JX NIPPON OIL & ENERGY CORPORATIONDownload PDFPatent Trials and Appeals BoardMay 4, 202015054610 - (D) (P.T.A.B. May. 4, 2020) Copy Citation UNITED STATES PATENT AND TRADEMARK OFFICE UNITED STATES DEPARTMENT OF COMMERCE United States Patent and Trademark Office Address: COMMISSIONER FOR PATENTS P.O. Box 1450 Alexandria, Virginia 22313-1450 www.uspto.gov APPLICATION NO. FILING DATE FIRST NAMED INVENTOR ATTORNEY DOCKET NO. CONFIRMATION NO. 15/054,610 02/26/2016 Yasushi Sato 0079558-000104 4198 21839 7590 05/04/2020 BUCHANAN, INGERSOLL & ROONEY PC POST OFFICE BOX 1404 ALEXANDRIA, VA 22313-1404 EXAMINER WILKINS III, HARRY D ART UNIT PAPER NUMBER 1796 NOTIFICATION DATE DELIVERY MODE 05/04/2020 ELECTRONIC Please find below and/or attached an Office communication concerning this application or proceeding. The time period for reply, if any, is set in the attached communication. Notice of the Office communication was sent electronically on above-indicated "Notification Date" to the following e-mail address(es): ADIPDOC1@BIPC.com PTOL-90A (Rev. 04/07) UNITED STATES PATENT AND TRADEMARK OFFICE ____________ BEFORE THE PATENT TRIAL AND APPEAL BOARD ____________ Ex parte YASUSHI SATO, KOTA MIYOSHI, KOJIRO NAKAGAWA, YOSHIHIRO KOBORI, and SHINJI OSHIMA ____________ Appeal 2019-003947 Application 15/054,610 Technology Center 1700 ____________ Before JEFFREY T. SMITH, AVELYN M. ROSS, and MERRELL C. CASHION, JR., Administrative Patent Judges. CASHION, Administrative Patent Judge. DECISION ON APPEAL STATEMENT OF THE CASE Pursuant to 35 U.S.C. § 134(a), Appellant1 appeals from the Examiner’s decision to reject claims 1–8. We have jurisdiction under 35 U.S.C. § 6(b). We AFFIRM. 1 We use the word “Appellant” to refer to “applicant” as defined in 37 C.F.R. § 1.42. Appellant identifies the real party in interest as JX NIPPON OIL & ENERGY CORPORATION. Appeal Br. 2. Appeal 2019-003947 Application 15/054,610 2 The invention relates to an electrochemical reduction device for hydrogenating an aromatic compound. Spec. ¶ 1. The reduction device comprises an intermediate layer between a diffusion layer and a reduction electrode catalyst layer. Id. ¶ 9. The intermediate layer allows for water to be easily retained in a proton conductive portion such as the ionomer (electrolyte) in the reduction electrode catalyst layer and the cathode side of the electrolyte membrane. Id. ¶ 32. Thereby, this facilitates the proton reduction reaction at the reduction electrode side more easily in an environment in which a large amount of aromatic compound is present. Id. ¶ 37. Claim 1 illustrates the subject matter on appeal and is reproduced below: 1. An electrochemical reduction device comprising: an electrolyte membrane having proton conductivity; a reduction electrode including a reduction electrode catalyst layer that is provided in contact with one major surface of the electrolyte membrane and has an electron conductive material and a metal containing one or both of Pt and Pd supported by the electron conductive material, a diffusion layer that is provided near to the other major surface of the reduction electrode catalyst layer, the other major surface being opposite to the electrolyte membrane, and that causes a liquid aromatic compound and a hydride of the aromatic compound to pass through, and an intermediate layer provided between the diffusion layer and the reduction electrode catalyst layer, the intermediate layer is configured to cause the liquid aromatic compound and the hydride of the aromatic compound to pass through and to suppress liquid water from passing through; an oxygen generating electrode provided in contact with the other major surface of the electrolyte membrane; Appeal 2019-003947 Application 15/054,610 3 a raw material supplier that supplies the aromatic compound in a liquid state to the reduction electrode; a moisture supplier that supplies water or humidified gas to the oxygen generating electrode; and a power controller that externally applies an electric field such that the reduction electrode has an electronegative potential and the oxygen generating electrode has an electropositive potential. The Examiner maintains the rejection of claims 1–8 under 35 U.S.C. § 103 as unpatentable over Pintauro (US 6,218,556 B1, issued April 17, 2001), Anderson (US 2003/0230495 