Prosecution Insights
Last updated: August 17, 2026
Application No. 17/707,524

ARGYRODITE SOLID ELECTROLYTES FOR SOLID-STATE BATTERIES AND METHODS OF MAKING THE SAME

Final Rejection §103
Filed
Mar 29, 2022
Priority
Jul 15, 2021 — CN 202110800597.8
Examiner
APPLEGATE, SARAH ARIMINTIA
Art Unit
1725
Tech Center
1700 — Chemical & Materials Engineering
Assignee
GM Global Technology Operations LLC
OA Round
5 (Final)
50%
Grant Probability
Moderate
6-7
OA Rounds
0m
Est. Remaining
99%
With Interview

Examiner Intelligence

Grants 50% of resolved cases
50%
Career Allowance Rate
10 granted / 20 resolved
-15.0% vs TC avg
Strong +56% interview lift
Without
With
+55.6%
Interview Lift
resolved cases with interview
Typical timeline
3y 5m
Avg Prosecution
38 currently pending
Career history
71
Total Applications
across all art units

Statute-Specific Performance

§101
0.4%
-39.6% vs TC avg
§103
64.2%
+24.2% vs TC avg
§102
17.1%
-22.9% vs TC avg
§112
12.8%
-27.2% vs TC avg
Black line = Tech Center average estimate • Based on career data from 20 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 . Election/Restrictions Claims 12-20 are withdrawn from further consideration pursuant to 37 CFR 1.142(b), as being drawn to a nonelected invention, there being no allowable generic or linking claim. Applicant timely traversed the restriction (election) requirement in the reply filed on 02/11/2025. 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. The factual inquiries for establishing a background for determining obviousness under 35 U.S.C. 103 are summarized as follows: 1. Determining the scope and contents of the prior art. 2. Ascertaining the differences between the prior art and the claims at issue. 3. Resolving the level of ordinary skill in the pertinent art. 4. Considering objective evidence present in the application indicating obviousness or nonobviousness. Claims 1-11 are rejected under 35 U.S.C. 103 as being unpatentable over Platt et al. (WO 2020153973 A1, “Platt”) in view of Yamamoto et al. (US 20180062200 A1, “Yamamoto”) and Makino et al. (US 20190198919 A1, “Makino”). Regarding claim 1, Platt discloses a method for making a solid-state argyrodite electrolyte (see title “solid electrolyte material synthesis method”; see [0022] “Li6PS5Br argyrodite” and see [0027] “Li6PS5Cl argyrodite”) the method comprising: contacting a first suspension and a first solution to form a precursor (see [0023] “precursors to generate the solid electrolyte”; see [0014] “These two solutions require a very short stirring time to produce two homogenous solutions that may be mixed and stirred again to form a final homogenous mixture of the solid electrolyte solution”; see [0022] 1st line disclosed mixing of two different solutions/suspension generated in step 120 (generates suspension) and step 130 (generates solution); see [0023] describes “homogenization and reaction of precursors to generate the solid electrolyte”), the first suspension comprising Li3PS4 (see [0018] “step 120” & “PS43- backbone” & “approximately 1 mole of Li2S is used for every 1 mole of P2S5 to achieve the desired solution”; see [0020] describes “reactants are Li2S and P2S5, Li3PS4”) and an ester solvent (see [0017] describes “solvents for use in step 120” and “ester molecules”). Platt discloses the first solution comprising Li2S, LiX (where X is selected from chloride (Cl), bromide (Br), iodine (I), or a combination thereof), and an alcohol solvent (see [0022] describes “second reactants Li2S and LiBr, and second solvent” & “to form a Li6PS5Br argyrodite composed of PS43- units”; see [0021] describes “multiple solvents” for step 130 & [0020] describes “second solvents” & “alcohols”). Platt discloses and removing the ester solvent and the alcohol solvent from the precursor to form the solid-state argyrodite electrolyte represented by the formula Li6PS5X, where X is selected from chloride (Cl), bromide (Br), iodine (I), or any combination thereof (see [0014] describes “the solvents may be removed from the solution by a technique such as vacuum drying to form the final solid electrolyte”; see [0022] describes “Li6PS5Br argyrodite”) and the solid-state argyrodite electrolyte has an ionic conductivity greater than or equal to about 1.0 x 10-4 S/cm to less than or equal to about 10 x 10-3 S/cm at about 25 °C (see P7 line 30 through P8 line 6 “Example 3 (Dual solution Method) ionic conductivity of the sample was 1.6 mS/cm.”; see P8 line 5 “ambient temperature”). Platt discloses 1.6 mS/cm which is equivalent to 0.0016 S/cm, which lies within the claimed range of about 1.0 x 10-4 S/cm to less than or