Lithium ion battery recycling process utilizing magnetic separation of electrode materials
US-2024047775-A1 · Feb 8, 2024 · US
US2017029920A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017029920-A1 |
| Application number | US-201615097332-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 13, 2016 |
| Priority date | Jul 31, 2015 |
| Publication date | Feb 2, 2017 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Provided is a recovery method of useful resources in seawater and brine, and more particularly, a recovery method of useful resources in seawater and brine capable of improving adsorption efficiency and recovery efficiency of trace amounts of useful resources such as strontium, lithium, boron, or the like, present in brine at low cost by using a magnetic adsorbent composite and a solid-liquid separation process which uses magnetic force.
Opening claim text (preview).
What is claimed is: 1 . A recovery method of useful resources in seawater and brine, the recovery method comprising: (a) adsorbing the useful resources in the seawater and brine using a magnetic adsorbent composite; (b) obtaining a useful resource desorption solution in which the useful resources are concentrated by desorbing the useful resources adsorbed in the magnetic adsorbent composite using a desorption solution; and (c) obtaining a compound from the useful resource desorption solution. 2 . The recovery method of claim 1 , wherein the magnetic adsorbent composite has a multilayer structure in which a core layer is made of magnetic particles, an adsorbent material layer is formed by coating a useful resource-adsorbent material on a surface of the core layer, and a binder layer is further formed between the core layer and the adsorbent material layer. 3 . The recovery method of claim 1 , wherein the useful resources are one or two or more selected among lithium, strontium, and boron. 4 . The recovery method of claim 2 , wherein the magnetic particles are made of one or two or more selected among iron, nickel, cobalt, manganese, gadolinium, and oxides thereof, magnetite, maghemite, iron monoxide, iron nitride, a cobalt platinum chromium alloy, a barium ferrite alloy, an aluminum manganese alloy, an iron platinum alloy, an iron palladium alloy, a cobalt platinum alloy, and a samarium cobalt alloy, the binder layer contains carbon, and the adsorbent material includes manganese and manganese oxides. 5 . The recovery method of claim 1 , wherein the magnetic adsorbent composite is prepared by a preparation method including: (1) mixing magnetic particles and a carbon precursor to prepare a mixture; (2) reacting the mixture at 150 to 250° C. to prepare magnetic particles on which a carbon layer is formed; and (3) mixing and reacting the magnetic particles on which the carbon layer is formed with an adsorbent material precursor solution. 6 . The recovery method of claim 5 , wherein in step (1), 50 to 300 parts by weight of the carbon precursor is contained in the mixture based on 100 parts by weight of the magnetic particles, the carbon precursor is one or two or more selected among glucose, citric acid, and polyethylene glycol (PEG), and the preparation method further includes, after step (2) and step (3), separating the magnetic particles using magnetic force, washing the separated magnetic particles, and then drying the washed magnetic particles. 7 . The recovery method of claim 5 , wherein in step (3), a concentration of the adsorbent material precursor solution is 0.01 to 1M, and a reaction is carried out under room temperature and atmospheric pressure conditions for 120 hours or more. 8 . The recovery method of claim 1 , further comprising, after step (a) and step (b), dispersing and washing the magnetic adsorbent composite in which the useful resources are adsorbed or from which the useful resources are desorbed in clean water, and separating the magnetic adsorbent composite using magnetic force. 9 . The recovery method of claim 1 , wherein the seawater and brine are seawater and brine from which dissolved magnesium and calcium are removed using a seawater electrolytic process. 10 . A magnetic adsorbent composite comprising: a core layer containing a magnetic particle; a binder layer containing carbon coated on a surface of the core layer; and an adsorbent material layer formed by coating a useful resource-adsorbent material on the binder layer. 11 . The magnetic adsorbent composite of claim 10 , wherein the binder layer has an average thickness of 5 to 20 nm and is contained in the entire magnetic adsorbent composite in a content range of 5 to 15 wt %, and the adsorbent material layer is contained in the entire magnetic adsorbent composite in a content range of 10 to 35 wt %.
Obtaining alkaline earth metals or magnesium · CPC title
Separation by a physical processing technique only, e.g. by mechanical breaking · CPC title
comprising inorganic material · CPC title
by sorption (using ion-exchange C02F1/42; sorbent compositions B01J) · CPC title
Heavy metals or heavy metal compounds · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.