Nanostructured thin film and method for controlling surface properties thereof
US-8974889-B2 · Mar 10, 2015 · US
US11697885B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11697885-B2 |
| Application number | US-201716334558-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 19, 2017 |
| Priority date | Sep 19, 2016 |
| Publication date | Jul 11, 2023 |
| Grant date | Jul 11, 2023 |
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A process is provided comprising submerging a substrate in an electrochemical deposit bath having at least a metal salt and saccharin. In embodiments, the film is further treated with anodization, and in other cases chemical vapor deposition. Films are also provided formed by the disclosed processes. The films are nanoporous on at least a portion of a surface of the films. Also disclosed are electronic devices having the films disclosed, including lithium-ion batteries, storage devices, supercapacitors, electrodes, semiconductors, fuel cells, and/or combinations thereof.
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We claim: 1. A process comprising at least partially submerging a substrate into an electrochemical deposition bath wherein a composition of the electrochemical deposition bath comprises at least a metal salt and saccharin; forming a deposit on the substrate; removing the deposit from the substrate to form a freestanding layer; and anodizing the freestanding layer to produce a nanoporous film; wherein the composition of the electrochemical deposition bath comprises one of (a) Co 2+ in a range of 0-250 g L −1 , Borate in a range of 0-45 g L −1 , a citrate salt in a range of 0-30 g L −1 , Saccharin up to 2 g L −1 ; wherein the electrochemical bath has a temperature in the range of 15-45° C., and wherein the electrochemical deposition bath comprises a salt of Co in a concentration of at least 0.001 g/L; and (b) Ni 2+ in a range of 0-230 g L −1 , Fe 2+ in a range of 0-40 g L −1 , Borate in a range of 0-50 g L −1 , the citrate salt in a range of 0-30 g L −1 , Saccharin up to 5 g L −1 ; wherein the electrochemical bath has a temperature in a range of 15-65° C., and wherein the electrochemical deposition bath comprises a salt of Ni and a salt of Fe each in a concentration of at least 0.001 g/L; and (c) Ni 2+ in a range of 0-220 g L −1 , Co 2+ in a range of 0-155 g L −1 , Borate in a range of 0-40 g L −1 , Cl − in a range of 0-13 g L −1 , wherein the electrochemical bath has a temperature in a range of 10-60° C., and wherein the electrochemical deposition bath comprises a salt of Ni and a salt of Co in a concentration of at least 0.001 g/L; and (d) Fe 2+ in a range of 0-100 g L −1 , Co 2+ in a range of 0-200 g L −1 , H 3 BO 3 in a range of 0-60 g L −1 , NaCl in a range of 0.001-50 g L −1 , Saccharin in a range of 0.001-5 g L −1 ; wherein the electrochemical bath has a temperature in a range of 10-50° C., and wherein the electrochemical deposition bath comprises a salt of Fe and a salt of Co each in a concentration of at least 0.001 g/L; and (e) Ni 2+ in a range of 0-100 g L −1 , Fe 2+ in a range of 0-100 g L −1 , Co 2+ in a range of 0-200 g L −1 , Borate in a range of 0-60 g L −1 , Cl − in a range of 0-50 g L −1 , Saccharin in a range of 0-5 g L −1 ; wherein the electrochemical bath has a temperature in a range of 10-55° C., and wherein the electrochemical deposition bath comprises a salt of Ni, a salt of Fe and a salt of Co each in a concentration of at least 0.001 g/L. 2. A process according to claim 1 , wherein the substrate comprises copper foil, nickel foil, stainless steel, indium tin oxide glass, indium tin oxide coated polyethylene or other conductive substrates. 3. A process according to claim 1 , which further comprises conducting an electrochemical deposition process on the substrate, wherein a current is applied having a current density is 0.001-1000 mA cm −2 . 4. A process according to claim 1 , wherein the salt of Fe in electrochemical deposition bath compositions (b), (d) and (e) is an Fe 2+ salt and the Fe 2+ is presented in the bath in an amount of at most 20% by weight based on the total weight of discharge ion salts. 5. A process according to claim 1 , wherein a source of the Fe comprises FeSO 4 , FeCl 2 , Fe(NO 3 ) 2 or other inorganic chemicals containing Fe. 6. The process of claim 1 , wherein the anodization is performed using an anodic electrolyte comprising F − in a range of 0.01-11 g L −1 , and water in a range of 0-54 g L −1 . 7. A process according to claim 6 , wherein a solvent for the anodic electrolyte comprises ethylene glycol, glycerol, dimethyl sulphoxide, N,N-dimethylformamide, or isopropyl alcohol, or a combination thereof. 8. A process according to claim 1 , wherein the pH of the electrochemical deposition bath is 1-6. 9. A process according to claim 8 , wherein a voltage is applied to the electrochemical deposition bath having a constant potential of 5-300 V. 10. The process of claim 1 , further comprising treating the film with a chemical vapor deposition (CVD) treatment.
of metals or alloys not provided for in groups C25D11/04 - C25D11/32 · CPC title
Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries · CPC title
Heterocyclic compounds · CPC title
characterised by their material · CPC title
as mixtures · CPC title
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