equal to about 10 x 10-3 S/cm. Platt does not explicitly disclose ester solvent selected from the group consisting of: methyl formate, methyl propionate, methyl butyrate, methyl pentanoate, ethyl formate, ethyl propionate, ethyl butyrate, ethyl pentanoate, ethyl hexanoate, ethyl heptanoate, ethyl octanoate, ethyl decanoate, propyl acetate, propyl propanoate, isopropyl acetate, isopropyl palmitate, butyl butyrate, isobutyl acetate, amyl acetate, pentyl propanoate, pentyl butyrate, pentyl pentanoate, pentyl hexanoate, isoamyl acetate, sec-amyl acetate, and combinations thereof. Yamamoto teaches ester in [0095] “non-limiting examples the organic solvent” & “esters such as methyl formate”. Platt and Yamamoto are analogous to the current invention because they are related to the same field of endeavor, namely solid electrolyte (see [0095]). Yamamoto teaches methyl formate amongst a list of other ester solvents. KSR Rationale E states that it is obvious to choose "from a finite number of identified, predictable solutions, with a reasonable expectation of success". Therefore, it would have been obvious to one of ordinary skill in the art before the effective filing date of the claimed invention to select methyl acetate from the list of possible ester solvents taught in Yamamoto. Platt does not explicitly disclose an alcohol solvent selected from the group consisting of: 1-butanol, 2-butanol, 3-pentanol, isopentanol, neopentanol, cyclopentanol, hexanol, cyclohexanol, methylcyclohexanol, heptanol, nonanol, and combinations thereof. Makino teaches in [0176] “cyclohexanol”. Platt and Makino are analogous to the current invention because they are related to the same field of endeavor, namely methods for manufacturing solid electrolytes (see Makino title). Makino teaches cyclohexanol amongst a list of other alcohol compound solvents. KSR Rationale E states that it is obvious to choose "from a finite number of identified, predictable solutions, with a reasonable expectation of success". Therefore, it would have been obvious to one of ordinary skill in the art before the effective filing date of the claimed invention to select cyclohexanol from the list of possible alcohol compound solvents taught in Makino. Regarding claim 2, modified Platt discloses the method of claim 1 and further discloses wherein the ester solvent is a first ester solvent and the first suspension further comprises a second ester solvent selected from the group consisting of: ethyl acetate (see [0017] “solvents for use in step 120 may include…ester molecules such as ethyl acetate…”), and the alcohol solvent is a first alcohol solvent and the first solution further comprises a second solvent (see [0021] “step 130” & “multiple solvents” & see [0020] “second solvents” & “alcohols”). Platt does not explicitly disclose selected from the group consisting of: tert-butanol, 2-pentanol, isobutanol, 1-pentanol, and combinations thereof. Makino teaches in [0164] “alcohol compound solvent” & “isobutanol” & “2-pentanol” & “t-butanol” which reads on tert-butanol. Makino teaches isobutanol, t-butanol, and 2-pentanol amongst a list of other alcohol compound solvents. KSR Rationale E states that it is obvious to choose "from a finite number of identified, predictable solutions, with a reasonable expectation of success". Therefore, it would have been obvious to one of ordinary skill in the art before the effective filing date of the claimed invention to select isobutanol, t-butanol, and 2-pentanol from the list of possible alcohol compound solvents taught in Makino. Regarding claim 3, modified Platt discloses the method of claim 1 and further discloses wherein contacting the first suspension and the first solution to form a precursor comprises forming a mixture comprising the first suspension and the first solution and mixing and stirring the mixture (see [0023] “precursors to generate the solid electrolyte”; see [0014] “These two solutions require a very short stirring time to produce two homogenous solutions that may be mixed and stirred again to form a final homogeneous mixture of the solid electrolyte solution.”; see [0022] “the two different solutions/suspensions” & “typically, reaction/stir time for each step 120 or step 130 may be between a few minutes and a few hours. Specific reaction/stirring time depend upon the details of the reactants and solvent used including parameters such as initial powder size, total volume, and total solids loading.”; see [0023] “Next, in step 140 the first and second combinations may be mixed for a predetermined period of time and temperature in order to create