Ex Parte Sell et alDownload PDFPatent Trial and Appeal BoardApr 23, 201311481746 (P.T.A.B. Apr. 23, 2013) Copy Citation UNITED STATES PATENT AND TRADEMARKOFFICE 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. 11/481,746 07/05/2006 Amy Sell 06028/6717AUS 5675 20879 7590 04/23/2013 EMCH, SCHAFFER, SCHAUB & PORCELLO CO P O BOX 916 ONE SEAGATE SUITE 1980 TOLEDO, OH 43697 EXAMINER MCCAIG, BRIAN A ART UNIT PAPER NUMBER 1774 MAIL DATE DELIVERY MODE 04/23/2013 PAPER 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. PTOL-90A (Rev. 04/07) UNITED STATES PATENT AND TRADEMARK OFFICE ____________ BEFORE THE PATENT TRIAL AND APPEAL BOARD ____________ Ex parte AMY SELL, TODD COFFMAN, BERNARD M. SHARKEY, RUSSELL P. LEWIS, ANDY LESTER, and DOUGLAS W. FOWLER ____________ Appeal 2012-007581 Application 11/481,746 Technology Center 1700 ____________ Before BRADLEY R. GARRIS, ADRIENE LEPIANE HANLON, and MICHAEL P. COLAIANNI, Administrative Patent Judges. GARRIS, Administrative Patent Judge. DECISION ON APPEAL Appeal 2012-007581 Application 11/481,746 2 Appellants appeal under 35 U.S.C. § 134 from the Examiner's decision rejecting claims 1, 3-7, 9-11, and 13-17. We have jurisdiction under 35 U.S.C. § 6. We AFFIRM. Appellants claim a method which comprises blending a minor amount of biodiesel with a major amount of diesel fuel, agitating the resulting mixture with a mixer during the blending, and "producing a resulting diesel fuel composition without shock crystallization wherein the resulting diesel fuel composition is wax free" (independent claim 1; see also independent claim 3). Appellants also claim a diesel fuel composition produced by such a method (dependent claims 11 and 13) as well as an apparatus for blending a diesel fuel composition (independent claim 14). Representative claim 1 reads as follows: 1. A method for blending a diesel fuel composition while retaining or improving diesel engine performance comprising the steps of: providing a major amount of diesel fuel at a temperature of 32°F or less; blending a minor amount of biodiesel at a temperature above 32°F with the diesel fuel; agitating the resulting mixture with a mixer during the blending; and producing a resulting diesel fuel composition without shock crystallization wherein the resulting diesel fuel composition is wax free. Appeal 2012-007581 Application 11/481,746 3 Under 35 U.S.C. § 102(e), the Examiner rejects claims 1, 3-7, 11, and 13 as anticipated by Copeland (US 2006/0037237 A1 published Feb. 23, 2006) and rejects claims 4 and 5 as anticipated by Copeland as evidenced by Knothe (Gerhard Knothe et al., Biodiesel: The Use of Vegetable Oils and Their Derivatives as Alternative Diesel Fuels (USDA 1994)). Under 35 U.S.C. § 103(a), the Examiner rejects claims 3, 9, 10, and 14-17 as unpatentable over Copeland in view of Woomer (US 5,203,878 issued Apr. 20, 1993) and McCabe (W.L. MCCABE ET AL., UNIT OPERATIONS OF CHEMICAL ENGINEERING 257 (McGraw-Hill 5th ed. 1993)). Appellants separately argue dependent claims 4 and 5 but not the other dependent claims (Br. 5-13). Accordingly, these other dependent claims will stand or fall with their parent independent claims. We sustain the above rejections for the reasons expressed in the Answer and in our Decision on prior appeal 2010-003153 for this application. The following comments are added for emphasis. Appellants reiterate the argument in their prior appeal that Copeland's in line blender and stirrer would cause shock crystallization (see, e.g., id. at 6-7). In support of this argument, Appellants refer generally to the Lewis Declaration of record in this appeal (but not in the prior appeal) (id.). According to Appellants, the Lewis Declaration "shows that Copeland's in line blender and stirrer would cause shock crystallization" (id.). Appellants do not identify with meaningful specificity the Declaration paragraphs which are considered to contain the above showing. Our independent review of this Declaration reveals nothing which specifically addresses Copeland's method and explains why the in line blender and stirrer Appeal 2012-007581 Application 11/481,746 4 used by Copeland would cause shock crystallization. Furthermore and importantly, neither the Brief nor the Declaration addresses the Examiner's reliance on the Figure 1 disclosure of Copeland as disclosing a method which corresponds to the claimed method and which produces a diesel fuel composition with no observable wax (Ans. para. bridging 4-5, 8 (1st full para.)). In addition, neither the Brief nor the Declaration addresses the point made in the prior appeal Decision that Appellants' above argument is contrary to their Specification disclosure of blending and paddle mixer techniques which avoid shock crystallization but which are indistinguishable from the in line blending and stirrer techniques of Copeland (Dec. 4). Appellants' remaining arguments are persuasively rebutted in the Answer and the prior appeal Decision. We emphasize that Appellants have not provided the record of this appeal with any meaningful response to these rebuttals. The decision of the Examiner is affirmed. 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). AFFIRMED bar Copy with citationCopy as parenthetical citation