Classifications

• • C—CHEMISTRY; METALLURGY
  • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
  • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
  • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
  • C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
  • C04B35/45—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on copper oxide or solid solutions thereof with other oxides
• • C—CHEMISTRY; METALLURGY
  • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
  • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
  • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
  • C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
  • C04B35/64—Burning or sintering processes
  • C04B35/65—Reaction sintering of free metal- or free silicon-containing compositions
• • H—ELECTRICITY
  • H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
  • H10N—ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
  • H10N60/00—Superconducting devices
  • H10N60/01—Manufacture or treatment
  • H10N60/0268—Manufacture or treatment of devices comprising copper oxide
  • H10N60/0296—Processes for depositing or forming copper oxide superconductor layers
  • H10N60/0548—Processes for depositing or forming copper oxide superconductor layers by deposition and subsequent treatment, e.g. oxidation of pre-deposited material
• • H—ELECTRICITY
  • H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
  • H10N—ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
  • H10N60/00—Superconducting devices
  • H10N60/01—Manufacture or treatment
  • H10N60/0268—Manufacture or treatment of devices comprising copper oxide
  • H10N60/0661—Processes performed after copper oxide formation, e.g. patterning

Definitions

• This invention relates to a method of forming films of superconducting ceramics, which involves electrodepositing a mixture of metals of the type and in
• the metal is electrodeposited in a pattern 5 to obtain a patterned superconductor after oxidation.
• a two-step method of forming a deposit e.g., 0 thin films of superconducting ceramic material
• the first step uses a modified electrodeposition technique to deposit a metal , which is then oxidized into a superconducting ceramic.
• the method of this 5 invention provides a means for forming coatings, by batch or continuous processes, on the surfaces of irregular objects including interior surfaces, wires, and patterned substrates.
• Such coatings of superconducting materials which cannot be conveniently 0 obtained by alternative technologies, are of interest for a variety of applications such as superconducting electrical lines, superconducting bearings, and superconducting wire windings for magnets, transformers, and generators.
• the present invention is believed to be 5 advantageous for the formation of superconducting devices, such as SQUID's and Josephson junctions, due to the feasibility of generating superconducting coatings in micropatterned forms.
• the electrodeposition step preferably consists of applying a reducing potential to a conductive substrate while it is in contact with an appropriate electrolyte 5 into which are also immersed a counter-electrode and, in some cases, other auxiliary electrodes. lit. particular, the electrodeposition can be conducted from an electrolyte containing salts of all of the metals in the mixture of metals to be deposited.
• Metals deposited from the electrolyte may include, but are not restricted to M - La, Y, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm,
• ⁇ f " a superconducting ceramic may be codeposited for" the purpose of imparting enhanced mechanical properties.
• Preferred metal compositions for electrochemical deposition and reaction to form the superconducting phase are those which are miscible,
• miscibility enhances the homogeneity of the superconductor product. Whether or not miscibility exists is either known or readily determined for the metal system of interest here.
• Preferred elements for imparting improved mechanical properties are metals,
• saic-fr. as silver, which do not substantially oxidize during formation of the superconductor.
• exemplary of salts that may be included in the electrolyte are: Y(N0 3 ) 3 , Ba(PFg) 2 , and Cu(0C0CH 3 ) 2 .
• the electrolyte medium containing the salts may be an aprotic liquid, i.e., a liquid containing minimal acidic protons, such as dimethylsulfoxide (DMSO) , dimethylformamide (DMF) , dimethoxyethane (DME) , tetrahydrofuran (THF) , and the like.
• aprotic liquid i.e., a liquid containing minimal acidic protons, such as dimethylsulfoxide (DMSO) , dimethylformamide (DMF) , dimethoxyethane (DME) , tetrahydrofuran (THF) , and the like.
• Such electrolyte media may contain, in addition, wetting, complexing, or other agents that impart control over composition or morphology of the deposit.
• Some water may also be included in the electrolyte solution in order to achieve in some instances the desired conductivity and solubility of the given salt. The water content would not be allowed to exceed that which would
• the potential applied to the substrate should be sufficient to reduce cations of each salt in the electrolyte to its neutral oxidation state. It should, therefore, be sufficiently cathodic (i.e., at a suitably reducting potential) to reduce the cation having the most negative reduction potential of the mixture.
