Ex Parte Bhan et alDownload PDFPatent Trial and Appeal BoardMay 30, 201311014365 (P.T.A.B. May. 30, 2013) 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. 11/014,365 12/16/2004 Opinder Kishan Bhan TH2820 (US) 4665 23632 7590 05/30/2013 SHELL OIL COMPANY P O BOX 2463 HOUSTON, TX 77252-2463 EXAMINER SINGH, PREM C ART UNIT PAPER NUMBER 1771 MAIL DATE DELIVERY MODE 05/30/2013 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 OPINDER KISHAN BHAN and SCOTT LEE WELLINGTON ____________ Appeal 2011-012361 Application 11/014,365 Technology Center 1700 ____________ Before CHUNG K. PAK, TERRY J. OWENS, and BEVERLY A. FRANKLIN, Administrative Patent Judges. DECISION ON APPEAL Appellants appeal under 35 U.S.C. § 134 from the Examiner's rejection of claims 1, 2, 4-18, and 46-48. We have jurisdiction under 35 U.S.C. § 6. STATEMENT OF THE CASE Claims 1is representative of the subject matter on appeal and is set forth below: 1. A method of producing a crude product, comprising: Appeal 2011-012361 Application 11/014,365 2 contacting a crude feed with one or more catalysts at a first temperature followed by contacting at a second temperature to produce a total product that includes the crude product, wherein the crude product is a liquid mixture at 25°C at 0.101 MPa, the crude feed having a TAN of at least 0.3 and the crude feed and the crude feed [sic] having a C5 asphaltenes content of at least 0.04 grams of C5 asphaltenes per gram of crude feed; and controlling contacting conditions such that the first contacting temperature is at least 30°C lower than the second contacting temperature, and the crude product has a TAN of at most 90% relative to the TAN of the crude feed, wherein TAN is as determined by ASTM Method 0664 and the C5 asphaltenes content in the crude product is reduced relative to the C5 asphaltenes content of the crude feed as determined by ASTM Method D2007. The prior art relied upon by the Examiner in rejecting the claims on appeal is: Hensley, Jr. 4,395,328 Jul. 26, 1983 Lindsay 4,729,826 Mar. 8, 1988 Halbert 5,910,242 Jun. 8, 1999 THE REJECTIONS 1. Claims 1, 2, and 17 are rejected under 35 U.S.C. §102(b) as anticipated by Lindsay, as evidenced by Halbert and Hensley. 2. Claims 4-16, 18, and 46-48 are rejected under 35 U.S.C. §103(a) over Lindsay in view of Halbert and Hensley. Appeal 2011-012361 Application 11/014,365 3 ISSUE Did the Examiner err in determining that Lindsay anticipates the claimed subject matter, and in particular, the aspect of claim 1 pertaining to (1) the “crude feed having a TAN of at least 0.3”; (2) the “crude feed having a C5 asphaltenes content of at least 0.04 grams of C5 asphaltenes per gram of crude feed”; (3) the “crude product has a TAN of at most 90% relative to the TAN of the crude feed”; and (4) the “C5 asphaltenes content in the crude product is reduced relative to the C5 asphaltenes content of the crude feed”? We answer this question in the affirmative and REVERSE. ANALYSIS The Examiner acknowledges that Lindsay does not disclose items 1-4 as listed above. With regard to the claimed TAN value (item (1)) and the reduction of the TAN value (item (3)), the Examiner states that a “typical crude is expected to inherently contains TAN and reduction of TAN during contacting with the catalyst”. Ans. 5. The Examiner relies upon Halbert for teaching that a typical crude contains TAN of 1 to 8. Id. However, Appellants rightly point out that Halbert is directed to “acidic crudes”. Halbert, col. 2, ll. 10-11. Br. 8-9. Appellants also rightly point out that Lindsay’s hydrocarbon-treated oil includes, broadly, all liquid and liquid/vapor hydrocarbon mixtures. Lindsey, col. 3, ll. 44-53. Br. 8. With regard to the claimed C5 asphaltenes content of at least 0.04 grams (item (2)), the Examiner relies upon Lindsay for disclosing crude feed Appeal 2011-012361 Application 11/014,365 4 having an asphaltene content of at least 0.213 grams per gram of crude feed as found in Table IX of Lindsay. Ans. 4-5. However, as the Examiner admits on page 11 of the Answer, Lindsay’s disclosure of the asphaltene content concerns the total asphaltene content, and thus, there is no indication of the content of C5 asphaltenes. Hence, the claimed element of “a C5 asphaltenes content of at least 0.04 grams of C5 asphaltenes per gram of crude feed” is not disclosed. Halbert and Hensley, Jr. also do not teach this element, and the Examiner does not rely upon them in this regard (the Examiner relies upon Hensley for teaching item (4), and relies upon Halbert as discussed, supra). Ans. 5-6. The above-mentioned record leads us to agree with Appellants, for at least the reasons set forth in their Brief, that a prima facie case of anticipation has not been satisfied. Not only is a claimed element missing from Lindsey, the reference must “direct those skilled in the art to the compound without any need for picking, choosing, and combining various disclosures not directly related to each other.” In re Arkley, 455 F.2d 586, 587 (CCPA 1972). This is not the case in the record before us for the reasons discussed, supra. In view of the above, we therefore reverse Rejection 1. With regard to Rejection 2, because Halbert and Hensley, Jr. do not cure the deficiencies of Lindsay, we also agree with Appellants’ position for at least the reasons set forth in the Brief on pages 13-15, and reverse Rejection 2. CONCLUSIONS OF LAW AND DECISION Each rejection is reversed. Appeal 2011-012361 Application 11/014,365 5 REVERSED tc Copy with citationCopy as parenthetical citation