LITHIUM OXIDE RECOVERY METHOD FROM LITHIUM MANGANESE OXIDE (LMO)
20220194806 · 2022-06-23
Assignee
Inventors
Cpc classification
Y02W30/84
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C22B7/002
CHEMISTRY; METALLURGY
C01P2002/72
CHEMISTRY; METALLURGY
International classification
Abstract
A method for recovering lithium oxide from lithium manganese oxide (LMO) includes producing lithium oxide (Li.sub.2O) via thermal reaction of lithium manganese oxide (LMO) in an hydrogen atmosphere, and performing water leaching of the produced lithium oxide to separate the lithium oxide from other products.
Claims
1. A method for recovering lithium oxide (Li.sub.2O) from lithium manganese oxide (LMO), the method comprising producing lithium oxide via thermal reaction of lithium manganese oxide (LMO) in a hydrogen atmosphere.
2. The method of claim 1, wherein the method further comprises performing water leaching of the produced lithium oxide to separate the lithium oxide from other products.
3. The method of claim 1, wherein a temperature of the thermal reaction is equal to or higher than 800° C.
4. The method of claim 1, wherein a temperature of the thermal reaction is equal to or higher than 1000° C.
5. The method of claim 2, wherein the water leaching includes separating the lithium oxide from the other products based on a difference between solubility of the lithium oxide and solubility of the other products.
Description
BRIEF DESCRIPTION OF DRAWINGS
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[0029] Present Example. A method of recovering lithium oxide by thermal reaction of lithium manganese oxide (LMO) in the present disclosure in a hydrogen reducing atmosphere was performed as follows.
DETAILED DESCRIPTION
[0030] Examples of various embodiments are illustrated and described further below. Further, descriptions and details of well-known steps and elements are omitted for simplicity of the description. Furthermore, in the following detailed description of the present disclosure, numerous specific details are set forth in order to provide a thorough understanding of the present disclosure. However, it will be understood that the present disclosure may be practiced without these specific details. In other instances, well-known methods, procedures, components, and circuits have not been described in detail so as not to unnecessarily obscure aspects of the present disclosure. It will be understood that the description herein is not intended to limit the claims to the specific embodiments described. On the contrary, it is intended to cover alternatives, modifications, and equivalents as may be included within the spirit and scope of the present disclosure as defined by the appended claims.
[0031] The terminology used herein is for the purpose of describing particular embodiments only and is not intended to limit the present disclosure. As used herein, the singular forms “a” and “an” are intended to include the plural forms as well, unless the context clearly indicates otherwise. It will be further understood that the terms “comprises”, “comprising”, “includes”, and “including” when used in this specification, specify the presence of the stated features, integers, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, integers, operations, elements, components, and/or portions thereof. As used herein, the term “and/or” includes any and all combinations of one or more of the associated listed items. Expression such as “at least one of” when preceding a list of elements may modify the entirety of list of elements and may not modify the individual elements of the list. When referring to “C to D”, this means C inclusive to D inclusive unless otherwise specified.
[0032] Unless otherwise defined, all terms including technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this inventive concept belongs. It will be further understood that terms, such as those defined in commonly used dictionaries, should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and will not be interpreted in an idealized or overly formal sense unless expressly so defined herein.
[0033] One aspect of the present disclosure provides a method for recovering lithium oxide from lithium manganese oxide (LMO). The method includes producing lithium oxide (Li.sub.2O) via thermal reaction of lithium manganese oxide (LMO) in a hydrogen reduction atmosphere, and recovering the produced lithium oxide (Li.sub.2O) via water leaching. The method may be conducted by way example as follows:
Present Example
Present Example 1—Hydrogen Reduction Atmosphere and 350° C. Thermal Reaction
[0034] 300 g of lithium manganese oxide (LMO) positive electrode active material was thermally reacted for 3 hours at 350° C. under a hydrogen reducing atmosphere (5.4 L/3 hours). In this connection, a rate of hydrogen input was 300 mL/min.
Present Example 2—Hydrogen Reduction Atmosphere, 850° C. Thermal Reaction
[0035] The process was carried out in the same manner as in Present Example 1, except that the thermal reaction temperature was set to 850° C.
