Prosecution Insights
Last updated: October 25, 2026
Application No. 18/354,927

ELASTICALLY DEFORMABLE FLOW FIELD COMPONENT

Final Rejection §102§103
Filed
Jul 19, 2023
Examiner
BERMUDEZ, CHARLENE
Art Unit
1721
Tech Center
1700 — Chemical & Materials Engineering
Assignee
Hyaxiom Inc.
OA Round
2 (Final)
37%
Grant Probability
At Risk
3-4
OA Rounds
9m
Est. Remaining
63%
With Interview

Examiner Intelligence

Grants only 37% of cases
37%
Career Allowance Rate
31 granted / 84 resolved
-28.1% vs TC avg
Strong +26% interview lift
Without
With
+26.3%
Interview Lift
resolved cases with interview
Typical timeline
4y 0m
Avg Prosecution
28 currently pending
Career history
115
Total Applications
across all art units

Statute-Specific Performance

§101
0.3%
-39.7% vs TC avg
§103
56.2%
+16.2% vs TC avg
§102
24.3%
-15.7% vs TC avg
§112
17.8%
-22.2% vs TC avg
Black line = Tech Center average estimate • Based on career data from 84 resolved cases

Office Action

§102 §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 . Summary Since the Office Action with the mailing date of 05 June 2026, claims 1-7 and 9-10 remain in the application for further examination with full consideration of remarks from applicant. The 102 and 103 rejections are maintained, and responses to applicant’s filed remarks are included in this Office Action. The text of those sections of Title 35, U.S. Code not included in this action can be found in a prior Office action. Claim Rejections - 35 USC § 102 Claims 1-7 and 10 are rejected under 35 U.S.C. 102(a)(2) as being anticipated by Hercz et al (WO 2024/209212 A2). This prior art reference being cited to as Hercz hereinafter in this Office Action. Regarding claim 1, Hercz discloses a flow field component (2512 Fig. 25C; “separator plate 2512” p. 55 L 25), comprising a plate having a first side (the bottom of separator plate 2512 shown in Fig. 25C, or “the protrusions 1337 and ribs 2538 form a convex surface on the second side of the separator plate” p. 55 LL 32-33 with italics added for emphasis on the feature corresponding to the claimed first side of the claimed plate and “the second fluid flow region in a second fluid volume 1365 is defined between the outer surface of the electrochemically active cell area 1350 of the adjacent cell unit and the (concave or depressed side of the) ribs 1337” p. 46 LL 25-27) and an oppositely facing second side (the top of separator plate 2512 shown in Fig. 25C, or “a concave surface on the first side of the separator plate” p. 55 L 33 with italics added for emphasis on the feature corresponding to the claimed second side of the claimed plate and “The concavity forms a first fluid volume 1360” p. 57 L 15 and indicated as 1360 in Fig. 25C), the plate having an undulating profile defining a plurality of segments (2538 Fig. 25C; “ribs 2538” p. 55 L31) and a plurality of channels between the segments (1337 shown in Fig. 25C has a space in its convex portion; “protrusions 1337 define the height of the first fluid flow region 1360” p. 55 L 34-p. 56 L1) on at least the first side of the plate (the height of protrusions 1337 is in the direction upward from the bottom surface of separator plate 2512), the undulating profile including some of the segments in a first reference plane (“The network of interconnected ribs may include end ribs 2538a, b, which are fluidicaliy connected to a protrusion 1337 at only one end” p. 56 LL 5-6, or the distal ends of the network of ribs shown in Fig. 25C) and others of the segments in a second reference plane that is parallel to and spaced from the first reference plane (the plane at a higher elevation than the previously cited end ribs that all of the other ribs in the middle portion of the separator plate 2512 are disposed on). Regarding claim 2, Hercz discloses the flow field component with all the features set forth in claim 1 above, and wherein the some of the segments remain in the first reference plane and the others of the segments remain in the second reference plane in a first condition wherein the plate is under a first compressive load (compressive loads are understood in the art to be a pushing force applied to a structure inwardly – in the case of the Hercz prior art, the corresponding compressive load acts along the thickness direction of the disclosed cell unit 300 in a stack. Therefore, pertaining to this limitation, “a separation between the second side of the separator plate and the first side of the cell layer. In a non-operational mode, when the pressure on each of the first and second sides of the separator plate is the same, the separation may decrease.” p. 19 LL 7-8 where no compressive load is applied because pressure on the top and bottom of the disclosed separator plate is the same and is in a static or net zero condition), the others of the segments being at least partially in the first reference plane in a second condition wherein the plate is under a second compressive load that is greater than the first compressive load (“(for fuel cell operation, for electrolysis cell operation