• codeposition from an electrolyte containing salts of Eu, Ba, and Cu requires the application of potential h -2.89 V versus normal hydrogen electrode in order to reduce Ba(+2) to Ba(0) (standard reduction potential -2.89 V) as well as Cu(+2) to Cu(0) (+0.34 V), and Eu(+3) to Eu(0) (-2.37 V).
• Electrode substrate materials may be metallic, semiconductive, or photoconductive. They may be free standing such as conductive plates, rods, wires, fibers, and foils, or supported by structural material such as conductive thin films of metals, conductive oxides, and semiconductors coated on quartz and ceramics.
• the electrode substrates may be virtually any size, shape, and number as long as the electrolyte in contact with the surfaces to be coated is also in contact with a counter electrode.
• the electrode substrate can consist of or include a metal or metal- containing composition which reacts with the electrodeposited metal during oxidation to form the superconductor.
• a metal or metal- containing composition which reacts with the electrodeposited metal during oxidation to form the superconductor.
• a preferred example is electrodeposition of all the metals in the superconductor except for copper onto a low denier copper wire or thin copper foil.
• Oxidation of the substrate containing electrodeposited metals then yields the superconductor in wire or foil form.
• substrate electrode geometries which provide preferential crystal growth directions can be used.
• One such convenient substrate electrode geometry is obtained by grooving the electrode surface with parallel lines.
• the substrate material can also be chosen as one which will disappear via sublimation or gasification under the oxidation conditions, so as to result in a substrate-free superconductor.
• the counter electrode and other auxiliary electrodes useful in this method are electrically conductive solids such as metals, semiconductors, and photoconductors. They may be inert or electroactive under the conditions of electrodeposition. Those that are electroactive may be useful as sources to the electrolyte of cations of metals being deposited. Counter electrodes with high electrical conductivities (above 100 S/cm) are preferred in order to minimize resistive energy losses during electroplating.
• the electrodeposition of the metal mixtures may be performed in seconds to several hours, depending on the deposition current ⁇ which may range from about 10 ⁇ 3 to about 10 +3 mA/cm 2 of substrate area.
• the preferred current for deposition from aprotic liquid electrolytes is from about 10 ⁇ 2 to about 10 mA/cm .
• the film thicknesses may range from about 10 ⁇ 2 to about 10 +3 micron or more.
• the preferred film thicknesses range from about 10 "1 to about 100 microns.
• Electrodeposition of precursor metal mixtures must be conducted at temperatures wherein the electrolyte is ionically conductive. Electrodeposition in aprotic liquid electrolytes is conducted, generally, at temperatures between about -40, and about +200,C.
• the preferred temperature range for using aprotic liquid electrolytes is from about 0, to about 100,C.
• Solid polymer electrolytes are generally useful between about 60, and about 300,C, and fused salt electrolytes are generally useful between about 200, and about 500,C. Due to higher obtainable conductivities, aprotic liquid electrolytes and fused salt electrolytes are preferred over solid polymer electrolytes. Due to convenient operation near room temperature, aprotic liquid electrolytes are most preferred.
• compositions of deposited mixtures are generally dictated by deposition currents of the individual species at a given applied potential, relative salt concentrations in the electrolyte, and total salt concentration.
• applied potentials are confined to those that are sufficient to deposit all desired species but not so highly cathodic as to harm the deposit through decomposition of the electrolyte.
• Relative deposition currents of the individual species which may differ greatly for a given mixture, are, therefore, similarly restricted.
• total salt concentration is restricted by solubilities in a given electrolyte medium. Adjustments to salt concentrations in the electrolyte are, however, effective in obtaining desired deposit compositions.
• This method therefore, includes a process for establishing the dependence of deposit composition on relative salt concentrations known to those of ordinary skill in the art. For example, at an applied potential of -5V (vs Ag/Ag + ) and a total salt concentration of 0.1 M in DMSO, Y-Ba-Cu in the deposit varied according to relative cation concentrations as follows:
• the invention also relates to a superconducting film on a substrate made in accordance with the method of the invention.
