Prosecution Insights
Last updated: October 02, 2026
Application No. 18/008,846

METHOD FOR PRODUCING LITHIUM SULFIDE

Final Rejection §103
Filed
Dec 07, 2022
Priority
Jul 09, 2020 — JP 2020-118591 +1 more
Examiner
PATEL, SUHANI JITENDRA
Art Unit
1783
Tech Center
1700 — Chemical & Materials Engineering
Assignee
Mitsui Mining & Smelting Co., Ltd.
OA Round
3 (Final)
61%
Grant Probability
Moderate
4-5
OA Rounds
0m
Est. Remaining
72%
With Interview

Examiner Intelligence

Grants 61% of resolved cases
61%
Career Allowance Rate
11 granted / 18 resolved
-3.9% vs TC avg
Moderate +11% lift
Without
With
+11.1%
Interview Lift
resolved cases with interview
Typical timeline
3y 5m
Avg Prosecution
29 currently pending
Career history
60
Total Applications
across all art units

Statute-Specific Performance

§101
0.8%
-39.2% vs TC avg
§103
70.2%
+30.2% vs TC avg
§102
18.7%
-21.3% vs TC avg
§112
6.4%
-33.6% vs TC avg
Black line = Tech Center average estimate • Based on career data from 18 resolved cases