A1, published December 18, 2003), Park (Sehkyu Park et al., “Effect on PTFE Content in Microporous Layer on Water Management,” ECS Transactions, 11 (1) 623-628 (2007) 10.1149/1.2780975), and Weber (Adam Z. Weber & John Newman, “Effects of Microporous Layers in Polymer Electrolyte Fuel Cells,” Journal of The Electrochemical Society, 152 (4) A677-A688, 2005). Final Act. 4–7; Ans. 3–6. Appellant does not argue any claim separate from the other. Accordingly, we select claim 1 as representative of the subject matter claimed and decide all issues as to this appeal based on the arguments as applied to claim 1. OPINION After review of the respective positions the Appellant presents in the Appeal and Reply Briefs and the Examiner presents in the Final Office Action and the Answer, we AFFIRM the Examiner’s prior art rejection for the reasons the Examiner presents. Our reasoning follows. Appeal 2019-003947 Application 15/054,610 4 Claim 1 recites an electrochemical reduction device comprising an intermediate layer provided between a diffusion layer and a reduction electrode catalyst layer, where the intermediate layer is configured to cause the liquid aromatic compound and the hydride of the aromatic compound to pass through to the catalyst layer while suppressing liquid water from passing through to the diffusion layer. See Spec. ¶ 37. The Examiner finds Pintauro teaches an electrochemical reduction device for the hydrogenation of an aromatic compound that differs from the claimed invention in that Pintauro does not disclose using an intermediate layer between the diffusion layer and the reduction electrode catalyst layer as claimed. Final Act. 4–5. The Examiner also finds Pintauro recognizes that cathode (reduction electrode) flooding by water caused by electroosmotic drag could be a potential problem in the device that results in the lack of access of aromatic compounds to catalyst regions in the reaction zone where hydrogen generation occurs. Final Act. 5; Pintauro col. 6 ll. 3– 9, Fig. 3. Citing to Anderson, the Examiner explains that the electro- osmotic flux causes some water molecules to be transported via electro- osmosis with the hydrogen ions through a proton exchange membrane from the anode side to the cathode side. Final Act. 5; Anderson Fig. 9, ¶¶ 40, 41. To address this difference from the claimed invention, the Examiner turns to Park and Weber. The Examiner finds that Park teaches that it is known to provide a microporous layer (dense (intermediate) layer) between a catalyst layer and a diffusion layer to increase the catalyst utilization and improve water management in the membrane-electrode assembly. Final Act. 5; Park 623–624. The Examiner also finds that Park discloses that the tested microporous layers increased the resistance to water flow through the gas Appeal 2019-003947 Application 15/054,610 5 diffusion layer. Ans. 7; Park 627. The Examiner further finds that Weber teaches the use of microporous layers (dense (intermediate) layers) between an electrode catalyst and a gas diffusion layer to improve water management within a PEM cell by keeping water away from the diffusion layer. Final Act. 6; Weber Abstr., Figure 1. The Examiner finds that Weber teaches the use of the microporous layers to prevent catalyst layers from becoming entrenched in the diffusion media, a condition that hinders their overall activity and accessibility. Ans. 7–8; Weber A677. The Examiner determines that it would have been obvious to one of ordinary skill in the art to modify Pintauro’s electrochemical reduction device by incorporating a microporous layer between a catalyst layer and a diffusion layer, as taught by Park and Weber, to improve the performance of Pintauro’s electrochemical device because the microporous layer would prevent water from reaching the diffusion layer while increasing catalyst utilization. Final Act. 6. Appellant does not contest the Examiner’s specific findings with respect to Pintauro. Appeal Br. 4. Instead, Appellant argues that both Park and Weber relate to fuel cells which generate water at the cathode electrode while Pintauro relates to an electrochemical reduction device where a reduction occurs at the cathode without water generation. Id. at 4–5. Thus, Appellant contends that there is a need to remove the water to suppress flooding