont PA Richard A. Stoltz - Murrysville PA David F. McLaughlin - Oakmont PA
Assignee:
Westinghouse Electric Corp. - Pittsburgh PA
International Classification:
B01D 300 C01G 2504 C01G 2704 C22B 3414
US Classification:
203 29
Abstract:
This is an improved method for separating hafnium from zirconium of the type where a complex of zirconium and hafnium chlorides and phosphorus oxychloride is prepared from zirconium-hafnium chloride and the complex is introduced into a distillation column, with the improvement comprising: electrochemical breaking of the zirconium of hafnium chloride complex taken from said distillation column to separate product from the complex. The electrochemical breaking of the complex, possibly by reducing zirconium or hafnium, is done in a molten salt bath. Preferably, the molten salt in said molten salt bath consists principally of a mixture of alkali metal and alkaline earth metal chlorides and zirconium or hafnium chloride. The product can be either chloride, metal, or mixed metal and subchloride for further processing.
Electrochemical Process For Zirconium Alloy Recycling
Thomas S. Snyder - Oakmont PA Richard A. Stoltz - Murrysville PA David Zuckerbrod - Pittsburgh PA
Assignee:
Westinghouse Electric Corp. - Pittsburgh PA
International Classification:
C25F 500
US Classification:
204140
Abstract:
A major cost component for zirconium alloy manufacture and fabrication is metal scrap generation during fabrication. This scrap, which has already incurred the entire process conversion cost from zircon sand to metal refining, constitutes an expensive cost to the fabrication process. The present invention teaches that these alloy scraps may be separated into their components by molten salt electrolysis using FLINAK electrolyte. The alloy components are recycled directly to the alloying process as cathodic grade metals, saving the cost of completely repeating the zircon conversion process.
Integrated Production Of Superconductor Insulation For Chemical Vapor Deposition Of Nickel Carbonyl
Thomas S. Snyder - Oakmont PA Richard A. Stoltz - Murrysville PA George R. Wagner - Murrysville PA
Assignee:
Westinghouse Electric Corp. - Pittsburgh PA
International Classification:
C23C 812 C23C 880 C23C 1616
US Classification:
505 1
Abstract:
This is a process for fabrication of nickel-oxide insulation on a superconductor. The process utilizes; reacting oxygen-free nickel powder with oxygen-free carbon monoxide generally at 50. degree. -75. degree. C. to produce a nickel carbonyl, separating the nickel carbonyl from reaction by-products and excess reagents by cooling the carbonyl and decanting the nickel carbonyl liquor, and contacting the carbonyl to a surface of a wire containing superconductor or superconductor precursors in an atmosphere containing a controlled amount of oxygen, with the wire at 50. degree. -800. degree. C. to produce nickel suboxide insulation on the wire. The purified nickel carbonyl and oxygen may be alternately (rather than simultaneously) introduced, to deposit a series of metallic nickel films on the wire, each of which metallic films are then oxidized to a nickel suboxide. The superconductor may be a niobium-tin superconductor, and the carbonyl contacted to wire containing unreacted niobium and tin at a wire temperature between 50. degree. -500. degree. C. to coat the wire with the nickel suboxide, and final forming of the wire done after the coating of wire and the niobium and the tin are reaction annealed after the final forming of the wire.
Zirconium And Hafnium Tetrachloride Separation By Extractive Distillation With Molten Zinc Chloride Lead Chloride Solvent
David F. McLaughlin - Oakmont PA Richard A. Stoltz - Murrysville PA
Assignee:
Westinghouse Electric Corp. - Pittsburgh PA
International Classification:
B01D 340 C01G 2504 C01G 2704
US Classification:
203 51
Abstract:
This is a molten salt extractive distillation process for separating hafnium from zirconium. It utilizes at least principally a ZnCl. sub. 2 -PbCl. sub. 2 molten salt solvent, and preferably ZnCl. sub. 2 -PbCl. sub. 2 in a near eutectic or eutectic mixture. The extraction column is preferably run about 370. degree. -390. degree. C. at about one atomosphere and stripping is preferably done at 375. degree. -400. degree. C. utilizing an inert gas carrier.