Office Action

§103
DETAILED ACTION Notice of Pre-AIA or AIA Status The present application, filed on or after March 16, 2013, is being examined under the first inventor to file provisions of the AIA . Status of Claims Claims 1, 10 are amended. Claim 5-8 are cancelled. Claims 1-4, 9-14 are pending. Response to Amendment Applicant’s amendments filed on 7/2/2026 have been entered. Claim rejections under 35 USC 103 from previous Office Action have been modified in view of amendments. Claim Rejections - 35 USC § 103 In the event the determination of the status of the application as subject to AIA 35 U.S.C. 102 and 103 (or as subject to pre-AIA 35 U.S.C. 102 and 103) is incorrect, any correction of the statutory basis (i.e., changing from AIA to pre-AIA ) for the rejection will not be considered a new ground of rejection if the prior art relied upon, and the rationale supporting the rejection, would be the same under either status. The following is a quotation of 35 U.S.C. 103 which forms the basis for all obviousness rejections set forth in this Office action: A patent for a claimed invention may not be obtained, notwithstanding that the claimed invention is not identically disclosed as set forth in section 102, if the differences between the claimed invention and the prior art are such that the claimed invention as a whole would have been obvious before the effective filing date of the claimed invention to a person having ordinary skill in the art to which the claimed invention pertains. Patentability shall not be negated by the manner in which the invention was made. Claim(s) 1, 4, 5, 7-10, 13 are rejected under 35 U.S.C. 103 as being unpatentable over Naruhashi et al (JP 2016216312A; machine translation) as evidenced by Cammack et al (“Reaction intermediates”, Cammack, R. Attwood, T. K. Campbell, P. N. Parish, J. H. Smith, A. D. Stirling, J. L. Vella, F.. (2006). Oxford Dictionary of Biochemistry and Molecular Biology (2nd Edition). Oxford University Press. Retrieved from https://app.knovel.com/hotlink/toc/id:kpODBMBE01/oxford-dictionary-biochemistry/oxford-dictionary-biochemistry). Regarding Claim 1 and Claim 9, Naruhashi teaches a method for producing lithium sulfide, comprising a step of calcining a raw material mixture containing lithium sulfate (a raw material containing lithium and sulfur elements) and a reducing agent (Paragraph 0009). The reducing agent is selected from carbon materials such as organic sugars, polyhydric alcohols, and carbon black, carbon fiber etc (Paragraphs 0018-0021). Naruhashi teaches the use of inert gas in the firing step such as nitrogen, argon, helium or hydrogen (Paragraph 0029; reducing gas). The claimed invention states a first step of reducing a raw material containing lithium (Li) and sulfur (S) elements, using a reductant containing a carbon (C) element, thereby obtaining an intermediate; and a second step of reducing the intermediate using a reducing gas, thereby obtaining lithium sulfide, wherein the second step is performed at a temperature in a range of 830 C to 930 C. Per Cammack, the definition of “reaction intermediates” is a transient chemical species formed directly or indirectly from the reactants of a chemical reaction, and that further reacts to give the reaction products. Furthermore, the instant specification also states that the first step and second step are performed simultaneously when a reducing atmosphere is used as the atmosphere for the reduction reaction (Paragraph 0020). Naruhashi has the same reactants (lithium-sulfur compound, and reductant), and it also has the same calcining/heat treatment temperature and atmosphere (inert gas such as nitrogen, argon, helium, hydrogen). Hydrogen is an inert reducing gas atmosphere. Hence, Naruhashi’s reaction would also produce an intermediate, and result in a two step reaction as claimed in instant invention. Furthermore, Naruhashi teaches that the calcining step has a temperature of 750 to 1000 C (Paragraph 0029), and in an example Naruhashi states that the raw material mixture is placed in a crucible and heated to 900 C at a rate of 5C/min in a nitrogen gas atmosphere in a firing furnace (Paragraph 0057). The temperature range in Naruhashi contains the claimed first step temperature range of 700 to 800 C, and the claimed second step range of 830 C to 930 C. Moreover, based on the heating rate of 5C/min, the raw materials of Naruhashi would be gradually heated between the ranges of both the first and second step claimed temperature ranges. The resulting intermediate and products of Naruhashi would in turn be the same as the claimed invention. Hence, it would have been obvious to one of ordinary skill in the art prior to the effective filing date of the claimed invention that the temperature range from Naruhashi is within the claimed range of both the first and second steps in order to suppress the formation of a different phase and efficiently obtain lithium sulfide (Paragraph 0029). Claim 9 is a product-by-process claim that claims the lithium sulfide product made with method described above using the teachings of Naruhashi. Regarding Claim 4, Naruhashi teaches the use of an inert gas atmosphere such as nitrogen, argon, helium, or hydrogen (Paragraph 0029). Nitrogen, argon are non-reducing inert gases akin to the inert gases in instant specification in Paragraph 0020. Regarding Claim 10, and Claim 13, Naruhashi teaches a method for producing an inorganic solid electrolyte comprising lithium sulfide obtained by specific method described in Naruhashi, and reacting that with phosphorus sulfide and lithium iodide (Paragraph 0044). The phosphorus sulfide can be phosphorus pentasulfide as seen in formulas shown in Paragraph 0045 i.e. P2S5. Lithium iodide is a lithium halide. The process consists of mechanical milling and mixing the above compounds, and then heating and melting the resulting mixture in an inert gas atmosphere (Paragraph 0047). This is akin to firing the raw material composition. The method of producing lithium sulfide per Naruhashi is also akin to the claimed invention. Naruhashi