only a first fluid may be provided).” p. 8 LL 19-22 with italics added for emphasis on the corresponding second condition of Hercz such that the net force applied on the disclosed separator plate is in the downward direction of the separator plate shown from the perspective of Fig. 25C). Regarding claim 3, Hercz discloses the flow field component with all the limitations set forth in claim 2 above, and wherein all of the segments are in the first reference plane in the second condition (“The cell stack may also be configured such that the first side of the separator plate contacts an outermost layer of the electrochemically active cell area of an adjacent cell unit, providing electrical contact therebetween and having a contact resistance that decreases as the pressure difference between the first side and the second side of the separator plate increases.” p. 9 LL 25-28, “a higher pressure in the first fluid volume relative to the second fluid volume increases the contact force between the separator plate and the electrochemically active cell area of an adjacent cell unit thereby decreasing the contact resistance” p. 55 LL 16-19, and “By bringing the downward protrusions into contact with the electrochemically active area of an adjacent neighbouring cell unit the contact resistance decreases, i.e. conductivity through the stack is improved.” p. 10 LL 3-5). Regarding claim 4, Hercz discloses the flow field component with all the features set forth in claim 3 above, and wherein the first compressive load corresponds to zero compressive force (as cited in claim 2 above, , “a separation between the second side of the separator plate and the first side of the cell layer. In a non-operational mode, when the pressure on each of the first and second sides of the separator plate is the same, the separation may decrease.” p. 19 LL 7-8 where no compressive load is applied because pressure on the top and bottom of the disclosed separator plate is the same and is in a static or net zero condition), the second compressive load corresponds to at least one of a load associated with positioning the flow field component within an electrolysis assembly and a load associated with operation of the electrolysis assembly (as cited in claim 2 above, “(for fuel cell operation, for electrolysis cell operation only a first fluid may be provided).” p. 8 LL 19-22 with italics added for emphasis on the corresponding second condition of Hercz such that the net force applied on the disclosed separator plate is in the downward direction of the separator plate shown from the perspective of Fig. 25C). Regarding claim 5, Hercz discloses the flow field component with all the features set forth in claim 1 above, and wherein the plate is elastically deformable such that the others of the segments are repeatedly moveable between the first reference plane and the second reference plane (“The separator plate may, for example, be a planar metal sheet that is non-porous, or any other planar sheet that is non-porous, and which acts to separate one ceil unit from an adjacent cell unit in a stack.” p. 57 LL 8-10 where planar metal sheets are known in the art to have properties inherent to the material of being elastically deformable). Regarding claim 6, Hercz discloses the flow field component with all the features set forth in claim 1 above, and including a plurality of second segments and a plurality of second channels on a second side of the plate that is opposite from the first side (the top surface of the ribs 2538 and protrusions 1337 formed in separator plate 2512 shown in Fig. 25C corresponds to the claimed plurality of second segments and plurality of second channels, while the bottom surface of ribs 2538 and protrusions 1337 formed in separator plate 2512 shown in Fig. 25C corresponds to the claimed plurality of segments and plurality of channels as recited in claim 1), wherein at least some of the second segments are at least partially oriented at an oblique angle relative to the first reference plane (the protrusions 1337 closer to the end ribs 2538a, b on the top surface of the separator plate 2512 shown in Fig. 25C is oblique to electrochemically active cell area 1350). Regarding claim 7, Hercz discloses the flow field component with all the features set forth in claim 6 above, and wherein the at least some of the second segments move toward being parallel with the first reference plane when the plate is subjected to a compressive load (“By bringing the downward protrusions into contact with the electrochemically active area of an adjacent neighbouring cell unit the contact resistance decreases, i.e. conductivity through the stack is improved.” p. 10 LL 3-5 and “a higher pressure in the first fluid volume relative to the second fluid volume increases the contact force between the separator plate and the electrochemically active cell area of an adjacent cell unit thereby decreasing the contact resistance” p. 55 LL 16-19). Regarding claim 10, Hercz discloses the flow field component with all the features set