• the invention has generally been discussed with respect to the yttrium or europium, barium, copper 1-2-3 composition and the bismuth, strontium, calcium, copper compositions, it is clear that this electrodeposition technique and later oxidation can be applied to other superconducting compositions such as, for example, that disclosed in copending application Serial No. 097,994, referred to as the 3-3-6, yttrium, barium, copper composition, and l 2 Ba 2 Ca 1 Cu2 ⁇ ⁇ and Tl 2 Ba 2 Ca 1 Cu 3 0 ⁇ compositions.
• Figure 1 is a comparison of the X-ray diffraction pattern (Cu k-alpha radiation) of a film deposited from a DMSO solution of Eu(N0 3 ) 3 , Ba(N0 3 ) 2 and Ca(0C0CH 3 ) after oxidation thereof (top) with the x-ray diffraction pattern of a previously established superconductor Y Ba 2 Cu 0 ⁇ and two impurity compositions (Y 2 BaCuc- , and CuO) ;
• Figure 2 is a magnetic susceptibility graph as a function of temperature of EuBa 2 Cu3 ⁇ 7+x formed by oxidation of an electrodeposited mixture of Eu, Ba and Cu;
• Figure 3 is a magnetic susceptibility graph as a function of temperature of the oxidized Bi, Sr, Ca and Cu-containing film of Example II herein;
• Figure 4 is a schematic diagram of two continuous electrochemical processes.
• metal mixtures are electrodeposited onto substrates and oxidized to form films of superconducting ceramics. More particularly, electrodeposition of appropriate metals is performed simultaneously from a single electrolyte. The oxidation is then generally performed by heating the deposited metal mixture in an oxygen-containing atmosphere.
• the principal advantage provided by this method is that a facile and versatile technique for incorporating elements into circuits, which can then be converted to a superconducting composition, is provided.
• the electrochemical technique is performed in a single step requiring neither the high temperatures necessary for metallurgical deposition of the metals nor the high vacuum required for chemical vapor or molecular beam deposition techniques.
• the selection and number of metals that may be electrodeposited is not restricted by the method, the only consideration being that it must include those metals in a ratio which can be oxidized to form a superconducting ceramic.
• the stoichioraetry and thickness of the metal deposited is controlled in accordance with conventional electrodeposition methods.
• Exemplary of metal mixtures which are formed and subsequently oxidized according to this method are mixtures of: Eu or Y, Ba, and Cu in a 1-2-3 ratio; Bi, Sr, Ca, and Cu in a 1-1-1-2 ratio; and TI, Ca, Ba, and Cu in a 1-1-1-2 ratio.
• the electrodeposition is conducted at room temperature from a liquid electrolyte comprised of salts of the metals dissolved in an aprotic solvent by applying a voltage across the substrate and counter- electrode such that the substrate is held at a constant potential of about -3 to about -6V versus a Ag/Ag+ reference electrode.
• concentrations of the salts are adjusted to account for the relative deposition rates of the different cation species.
• Y, Ba, and Cu are deposited in a ratio of 1-2-3 onto an In- Sn oxide film on a quartz substrate when a potential of about -5 V versus Ag/Ag+ is applied to the substrate immersed in a DMSO solution that is about 0.1 M in
• Y(N0 3 )3- about 0.27 M in Ba(N0 3 .2' and aboufc °- 05 M in Cu(OCOCH ) 2 .
• Bi, Sr, Ca and Cu are deposited onto a Pt substrate when a like potential is applied to the substrate immersed in a DMSO solution that is about 0.02 M in Bi(N0 3 ) 3 , about 0.1 M in
• the substrate with deposited film is removed, rinsed in fresh solvent, and dried.
• the electrodeposition process can function as a purification step to eliminate undesirable impurities in the metal salts
• this present process for forming the superconductors can utilize effectively lower impurity precursors than are possible for alternate fabrication techniques for thin film formation, such as sputtering.
• the substrate is then heated in an oxidizing atmosphere up to a temperature and time sufficient to oxidize the deposited metals into the superconducting ceramic state.
• an oxidizing atmosphere up to a temperature and time sufficient to oxidize the deposited metals into the superconducting ceramic state.