teaches a method for producing lithium sulfide, comprising a step of calcining a raw material mixture containing lithium sulfate (a raw material containing lithium and sulfur elements) and a reducing agent (Paragraph 0009). The reducing agent is selected from carbon materials such as organic sugars, polyhydric alcohols, and carbon black, carbon fiber etc (Paragraphs 0018-0021). Naruhashi teaches the use of inert gas in the firing step such as nitrogen, argon, helium or hydrogen (Paragraph 0029). The claimed invention states a first step of reducing a raw material containing lithium (Li) and sulfur (S) elements, using a reductant containing a carbon (C) element, thereby obtaining an intermediate; and a second step of reducing the intermediate using a reducing gas, thereby obtaining lithium sulfide, wherein the second step is performed at a temperature in a range of 830 C to 930 C. Per Cammack, the definition of “reaction intermediates” is a transient chemical species formed directly or indirectly from the reactants of a chemical reaction, and that further reacts to give the reaction products. Naruhashi has the same reactants (lithium-sulfur compound, and reductant), and it also has the same calcining/heat treatment temperature and atmosphere (inert gas such as nitrogen, argon, helium, hydrogen). Hence, Naruhashi reaction would also produce an intermediate, and result in a two step reaction as claimed in instant invention. Furthermore, Naruhashi teaches that the calcining step has a temperature of 750 to 1000 C (Paragraph 0029), and in an example Naruhashi states that the raw material mixture is placed in a crucible and heated to 900 C at a rate of 5C/min in a nitrogen gas atmosphere in a firing furnace (Paragraph 0057). The temperature range in Naruhashi contains the claimed first step temperature range of 700 to 800 C, and the claimed second step range of 830 C to 930 C. Moreover, based on the heating rate of 5C/min, the raw materials of Naruhashi would be gradually heated between the ranges of both the first and second step claimed temperature ranges. The resulting intermediate and products of Naruhashi would in turn be the same as the claimed invention. Hence, it would have been obvious to one of ordinary skill in the art prior to the effective filing date of the claimed invention that the temperature range from Naruhashi is within the claimed range of both the first and second steps in order to suppress the formation of a different phase and efficiently obtain lithium sulfide (Paragraph 0029). Claim 11 is rejected under 35 U.S.C. 103 as being unpatentable over Naruhashi as evidenced by Cammack, and further in view of Kambara et al (US 20140302382 A1). Naruhashi teaches the solid electrolyte formed using the same raw materials, and process of making, but does not specifically teach that the solid electrolyte contains a crystalline phase with an argyrodite type crystal structure. However, Kambara teaches a method to make solid electrolyte that has a crystalline phase (Paragraph 0181). Kambara also refers to the crystallized solid electrolyte as a glass ceramic (Paragraph 0181). This type of material is considered to have an argyrodite structure. Also, per MPEP 2112.01 II., products of identical chemical composition can not have mutually exclusive properties. Hence, the solid electrolyte of Kambara has a crystalline phase, and argyrodite structure as claimed. Claim 2, 3, 12, 14 are rejected under 35 U.S.C. 103 as being unpatentable over Naruhashi as evidenced by Cammack, in view of Kikuchi et al (US 20230135532 A1; effective filing date 03/17/2020). Regarding Claim 2 and Claim 3, Naruhashi teaches the two step reaction of claimed invention that occurs in an inert atmosphere of hydrogen which is a reducing gas. Naruhashi has the same reactants (lithium-sulfur compound, and reductant), and it also has the same calcining/heat treatment temperature and atmosphere (inert gas such as nitrogen, argon, helium, hydrogen). Hydrogen is an inert reducing gas atmosphere. Naruhashi teaches the use of X-ray diffraction to measure the peaks related to the products of the lithium sulfide process such that the peaks are measured at the 2θ corresponding to lithium sulfate, lithium sulfide and lithium carbonate. Since, the reactions, and method related to heat treatment and inert atmosphere in Naruhashi is the same as the claimed invention, it is expected that the intensity of the resulting products using XRD is the same as the claimed invention. See MPEP 2112.01, that states when the claimed and prior art products are produced by identical or substantially identical processes, a prima facie case of obviousness has been established. Furthermore, in Kikuchi Figure 4 (annotated below), X-ray diffraction is used to measure the unreacted residue, and in the product peaks of raw material lithium sulfate (which is the claimed IA) do not appear. The XRD graph also shows that in the region of the peak for lithium carbonate (which is the claimed IC) there is no discernable peak formed. This means that the product has negligible amounts of lithium carbonate. Kikuchi has similarity in lithium sulfide production process as explained in more detail in rejection of Claims 12, 14 below. Hence, it would have been obvious to one of ordinary skill in the art prior to the effective filing date of the claimed invention that the XRD peak intensities of resulting products in the combined method of Naruhashi and Kikuchi are in the same ratio as the claimed invention in order to produce lithium sulfide with high ionic conductivity (Paragraph 0013). PNG media_image1.png 852 556 media_image1.png Greyscale Regarding Claim 12, Naruhashi teaches the two step reaction of claimed invention that occurs in an inert atmosphere of hydrogen which is a reducing gas. Naruhashi teaches the use of argon and nitrogen as inert gases used in the heating step, but does not specifically teach that the first step is performed in an inert gas atmosphere which is non-reducing. However, Kikuchi teaches a method for producing lithium sulfide in which a