a solid electrolyte solution. Mixing time is not specifically limited as long as it allows for appropriate homogenization and reaction of precursors to generate the solid electrolyte.”). Regarding claim 4, modified Platt discloses the method of claim 3 and further discloses wherein the mixture is mixed and stirred for a time greater than or equal to about 30 minutes to less than or equal to about 24 hours (see [0022] “Example processes described below indicated various reaction/stirring time.”; see [0023] “Next, in step 140 the first and second combinations may be mixed for a predetermined period of time and temperature in order to create a solid electrolyte solution” & “typically, reaction/stirring time for step 140 may be between a few minutes and a few hours.”; see [0027] Example 3 “stirred for 30 min.”; “stirred for 30 min”; combined and further stirred for 15 mins”). Regarding claim 5, modified Platt discloses the method of claim 1 and further discloses wherein the precursor has a molar ratio of 1:1 of Li2S:P2S5 and Platt also discloses Li3PS4 (see [0018] “approximately 1 mole of Li2S is used for every 1 mole of P2S5 to achieve the desired solution.”; see [0020] “reactants are Li2S and P2S5, Li3PS4”; see [0027] “it should be understood that the present method may include electrolytes with other phases with and without halogen such as compounds: Li3PS4”; see Example 4 “0.615 g of P2S5 was mixed with 0.127 g Li2S in 25 mL ethyl acetate (EA) and stirred for 5 h” & “0.223 g LiCl was mixed with 0.478 g Li2S in 25 mL ethanol and stirred for 5 h” & “Li6PS5Cl argyrodite was the primary phase observed”). Platt does not explicitly disclose wherein the precursor has a 1:1:1 molar ratio of Li3PS4: Li2S: LiX. However, Platt does disclose that ratios and amounts of the various reactions are not limited and may be changed to obtain the appropriate final material stoichiometry (see [0021] “For step 130, the ratios and amounts of the various reactants are not specifically limited, and may be chosen to obtain the appropriate final material stoichiometry.”). Therefore, it would have been prima facie obvious to one of ordinary skill in the art before the effective filing date of the claimed invention to include the precursor has a ratio to obtain the appropriate final material stoichiometry, as suggested by Platt. Doing so would obtain the final material stoichiometry of the Li6PS5CL argyrodite (see P8 Example 4 line 15 “Li6PS5Cl argyrodite was the primary phase observed”), as suggested by Platt. Regarding claim 6, modified Platt teaches the method of claim 1 and further discloses wherein the method further comprises preparing the first suspension, wherein preparing the first suspension comprises: contacting Li2S and P2S5 in the ester solvent to form a mixture (see [0018] “step 120” & “PS43- backbone, in one embodiment, approximately 1 mole of Li2S is used for every 1 mole of P2S5 to achieve the desired solution. The amount of solvent added to the combination is not limited as long as the amount of solvent supports synthesis of the desired composition of solid” & “multiple solvents may be mixed together with the noted reactants” & see [0017] “solvents for use in step 120” & “ester molecules”); and mixing and stirring the mixture (see [0022] “the two different solution/suspensions” & “Typically, reaction/stir time for each step 120 or step 130 may be between a few minutes and a few hours. Specific reaction/stirring time depend upon the details of the reactants and solvent used including parameters such as initial powder size, total volume, and total solids loading”; see P8 Example 4 (Dual Solution Method) “0.615 g of P2S5 was mixed with 0.127 g Li2S in 25 mL ethyl acetate (EA) and stirred for 5 h.”). Platt does not explicitly disclose a time greater than or equal to about 8 hours to less than or equal to about 96 hours. However, Platt does disclose mixing time is not limited as long as it allows for appropriate homogenization and reaction of precursors (see [0023] “in step 140 the first and second combinations may be mixed for a predetermined period of time and temperature in order to create a solid electrolyte solution. Mixing time is not specifically limited as long as it allows for appropriate homogenization and reaction of precursors to generate the solid electrolyte.”). Therefore, it would have been prima facie obvious to one of ordinary skill in the art to include mixing and stirring and a time in order to allow for homogenization, as suggested by Platt. Doing so allows for appropriate reaction of precursors to generate the solid electrolyte, as suggested by Platt. Regarding claim 7, modified Platt discloses the method of claim 1 and further discloses a molar ratio of 1:1 for Li2S:P2S5 (see [0018] and P8 Example 4). Platt discloses a total concentration of the Li2S and the P2S5 in the mixture is greater than or equal to about 0.5 wt. % (see P8 line 20 through line 27 “Example 4 (Dual Solution Method) 0.615 g of P2S5 was mixed with 0.127 g Li2S in 25 mL ethyl acetate (EA) and stirred for 5 h. The Li2S particles were approximately 0.5 mm diameter. 