Preparation Of Complexes Of Zirconium And Hafnium Tetrachlorides With Phosphorus Oxychloride
Thomas S. Snyder - Oakmont PA Richard A. Stoltz - Murrysville PA
Assignee:
Westinghouse Electric Corp. - Pittsburgh PA
International Classification:
B01D 332 C01G 2504 C01G 2704
US Classification:
203 29
Abstract:
This is a method for molten salt systems related to distillation for zirconium-hafnium separation and prevents buildup of iron chloride by electrochemically reducing iron from the molten salt to give very low levels of iron chloride in the distillation column, to reduce corrosion, improve the product and, in some cases, to allow the molten salt system to be run continuously. The improvement comprises electrochemical purification of molten salt containing zirconium-hafnium chloride either, prior to introduction of the zirconium-hafnium chloride into a distillation column, or after introduction, or both, to substantially eliminate iron chloride from the zirconium-hafnium chloride. The molten salt during the electrochemical purification consists essentially of a mixture of chlorides of alkali metals, alkaline earth metals, zirconium, hafnium, aluminum, manganese, and/or zinc.
Method For Determining The Position And Inclination Of A Flame Front During In Situ Combustion Of A Rubbled Oil Shale Retort
Richard A. Stoltz - Murrysville PA Albert C. Metrailer - Broken Arrow OK
Assignee:
Standard Oil Company (Indiana) - Chicago IL
International Classification:
E21B 4324 E21B 4712
US Classification:
166251
Abstract:
A passive method for locating the position and inclination of a flame front, within an oil-shale retort of known dimensions and location during an in situ combustion of the retort involving detecting the sound generated by the flame front, by two matched detectors separated by a fixed known distance. The pair of matched detectors are suspended vertically in a liquid-filled well which was drilled essentially parallel to the side wall of the retort. The outputs of the two detectors are fed directly to a differential amplifier and the resulting difference signal is monitored as a function of depth as the pair of detectors are raised and/or lowered in the well. The minimum in this signal corresponds to the position of the flame front within the retort. Repeated measurements in various observation wells establish the inclination of the flame front.
Method Of Purifying Zirconium Tetrachloride And Hafnium Tetrachloride In A Vapor Stream
Thomas S. Snyder - Oakmont PA Richard A. Stoltz - Plano TX
Assignee:
Westinghouse Electric Corp. - Pittsburgh PA
International Classification:
C01B 3308 C01G 2504 C01G 2704 B01D 3900
US Classification:
423240S
Abstract:
A vapor stream from a sand chlorinator containing principally zirconium tetrachloride, hafnium tetrachloride and silicon tetrachloride contaminated with ferric chloride is purified by cooling the vapor to a temperature of about 335. degree. C. to about 600. degree. C. The cooled vapors flow through a gaseous diffusion separative barrier where a silicon tetrachloride vapor stream contaminated with metal chlorides flows from the separative barrier as a "fast" stream; ferric chloride is adsorbed by the separative barrier; and a vapor stream principally containing zirconium tetrachloride, hafnium tetrachloride and silicon tetrachloride is screened by the separative barrier.
Results 1 - 79 Are you looking for Richard Stoltz? MyLife is happy to assist you on the quest as we dedicate our efforts to streamline to process of finding long-lost ...
Joseph Steinbach, Robert Pavek, Richard Puariea, Carol Stevens, Karen Hjelle, Merry Thompson, Darryl Same, Patricia Patricia, Kathleen Daniels, Thomas Cherney, Dennis Larsen
Richard Stoltz (1985-1989), Melissa Mraz (1981-1985), Dan Olas (1974-1982), Matt Orzech (1976-1984), Kevin Gaffey (1980-1987), David Pompey (1975-1979)