forth in claim 1 above, and wherein the plate is stamped into a shape establishing the undulating profile with the segments in the respective reference planes (“a separator plate having a first side and a second side is provided. The separator plate may be produced by cutting or stamping.” p. 57 LL 7-8). Claim Rejections - 35 USC § 103 Claim 9 is rejected under 35 U.S.C. 103 as being unpatentable over Hercz (WO 2024/209212 A2) in view of Ohara et al (US 2004/0170882 A1). The latter prior art reference cited to as Ohara hereinafter in this Office Action. Regarding claim 9, Hercz discloses the fluid flow component with all the features set forth in claim 1 above, but does not disclose wherein the plate comprises a single piece of stainless steel. However, Ohara discloses a fluid flow component comprising a plate (10 Fig. 1; “a corrugated metal plate 10” [0052]) having an undulating profile (“plurality of conductive Separator plates, each comprising a corrugated metal plate having ridges and grooves that are alternately formed in parallel” [0010]). Ohara teaches wherein the plate comprises a single piece of stainless steel (The material used for the corrugated metal plate in accordance with the present invention is preferably a thin plate … such as Stainless Steel” [0049]). Ohara furthermore teaches that stainless steel is a suitable material for single piece undulating plates used as a fluid flow component because of its good electric conductivity properties and is capable of easy formation into the undulating profile by press working or the like ([0049]). Therefore, it would have been obvious for a person having ordinary skill in the art to replace the fluid flow component of Hercz with the fluid flow component of Ohara from the perspective of wherein the plate comprises a single piece of stainless steel, in order to achieve a fluid flow component that has good electric conductivity and has capabilities of being easily formed into the undulating profile by press working or the like. Response to Arguments Applicant's arguments filed 26 August 2026 have been fully considered but they are not persuasive. Applicant appears to remark that Hercz et al (WO 2024/209212 A2) is not prior art because the prior art’s only filing date that is before the instant application’s effective filing date of 19 July 2023 is the foreign priority filing date of 06 April 2023 drawn to GB 202305181 D0 prior art publication, which applicant files a copy of the prior art’s claimed subject matter as a CLM document in the instant application and is referred to as Exhibit A. An application claiming priority under § 119 or § 365(a) is effectively filed as its priority filing date only for subject matter described in the publication of the priority application date, and because the rejection of the instant claim 1 relies on separator plate 2512 and ribs 2538 shown in Fig. 25C of Hercz and GB 202305181 D0 does not disclose a Fig. 25C, separator plate 2512 and ribs 2538 then the Hercz prior art reference is not entitled to the 06 April 2023 filing date. In response to applicant remarks above, the examiner respectfully disagrees on the application of the requirements held by § 119 or § 365(a) concerning effective filing date. § 119 or § 365(a) is only mentioned to require the claimed subject matter to be described in the publication of the priority application date. Exhibit A lists nearly identical claimed subject matter with the exception of clerical differences such as “the electrochemically active cell area” instead of “the cell layer” in claim 1 of GB 202305181 D0 and Hercz, respectively. Moreover, Exhibit A recites “separator plate” and “ribs” as part of the subject matter claimed in GB 202305181 D0. Hercz is therefore entitled to the 06 April 2023 filing date of GB 202305181 D0 because GB 202305181 D0 meets the requirements set forth by § 119 or § 365(a). Conclusion THIS ACTION IS MADE FINAL. 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 CHARLENE BERMUDEZ whose telephone number is (571)272-0610. The examiner can normally be reached Mondays through Thursdays generally from 12 PM to 5 PM Eastern Time. 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, Allison Bourke can be reached at (303) 297-4684. 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. /CHARLENE BERMUDEZ/Examiner, Art Unit 1721 /ALLISON BOURKE/Supervisory Patent Examiner, Art Unit 1721
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Prosecution Timeline

Jul 19, 2023
Application Filed
Jun 02, 2026
Examiner Interview (Telephonic)
Jun 05, 2026
Non-Final Rejection mailed — §102, §103
Aug 26, 2026
Response Filed
Oct 05, 2026
Final Rejection mailed — §102, §103 (current)

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Prosecution Projections

3-4
Expected OA Rounds
37%
Grant Probability
63%
With Interview (+26.3%)
4y 0m (~9m remaining)
Median Time to Grant
Moderate
PTA Risk
Based on 84 resolved cases by this examiner. Grant probability derived from career allowance rate.

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