0.223 g LiCl was mixed with 0.478 g Li2S in 25 mL ethanol and stirred for 5 h. The EA and ethanol mixtures were combined and further stirred for 15 min, and then the final mixture was heated at 150 °C under vacuum for 1.5 h to form a ceramic powder. The powder was further heated at 550 °C under flowing argon for 2h. X-ray diffraction analysis was carried out on the powders. Li6PS5Cl argyrodite was the primary phase observed.”). Platt does not explicitly disclose wherein the mixture has a molar ratio of the Li2S and P2S5 greater than or equal to about 2.9 to less than or equal to about 3.1. However, Platt does disclose the ratios and amounts of the various reactants are not limited and may be chosen to obtain the appropriate final material stoichiometry (see [0021] “For step 130, the ratios and amounts of the various reactants are not specifically limited, and may be chosen to obtain the appropriate final material stoichiometry.”). Therefore, it would have been prima facie obvious to one of ordinary skill int the art before the effective filing date of the claimed invention to incorporate ratios and amounts to obtain the appropriate final material stoichiometry, as suggested by Platt. Regarding claim 8, modified Platt discloses the method of claim 1 and further discloses wherein the method further comprises; preparing the first solution, the preparing of the first solution comprising: contacting Li2S and LiX in the alcohol solvent to form a mixture; and mixing and stirring the mixture for a time greater than or equal to about 0.1 hours to less than or equal to about 24 hours (see [0019] “ step 130” & “second reactants may include, for example, Li2S and LiX (X = F, Cl, Br, or I).”; see P8 lines 20-27 “Example 4 (Dual Solution Method) 0.615 g of P2S5 was mixed with 0.127 g Li2S in 25 mL ethyl acetate (EA) and stirred for 5 h. The Li2S particles were approximately 0.5 mm diameter. 0.223 g LiCl was mixed with 0.478 g Li2S in 25 mL ethanol and stirred for 5 h. The EA and ethanol mixtures were combined and further stirred for 15 min, and then the final mixture was heated at 150° C. under vacuum for 1.5 h to form a ceramic powder.”). Platt discloses mixing and stirring for 5 hours which lies within the claimed range of a time greater than or equal to about 0.1 hours to less than or equal to about 24 hours, which renders this claim obvious. Regarding claim 9, modified Platt discloses the method of claim 1 and discloses a molar ratio of 1:1 for Li2S:P2S5 (see P8 lines 20-27 & [0018]). Platt does not explicitly disclose wherein the mixture has a molar ratio of the Li2S and the LiX of greater than or equal to about 0.9 to less than or equal to about 1.1, and a total concentration of the Li2S and the LiX in the mixture is greater than or equal to about 0.1 wt.% to less than or equal to about 20 wt.%. However, Platt does disclose concentration of Li2S and the LiX (see P8 lines 20-27 “Example 4” & “0.615 g of P2S5” & “0.127 g Li2S” & “0.223 g LiCl” & “0.478 g Li2S”; see [0021] “ratios and amounts of the various reactants are not specifically limited, and may be chosen to obtain the appropriate final material stoichiometry”). Therefore, it would have been prima facie obvious to one of ordinary skill in the art before the effective filing date of the claimed invention to incorporate ratios and amounts of various reactants to obtain the appropriate final material stoichiometry, as suggested by Platt. Regarding claim 10, modified Platt discloses the method of claim 1 and further discloses wherein the removing the ester solvent and the alcohol solvent form the precursor solution to form the solid-state argyrodite electrolyte further comprises (see [0014] “The solvents may be removed from the solution by a technique such as vacuum drying to form the final solid electrolyte”; see [0022] “Li6PS5Br argyrodite”; see [0018] “multiple solvents”; see [0017] “ester molecules”; see [0021] “multiple solvents”; see [0020] “second solvents” & “alcohols”) heating the precursor to a temperature greater than or equal to about 80 °C to less than or equal to about 700 °C