• melting and resolidification of the as-formed superconductor can be employed to provide enhanced critical currents via enhanced preferential alignment of crystallite grains in the superconductor.
• this procedure can be employed in combination with other technologies to produce patterned superconducting films.
• electrical circuits and other objects containing semiconductors, insulators, or conductor elements with superconducting paths may be formed by this method in combination with conventional lithography or in combination with photoinduced enhancement of electrodeposition.
• Such combinations can be particularly useful in forming parallel arrays of superconducting wires and dots such as those useful as high efficiency transparent shields of electromagnetic radiation.
• patterned superconductor films can arise from electrodeposition using patterned counterelectrodes.
• the procedure can be employed in a continuous manner using continuous substrates configured, for example, about a
• rotating drum or rotating belt cathode (see Fig. 4).
• photoresist is deposited (for example, by solution or gas deposition) on the electrode substrate.
• a positive photoresist is made insoluble or nonvolatile as a consequence of selected area irradiation, so the substrate conducting electrode is
• the irradiation process can lead to either enhanced solubility or volatilization of the irradiated regions of the photoresist.
• electrode can be used to expose the conductor surface only at irradiated regions of the photoresist. Upon subsequent electroplating, the superconductor precursor alloy forms only on portions of the electrode where the insulating layer of photoresist has been removed.
• the metal alloy composition which is precursor to
• the superconductor can also be electrochemically deposited in a patterned form on an electrode using photoinduced enhancement of electrochemical deposition.
• the most convenient photon source is a high energy laser which is scanned across the electrode surface to generate the patterned alloy deposition.
• the mechanism of the photoenhanced electrochemical deposition varies. For example, relatively low photon fluxes can be used to generate photocarriers in a photoconductor present at the electrode surface. The resulting current flow through the photoconductor then generates the patterned alloy deposition.
• the photon source can provide patterned alloy deposition by selective volume heating of either the electrolyte or the electrode surface, so as to provide increased current flow at points of irradiation.
• High temperature oxidation and thermal annealing transforms the patterned alloy deposition into a patterned superconductor deposition.
• Patterned deposition on a photoconductor surface can also result from patterned exposure to penetrating radiation, such as x-rays. Hence, it is possible to generate a patterned deposition of the superconductor on surface areas which are inaccessible to either visible or ultraviolet radiation.
• a patterned counter electrode or patterned motion of a counter electrode can be used for the electroplating of the precursor superconductor alloy.
• segmentation of the patterned counter electrode so as to provide subunits in the pattern which are at different voltages, provides an additional design feature for the patterned electroplating of the precursor superconductor alloy. This effective segmentation can be either by direct electrical separation or by the use of internal resistive elements.
• use of a counter electrode which undergoes voltage changes during patterned motion provides additional flexibility for the electrochemical deposition of a patterned superconductor precursor alloy.
• Modification of the above-described photoenhanced electrochemical deposition can be used to conveniently generate parallel superconducting wires having separations comparable with the wavelength of light.
• the modified approach utilizes the alternating stripes of intense light and near-zero light intensity resulting from the interference of two light beams.
• This pattern of illumination .generates, via selected area photoenhancement of current flow, the patterned deposition of superconductor precursor alloy.
• oxidation of the thereby obtained precursor alloy wires can provide the additional advantage of oriented growth of the superconductor as a consequence of the shape anisotropy of the precursor alloy. Such oriented growth is preferred for improving the properties of the superconductor, and specifically for increasing the critical amount.
• Patterned electrochemical deposition of the superconductor precursor alloy on a transparent electrode substrate permits preparation of an optically transparent superconductor.
• the pattering such as an array of parallel strips or a two-dimensional dot array of either the superconducting or the superconductor-free areas, provides for optical transparency.
• Such transparent films can find applications as windows which have extremely high efficiency for the shielding of radio frequency and microwave frequency radiation.
• Use of a two-dimensional dot array of superconductor can provide for a film which is superconducting in the film thickness direction and insulating in the plane of the film.