Present Example 3—Hydrogen Reduction Atmosphere, 950° C. Thermal Reaction
[0036] The process was carried out in the same manner as in Present Example 1, except that the thermal reaction temperature was set to 950° C.
Present Example 4—Hydrogen Reduction Atmosphere, 1150° C. Thermal Reaction
[0037] The process was carried out in the same manner as in Present Example 1, except that the thermal reaction temperature was set to 1150° C.
Comparative Example 1—Carbon Dioxide Atmosphere, 900° C. Thermal Reaction
[0038] 300 g of lithium manganese oxide (LMO) positive electrode active material was thermally reacted for 1 hour at 900° C. under a carbon dioxide atmosphere (1.8 L/hour). In this connection, a rate of carbon dioxide input was 300 ml/min.
Comparative Example 2—Carbon Dioxide Atmosphere, 1000° C. Thermal Reaction
[0039] The process was carried out in the same manner as in Comparative Example 1, except that the thermal reaction temperature was set to 1000 ° C.
Comparative Example 3—Carbon Dioxide Atmosphere, 1200° C. Thermal Reaction
[0040] The process was carried out in the same manner as in Comparative Example 1, except that the thermal reaction temperature was set to 1200° C.
Example Water Leaching
[0041] 5 g of the reaction product prepared in Present Example 4 was stirred with 50 ml of distilled water at a weight ratio of 1:10 for 30 minutes for washing, and thus a water leaching process was performed to separate the powder sample and the liquid sample from each other. The water leaching process is shown in
Experimental Example
Test 1—TGA (Thermogravimetric Analysis)
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Test 2—XRD Analysis
[0043] XRD analysis of the lithium manganese oxide (LMO) and the Present Examples 1 to 4 were carried out to analyze the components of the material obtained in each of Present Examples.
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[0047] In the graphs of
[0048] Further, in the graph of
[0049] Therefore, it may be identified based on the results of the XRD tests of lithium manganese oxide (LMO) and Present Examples 1 to 4 that the lithium manganese oxide (LMO) undergoes a phase change via a thermal reaction at 800° C. or higher, and a substantial portion of Li and Mn are separated from each other via a thermal reaction at 1000° C. or higher.
[0050] Further, Comparative Examples 1 to 3 using carbon dioxide instead of hydrogen were subjected to XRD analysis to analyze components of the materials obtained in each of Comparative Examples.
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[0052] Therefore, it may be identified based on the results of the XRD tests of lithium manganese oxide (LMO) and Comparative Examples 1 to 3 that when carbon dioxide is used instead of hydrogen, the thermal reaction proceeds at a temperature significantly higher than the thermal reaction temperature range of the Present Examples, resulting in a phase change of only a portion thereof, such that the complete separation between Li and Mn is not achieved.
Test 3—ICP-OES Analysis of Liquid
[0053] The liquid sample obtained through the example water leaching was analyzed using ICP-OES to measure the lithium content in the liquid sample.
[0054] It may be identified based on the result of the ICP-OES analysis, a Li element is present in the liquid sample and the Li element is contained at a content of 1928.21 ppm, so that Li is separated from Mn via the process according to the present disclosure.
Test 4—XRD Analysis and SEM Images of Powders
[0055] The powder sample obtained through the example water leaching was subjected to XRD analysis and was subjected to SEM imaging to observe the powder particles and shape thereof in the powder sample.
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[0057] Therefore, it may be identified based on the
[0058] Although the embodiments of the present disclosure have been described in more detail with reference to the accompanying drawings, the present disclosure is not necessarily limited to these embodiments. The present disclosure may be implemented in various modified manners within the scope not departing from the technical idea of the present disclosure. Accordingly, the embodiments disclosed in the present disclosure are not intended to limit the technical idea of the present disclosure, but to describe the present disclosure. the scope of the technical idea of the present disclosure is not limited by the embodiments. Therefore, it should be understood that the embodiments as described above are illustrative and non-limiting in all respects. The scope of protection of the present disclosure should be interpreted by the claims, and all technical ideas within the scope of the present disclosure should be interpreted as being included in the scope of the present disclosure.