for a time greater than or equal to about 30 minutes to less than or equal to about 48 hours (see P8 lines 20-27 “Example 4 (Dual Solution Method)” & “and then the final mixture was heated at 150 °C under vacuum for 1.5 h to form a ceramic powder. The powder was further heated at 550 °C. under flowing argon for 2 h.” & “Li6PS5Cl argyrodite was the primary phase observed”). Platt discloses temperature 150 °C and 550 °C which lie within the temperature range of temperature greater than or equal to about 80 °C to less than or equal to about 700 °C, which renders this claim limitation obvious. Platt discloses a time 1.5 h and 2 h which lie within the claimed range of greater than or equal to about 30 minutes to less than or equal to about 48 hours, which renders this claim limitation obvious. Claim 11 is rejected under 35 U.S.C. 103 as being unpatentable over Platt et al. (WO 2020153973 A1, “Platt”) in view of Yamamoto et al. (US 20180062200 A1, “Yamamoto”) and Makino et al. (US 20190198919 A1, “Makino”) as applied to claim 1 above, and further in view of Zhang et al. (Zhixia Zhang, Long Zhang, Yanyan Liu, Chuang Yu, Xinlin Yan, Bo Xu, Li-min Wang, Synthesis and characterization of argyrodite solid electrolytes for all-solid-state Li-ion batteries, Journal of Alloys and Compounds, Volume 747, 2018, Pages 227-235). Regarding claim 11, modified Platt discloses the method of claim 1 and further Platt discloses wherein the solid-state argyrodite electrolyte comprises a plurality of Li6PS5X particles (see [0022] “to form a Li6PS5Br argyrodite”; see [0019] “step 130” & “second reactants may include, for example, Li2S and LiX (X = F, Cl, Br, or I).”; see P8 line 7 “Example 4 (Dual Solution Method)” & P8 line 15 “Li6PS5Cl argyrodite was the primary phase observed”; see [0014] “Described herein are novel soft chemical processes relying upon synthesis methods using multipart solvent/solution based approaches employing selective solvation and/or particle size reduction for different reactants used to form the solid electrolytes”). Platt does not explicitly disclose having an average particle size greater than or equal to about 0.1 micrometer to less than or equal to about 100 micrometers. However, Platt does disclose on P8 line 18 “ionic conductivity of the sample was 1.3 mS/cm.” Platt also discloses “particle size reduction for different reactants used to form the solid electrolyte” in [0014]. Zhang teaches average particle size of Li6PS5Cl is 12 µm (see P230, FIG. 2 “SEM images of the Li6PS5Cl morphology are displayed in Fig. 2” & “the average particle size is 12 µm for the former and 8 µm for the latter sample, thus leading to higher ionic conductivity of the sintered sample than that of the mechanically alloyed sample”). A result effective variable is a variable which achieves a recognized result. The determination of the optimum or workable ranges of a result-effective variable is routine experimentation and therefore obvious. MPEP § 2144.05. Thus, the average particle size is a variable that achieves the recognized result of improved ionic conductivity. That makes the average particle size a result-effective variable. Therefore, it would have been obvious to one of ordinary skill in the art at the time of the invention to routinely experiment with the average particle size and come up with greater than or equal to about 0.1 micrometer to less than or equal to about 100 micrometers. Response to Arguments Applicant’s arguments with respect to claim 1 have been considered but are moot because the new ground of rejection does not rely on any reference applied in the prior rejection of record for any teaching or matter specifically challenged in the argument. 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 SARAH APPLEGATE whose telephone number is (571)270-0370. The examiner can normally be reached Monday - Friday 9:00 am - 5:00 pm ET. 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, Nicole Buie-Hatcher can be reached at (571) 270-3879. 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. /S.A.A./Examiner, Art Unit 1725 /JAMES M ERWIN/Primary Examiner, Art Unit 1725 07/10/2026
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Prosecution Timeline

Show 14 earlier events
Dec 15, 2025
Examiner Interview Summary
Dec 22, 2025
Response Filed
Feb 20, 2026
Non-Final Rejection mailed — §103
Apr 24, 2026
Interview Requested
May 05, 2026
Examiner Interview Summary
May 05, 2026
Applicant Interview (Telephonic)
May 19, 2026
Response Filed
Jul 14, 2026
Final Rejection mailed — §103 (current)

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