Ex Parte De Rezende Pinho et alDownload PDFBoard of Patent Appeals and InterferencesMay 24, 201210480966 (B.P.A.I. May. 24, 2012) 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. 10/480,966 06/03/2004 Andrea De Rezende Pinho APB2880-FCC 9029 56744 7590 05/25/2012 Albemarle Netherlands B.V. Patent and Trademark Department 451 Florida Street Baton Rouge, LA 70801 EXAMINER SINGH, PREM C ART UNIT PAPER NUMBER 1771 MAIL DATE DELIVERY MODE 05/25/2012 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 BOARD OF PATENT APPEALS AND INTERFERENCES ____________________ Ex parte ANDREA DE REZENDE PINHO, EDISSON MORGADO JUNIOR, MARLON BRANDO DE ALMEIDA, PAUL O'CONNOR, and PIETER IMHOF ____________________ Appeal 2010-007964 Application 10/480,966 Technology Center 1700 ____________________ Before CATHERINE Q. TIMM, MICHAEL P. COLAIANNI, and GEORGE C. BEST, Administrative Patent Judges. TIMM, Administrative Patent Judge. DECISION ON APPEAL Appellants appeal under 35 U.S.C. § 134 from the Examiner’s decision to reject claims 1-3, 5, 6, and 8-13 under 35 U.S.C. § 103(a) as obvious over Morgado1 in view of Bourgogne2. We have jurisdiction under 35 U.S.C. § 6(b). We AFFIRM. 1 Morgado et al., BR: PI 9704925-5A, pub. May 11, 1999. 2 Bourgogne et al., US 5,660,716, patented Aug. 26, 1997. Appeal 2010-007964 Application 10/480,966 2 The claims are directed to a process for fluid catalytic cracking (FCC) of hydrocarbon feeds in a downflow reactor using a specified cracking catalyst (Spec. 1:14-15). Appellants do not argue any claim apart from the others (Br. 8-9). We select claim 1 as representative for deciding the issues on appeal. Claim 1 reads as follows: 1. A process for the fluid catalytic cracking of hydrocarbons comprising the following steps: a) atomizing and injecting a hydrocarbon feedstock into the top portion of a tubular downflow reactor and contacting this hydrocarbon feedstock with a catalyst having an AAI of at least 3.5, b) separating reaction products and spent catalyst at the bottom of said downflow reactor, c) treating the spent catalyst with steam, d) regenerating the spent catalyst in a regeneration zone, and e) recycling the regenerated catalyst to the downflow reactor; wherein the catalyst comprises 10-60 wt. % of a solid acid, 0-50% wt. % of alumina, 0-40% wt. % of silica, and the balance kaolin. (Claims App. at Br. A-1.) Appellants use a catalyst having an AAI of at least 3.5 in their FCC process. According to the Specification, “[t]he AAI is a measure of the accessibility of the catalyst pores to large, often high-molecular weight compounds” (Spec. 4:8-9). “The higher the AAI value, the more accessible the catalyst pores are.” (Spec. 4:19.) The Specification states that Appeal 2010-007964 Application 10/480,966 3 “[s]uitable methods for the preparation of such highly accessible catalysts include the methods disclosed in Brazilian patent publication BR PI 9704925-5A” (Spec. 7:1-2). The Brazilian patent publication referenced by the Specification is Morgado, the primary reference applied by the Examiner to reject the claims. In FCC processes using downflow reactors, the catalyst and the hydrocarbon feed flow downward (Spec. 1:20-22). However, according the Specification, while downflow reactors were known in the art, upflow or riser reactors where the catalyst and the hydrocarbon flow upward were more typically used. (Spec. 1:19-20.) There is no dispute that Morgado describes a known catalyst for FCC with the composition and AAI recited in claim 1, and that Bourgogne describes a downflow fluidized bed for such FCC processes. Appellants’ own Specification indicates as much (see, e.g., Spec. 2:24-26 discussing US 5,660,716 (Bourgogne); Spec. 7:1-4 discussing BR PI 9704925-5A (Morgado)). While we agree with Appellants that Morgado does not describe using the catalyst of that reference in a downflow reactor, we cannot say that this fact negates the other facts found by the Examiner establishing that it would have been obvious to one of ordinary skill in the art to have used the known FCC catalyst of Morgado in a known downflow reactor such as that taught by Bourgogne. The combination would have been merely the use of a