• the electrode electroplated with the superconductor precursor alloy can be in the form of a moving belt or wire which passes continuously into the electroplating solution and into close proximity to the counter electrode. (Passage of the wire through the center of a cylindrical counter electrode is preferred in the latter instance.) If desired, the belt (or wire) can then pass from the electroplating solution into a chamber for thermal treatment in an oxygen-containing atmosphere. This thermal treatment in oxygen to provide the high temperature superconductor can employ an oxygen plasma or laser-induced heating. If thick coatings of the superconductor are desired, the belt (or wire) can pass continuously between the electroplating bath and the oxidation chamber.
• thick coatings of superconductor can be formed on a drum-shaped article by rotation of a drum-shaped electrode so that electroplating continuously occurs on the side of the drum which is immersed in the electroplating solution.
• the opposite side of the drum can be continuously laser heated in an oxygen-containing atmosphere to transform the metal alloy into a superconductor.
• electrodeposition can be on a disk shaped counter electrode which is continuously rotated, so as to expose a continuously varying surface of the disk to electroplating process.
• the rotating drum method can be employed for the direct fabrication of a spiral-like wind of superconducting and insulating sheets.
• processing conditions can be changed so that near 360, deposition of an insulator is applied. Alternation of the processing conditions which result in the insulator and the superconductor, so as to maintain continuity in the superconductor sheet, results in the winding of the magnet.
• the changes in processing conditions can correspond to changes in the applied electrochemical potential, changes in the composition of the electrochemical bath, and/or changes in the heat treatment environment, so as to result in the change from formation of superconductor to formation of insulator.
• the insulator layer can be applied by more conventional routes, such as sputtering 0 a layer of insulating oxide.
• the electrochemical approach is well suited for deposition of the superconductor precursor alloy on complicated shapes and S interior surfaces of articles.
• the precursor alloy to the superconductor can be deposited on the inside surface of a pipe by filling the pipe with electrolyte, centrally located the anode in the pipe, and utilizing the inner surface of the pipe as the 0 cathode for electrochemical deposition. Transformation of the precursor alloy into the superconductor is then conveniently accomplished by heat treatment of the pipe in an oxygen-containing atmosphere.
• Example I Europium, barium, and copper were codeposited by O electrodeposition onto a platinum foil electrode in a molar ratio of 1-2-3.
• the platinum foil electrode, a copper counter electrode, and a Ag/Ag+ reference electrode were immersed in a dimethylsulfoxide solution that was 0.1 M in Eu(N0 3 ) 3 , 0.27 M in Ba(N0 3 ) 2 , and 5 0.051 M in Cu ( OCOCH 3 ) 2>
• a constant potential of -5.0 V versus the Ag/Ag+ electrode was applied to the platinum electrode and a deposit formed on the platinum electrode. After 11 coulombs/cm 2 had passed, the platinum electrode was removed, rinsed in fresh DMSO and dried.
• Example II Bismuth, strontium, calcium and copper were codeposited onto a platinum foil electrode in a ratio of 0.2-0.2-1-2 following the procedure outlined in Example I. Ten coulombs were passed while a potential of -4V vs a Ag/Ag + reference electrode was applied to the platinum electrode while the substrate was immersed in a DMSO solution of 0.02 M Bi(N0 3 ) 3 , 0.1 M Sr(N0 3 ) 2 , 0.092 M Ca(N0 3 ) 2 r and 0.025 M Cu(OCOCH 3 ) 2 . A smooth film comprised of tightly packed micro spheres resulted, each sphere consisting of the four elements.
• Yttrium, barium and copper were codeposited by electrodeposition onto a platinum foil electrode in a ratio of 1:2:3.
• the platinum foil electrode and a copper counter electrode were immersed in a dimethyl- sulfoxide (DMSO) solution of 0.021M Y(N0 3 ) 3 , 0.057M Ba
• the platinum electrode was removed, rinsed in fresh DMSO and dried and analyzed by the electron microprobe technique. The analysis indicated that the deposit consisted of Y, Ba and Cu in the ratio of roughly 1:2:3. The electrode thereafter was heated to about 900,C for about 5 minutes to yield a black film in place of the deposited metals.