first reaction step takes place between lithium sulfate, and reducing agent such as carbon (Paragraph 0021, 0024). Kikuchi also teaches that an inert gas atmosphere of argon or nitrogen is used in the furnace for this reaction step (Paragraph 0029). These are non-reducing inert gases per the ones used in the instant specification. Hence, it would have been obvious to one of ordinary skill in the art prior to the effective filing date of the claimed invention to combine the teachings of Naruhashi and Kikuchi to use the non-reducing atmosphere for reacting lithium sulfate and carbon in order to produce lithium sulfide with high ionic conductivity (Paragraph 0013). Regarding Claim 14, Naruhashi teaches the method steps of claim 10, and the use of inert gas atmosphere in the calcining step, but does not specifically teach that the first step is performed in a non-reducing inert gas atmosphere. However, Kikuchi teaches a method for producing lithium sulfide in which a first reaction step takes place between lithium sulfate, and reducing agent such as carbon (Paragraph 0021, 0024). Kikuchi also teaches that an inert gas atmosphere of argon or nitrogen is used in the furnace for this reaction step (Paragraph 0029). These are non-reducing inert gases per the ones used in the instant specification. Hence, it would have been obvious to one of ordinary skill in the art prior to the effective filing date of the claimed invention to combine the teachings of Naruhashi and Kikuchi to use the non-reducing atmosphere for reacting lithium sulfate and carbon in order to produce lithium sulfide with high ionic conductivity (Paragraph 0013). References of Interest Barker et al (US 20110200878 A1) Response to Arguments Applicant’s arguments with respect to claim(s) 1 have been considered but are moot because the new ground of rejection does not rely on the same interpretation and embodiment of the reference applied in the prior rejection of record for any teaching or matter specifically challenged in the argument. Applicant argues that the combination of Naruhashi and Cammack does not disclose or suggest the features of amended claim 1 related to the temperature range of first and second step. Examiner disagrees with this argument, and points to rejection in section above. Naruhashi teaches a heating rate in the furnace calcining step which implies that the raw material is heated within the temperature ranges of the first step initially and then the range of the second step as the temperature in the furnace increases gradually. Furthermore, Cammack supports how the intermediate formed in a two-step reaction is a transient chemical species formed directly or indirectly from the reactants of a chemical reaction, and that further reacts to give the reaction products (simultaneous reaction steps). Hence, Naruhashi as evidenced by Cammack still reads on amended claim 1. Conclusion Applicant's amendment necessitated the new ground(s) of rejection presented in this Office action. Accordingly, THIS ACTION IS MADE FINAL. See MPEP § 706.07(a). Applicant is reminded of the extension of time policy as set forth in 37 CFR 1.136(a). A shortened statutory period for reply to this final action is set to expire THREE MONTHS from the mailing date of this action. In the event a first reply is filed within TWO MONTHS of the mailing date of this final action and the advisory action is not mailed until after the end of the THREE-MONTH shortened statutory period, then the shortened statutory period will expire on the date the advisory action is mailed, and any nonprovisional extension fee (37 CFR 1.17(a)) pursuant to 37 CFR 1.136(a) will be calculated from the mailing date of the advisory action. In no event, however, will the statutory period for reply expire later than SIX MONTHS from the mailing date of this final action. Any inquiry concerning this communication or earlier communications from the examiner should be directed to SUHANI JITENDRA PATEL whose telephone number is (571)272-6278. The examiner can normally be reached Monday-Friday 8:00 AM - 5:00 PM. Examiner interviews are available via telephone, in-person, and video conferencing using a USPTO supplied web-based collaboration tool. To schedule an interview, applicant is encouraged to use the USPTO Automated Interview Request (AIR) at http://www.uspto.gov/interviewpractice. If attempts to reach the examiner by telephone are unsuccessful, the examiner’s supervisor, Maria Veronica D. Ewald can be reached on 571-272-8519. The fax phone number for the organization where this application or proceeding is assigned is 571-273-8300. Information regarding the status of published or unpublished applications may be obtained from Patent Center. Unpublished application information in Patent Center is available to registered users. To file and manage patent submissions in Patent Center, visit: https://patentcenter.uspto.gov. Visit https://www.uspto.gov/patents/apply/patent-center for more information about Patent Center and https://www.uspto.gov/patents/docx for information about filing in DOCX format. For additional questions, contact the Electronic Business Center (EBC) at 866-217-9197 (toll-free). If you would like assistance from a USPTO Customer Service Representative, call 800-786-9199 (IN USA OR CANADA) or 571-272-1000. /SUHANI JITENDRA PATEL/Examiner, Art Unit 1783 /MARIA V EWALD/Supervisory Patent Examiner, Art Unit 1783
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Prosecution Timeline

Dec 07, 2022
Application Filed
Jul 09, 2025
Non-Final Rejection mailed — §103
Dec 05, 2025
Response Filed
Mar 06, 2026
Non-Final Rejection mailed — §103
Jul 02, 2026
Response Filed
Sep 11, 2026
Final Rejection mailed — §103 (current)

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Prosecution Projections

4-5
Expected OA Rounds
61%
Grant Probability
72%
With Interview (+11.1%)
3y 5m (~0m remaining)
Median Time to Grant
High
PTA Risk
Based on 18 resolved cases by this examiner. Grant probability derived from career allowance rate.

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