at the cathode electrode. Id. at 4. According to Appellant, Park and Weber provide a microporous layer between a diffusion layer and a catalyst layer to manage the water in the electrode to prevent flooding. Id. Appellant contends that Park achieves this by using the microporous layer to promote the movement of water from the catalyst layer to the diffusion layer Appeal 2019-003947 Application 15/054,610 6 while Weber uses the microporous layer to drive water away from the cathode catalyst layer to the anode. Id. at 5. Therefore, Appellant asserts that the Examiner failed to provide a factual finding that adopting the MPL described in Park or Weber in the Pintauro device would be reasonably expected to achieve the results desired in Pintauro. Appeal Br. 6. Appellant’s arguments do not identify error in the Examiner’s determination of obviousness. The Examiner finds Pintauro recognizes that cathode (reduction electrode) water flooding is caused by electroosmotic drag and creates a potential problem in the device that results in the lack of access of aromatic compounds to catalyst regions in the reaction zone where hydrogen generation occurs. Final Act. 5; Pintauro col. 6 ll. 3–9, Fig. 3. The Examiner further explains that electro-osmotic flux causes some water molecules to be transported via electro-osmosis with the hydrogen ions through a proton exchange membrane from the anode side to the cathode side. Final Act. 5; Anderson Fig. 9, ¶¶ 40, 41. Thus, contrary to Appellant’s argument that Pintauro’s electrochemical reduction device does not generate water (Appeal Br. 4–5), there is a reasonable basis for one skilled in the art to expect Pintauro’s device to experience the detrimental effect from water molecules transported via electro-osmosis through a proton exchange membrane from the anode side to the cathode side. Park and Weber provide a means to prevent this transportation of water to the cathode side. Thus, Appellant’s arguments do not address adequately this analysis by the Examiner. While Appellant asserts that nothing in Anderson discloses or suggests using a microporous layer to control bidirectional water flux (Reply Appeal 2019-003947 Application 15/054,610 7 Br. 7), the Examiner relies on Anderson solely to establish water would be transported to the cathode of Pintauro’s device via electroosmotic flux. Again, Appellant’s arguments do not address the reasons for which the Examiner relies on Anderson. Appellant contends that the use of a dense (intermediate) layer as claimed provides an advantage over the prior art of maintaining a certain amount of moisture in the reduction electrode catalyst layer and, thus, the electrolyte membrane and the reduction electrode catalyst layer are suppressed from being dried and the hydride-producing reaction for an aromatic compound can be further promoted. Appeal Br. 6; Spec. ¶ 46. The burden of establishing unexpected results rests on the Appellant. Appellant may meet this burden by establishing that the difference between the claimed invention and the closest prior art was an unexpected difference. See In re Klosak, 455 F.2d 1077, 1080 (CCPA 1972). The unexpected results must be established by factual evidence; attorney statements are insufficient to establish unexpected results. See In re Geisler, 116 F.3d 1465, 1470–71 (Fed. Cir. 1997). In this case, Appellant does not direct us to any objective evidence in support of the alleged unexpected results. Appellant, at most, has provided mere attorney arguments and such arguments of counsel cannot take the place of evidence. See In re De Blauwe, 736 F.2d 699, 705 (Fed. Cir. 1984); In re Payne, 606 F.2d 303, 315 (CCPA 1979). Therefore, we agree with the Examiners’ determination that Appellant has not met the burden of establishing unexpected results. Ans. 8–9. Appeal 2019-003947 Application 15/054,610 8 Accordingly, we AFFIRM the Examiner’s prior art rejection of claims 1–8 under 35 U.S.C. § 103 for the reasons the Examiner presents and we give above. CONCLUSION In summary: Claims Rejected 35 U.S.C. § Basis Affirmed Reversed 1–8 103 Pintauro, Anderson, Park, Weber 1–8 No time period for taking any subsequent action in connection with this appeal may be extended under 37 C.F.R. § 1.136(a)(1)(iv). AFFIRMED Copy with citationCopy as parenthetical citation