known FCC catalyst in a known FCC process. One would have expected to obtain the known benefits associated with the catalyst along with the known benefits associated with the downflow reactor. “The combination of familiar Appeal 2010-007964 Application 10/480,966 4 elements according to known methods is likely to be obvious when it does no more than yield predictable results.” KSR Int'l Co. v. Teleflex Inc., 550 U.S. 398, 416 (2007). Appellants contend that the catalyst and reactor combination provides synergistic, unexpected and superior results (Br. 8-9). Appellants point to data discussed in Tables 2 and 4 of their Specification to support their argument (id.). Table 2 displays the results of a FCC process using a riser reactor and a FCC process using a downflow reactor (Spec. 9:5-6 and 9:15-16). Both reactors are run at constant coke production and with conventional catalyst (id.). Table 2 shows that the downflow reactor results in improved conversion levels, improved selectivity to C3 olefins, and improved hydrogen selectivity, but that the downflow reactor results in worse bottoms conversion (bottoms of 13.0 wt% vs. 11.6 wt% in riser reactor) (Br. 8; Spec. 9:15-20 and Table 2). In contrast, according to Appellants, using Appellants’ catalyst having an AAI of greater than 3.5 in a downflow reactor results in a significant increase in bottoms conversion as shown in Table 4 (Br. 8-9). Table 4 reports results for two downflow processes, one using a catalyst with an AAI of 6.0 and the other using a catalyst with AAI of 2.0. The AAI 6.0 catalyst (E1D) has a better bottoms conversion (8.4 wt% bottoms) as compared to the AAI 2.0 catalyst (14.7 wt% bottoms). We agree with the Examiner, however, that the evidence as a whole indicates that better bottoms conversion would have been expected rather than unexpected (Ans. 10 and 12). “[A]ny superior property must be Appeal 2010-007964 Application 10/480,966 5 unexpected to be considered as evidence of non-obviousness.” Pfizer, Inc. v. Apotex, Inc., 480 F.3d 1348, 1371 (Fed. Cir. 2007). As pointed out by the Examiner, Morgado discloses that the controlled porosity of the higher AAI catalyst provides greater accessibility of the reagent molecules to the active components of the zeolite catalyst, and also facilitates the rapid diffusion of the cracking products, thus avoiding over-cracking and the formation of undesirable products such as coke (Ans. 10, Morgado, p. 4, ll. 15-22). The ordinary artisan would have expected to obtain increased bottoms conversion with Morgado’s catalyst because the larger molecules would have better access to the active material in the catalyst. One would have expected to obtain both the known benefits of the downflow reactor and the known benefits of the catalyst when the two are used together. Appellants do not offer any convincing evidence of what results would have been expected by the combination, and, therefore, a comparison of expected properties to the results reported in Table 4 is not possible. Moreover, we note that Appellants’ assertion of unexpected results is merely made in the Brief. There is no statement in the Specification that the results are unexpected. Appellants’ assertion in the Brief is insufficient to establish non-obviousness. See In re Mayne, 104 F.3d 1339, 1343-44 (Fed. Circ. 1997) (noting that an unsupported assertion is insufficient to make a showing that “the claimed invention exhibits some superior property or advantage that a person of ordinary skill in the relevant art would find surprising or unexpected.”); In re Geisler, 116 F.3d 1465, 1471 (Fed. Cir. 1997) (explaining that argument by counsel cannot take the place of evidence). Appeal 2010-007964 Application 10/480,966 6 Therefore, Appellants have not met their burden of showing that the results would have been so significantly better than what would have been expected from the combination that the results would have been unexpected by the ordinary artisan. CONCLUSION We sustain the Examiner’s rejection. DECISION The Examiner’s decision is affirmed. TIME PERIOD FOR RESPONSE 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 cam Copy with citationCopy as parenthetical citation