• the black film exhibited an x-ray diffraction pattern identical to that of the previously prior art synthesized superconducting ceramic
• EXAMPLE IV Yttrium, barium, and copper were codeposited in different ratios, onto conductive indium-tin oxide films supported on quartz, from DMSO electrolytes having different relative concentrations of Y(N0 3 ) 3 , Ba(N0 3 ) 2 , and Cu(0C0CH 3 ) 2 .
• the total ion concentration was about 0.05 to about 0.1 M
• the potential applied to the substrate was -5 V versus Ag/Ag +
• about 2 to about 10 coulombs were passed during electrodeposition.
• the composition of the deposit was determined by electron microprobe analysis. Representative electrolytes and compositions of their resulting deposits are shown below. Electrolyte Composite v +3 - Ba +2 - Cu +2 Y - Ba - Cu
• Europium, barium, and copper were codeposited in a molar ratio of about 1-2-3 onto the interior surfaces of cylindrical copper tubes having internal diameters of 2, 4, and 6 mm.
• Each tube was fitted with a copper wire counter electrode held in the axial position of the tube by a porous separator of hydrophylic polypropylene (Celgar-d ) .
• a potential of -5 V versus its copper counter electrode was applied to the tube.
• a continuous film covering the internal surfaces of the tubes were formed. Samples of the films scraped from the tubes were shown by microprobe analysis to contain Eu, Ba, and Cu in a ratio of about 1-2-3.
• Bismuth, strontium, calcium, and copper were codeposited onto carbon mat in a ratio of about 0.2 - 0.2 - 1 - 2 following the procedure of Example II except that about 100 coulombs per cm 2 were passed during electrolysis.
• a film of the electrodeposited metals covered the carbon fibers. Oxidation of the coated carbon mat by heating at 850, C for 15 minutes substantially removed the carbon fibers leaving behind a continuous network of ceramic fibers.
• Example VII Selected area electrochemical deposition of the superconductor precursor alloys is accomplished by modifying conventional lithographic techniques which are conventionally employed to form circuits of metallic and semiconducting elements.
• An insulating photoresist is deposited by either solution or gas deposition on the platinum electrode substrate.
• a positive photoresist is made insoluble by selected area irradiation, so that the substrate conducting electrode is later revealed (after solvent or thermal treatment) in those regions of the electrode where the photoresist has not been irradiated.
• the electrode is electro ⁇ deposited as in Example I and only those regions, i.e., the non-irradiated regions of the electrode which are not insulating, undergo deposition of the alloy or metals upon electroplating.
• the superconductor precursor alloy forms only on the portions of the electrode where the insulating layer of photoresist has been removed.
• the oxidation is conducted in accordance with Example I.
• Example VIII A metal alloy composition which is precursor to the superconductor of Example I, is electrochemically deposited in a patterned form on an electrode using photo-induced enhancement of electrochemical deposition.
• the photon source is a high energy laser which is scanned across the electrode surface to generate the patterned alloy deposition.
• the selected photon frequency, electrolyte, electrode potential and target electrode surface is varied to control the rate of the photoenhanced electro-chemical deposition to a predetermined value.
• high temperature oxidation i.e., at about 900,C
• thermal annealing at about 650,C is employed to transform the patterned alloy deposition into a patterned superconductor film.
• Example V The method of Example V is modified to generate parallel superconducting wires having separations comparable with the wavelength of the light employed in the photo deposition.
• the approach utilizes alternating stripes of intense light and near zero light intensity resulting from the interference of two light beams appropriately positioned.
• the patterned illumination generates, through selected area photo-enhancement of current flow, the patterned deposition of superconductor precursor alloys.
• the oxidation of the thereby obtained precursor alloy wires provides oriented growth of the superconductor during oxidation as a consequence of the shape anisotropy of the precursor alloy. This preferred growth improves the properties of the superconductor with the oxidation being accomplished, into the superconducting state, in accordance with the method of
• Example X Deposition of the superconductor precursor alloys on the inside of a metal tube and on the surface of a metal wire is accomplished by electrochemical techniques similar to that described in examples I and II. Thereafter the oxidation to superconducting ceramic is conducted also in accordance with the processes described in examples I and II to give a wire and the inside of a tube coated with superconducting material.

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