Ex Parte Yada et alDownload PDFBoard of Patent Appeals and InterferencesJul 28, 201010853199 (B.P.A.I. Jul. 28, 2010) Copy Citation UNITED STATES PATENT AND TRADEMARK OFFICE __________ BEFORE THE BOARD OF PATENT APPEALS AND INTERFERENCES __________ Ex parte SHUHEI YADA, KENJI TAKASAKI, YASUSHI OGAWA, and YOSHIRO SUZUKI __________ Appeal 2009-012733 Application 10/853,199 Technology Center 1600 __________ Before ADRIENE LEPIANE HANLON, DEMETRA J. MILLS, and KAREN M. HASTINGS, Administrative Patent Judges. MILLS, Administrative Patent Judge. DECISION ON APPEAL1 This is an appeal under 35 U.S.C. § 134. The Examiner has rejected the claims for obviousness. We have jurisdiction under 35 U.S.C. § 6(b). 1 The two-month time period for filing an appeal or commencing a civil action, as recited in 37 C.F.R. § 1.304, or for filing a request for rehearing, as recited in 37 C.F.R. § 41.52, begins to run from the “MAIL DATE” (paper delivery mode) or the “NOTIFICATION DATE” (electronic delivery mode) shown on the PTOL-90A cover letter attached to this decision. Appeal 2009-012733 Application 10/853,199 2 STATEMENT OF CASE The following claim is representative. 1. A process for producing (meth)acrylic acid which comprises a (meth)acrylic acid-yielding reaction step in which a starting compound for (meth)acrylic acid production is subjected to an oxidation reaction, a distillation step in which light matters are separated from the liquid reaction mixture from the (meth)acrylic acid-yielding reaction step to obtain crude (meth)acrylic acid, a step in which by-products generated in the reaction step and distillation step are pyrolyzed to recover (meth)acrylic acid, and a step in which the (meth)acrylic acid recovered is supplied to the distillation step, characterized in that the temperature for the pyrolysis of the by-products is from 140 to 240°C and the pressure for the pyrolysis is from 70 to 130 kPa. Cited References Sato et al. US 4,317,926 Mar. 2, 1982 Uemura et al. US 6,252,110 B1 Jun. 26, 2001 Grounds of Rejection Claims 1-4 are rejected under 35 U.S.C. § 103(a), as being unpatentable for obviousness over Uemura in view of Sato. Discussion ISSUE The Examiner concludes that Uemura teaches the method for recovering acrylic acid obtained from the gas-phase catalytic oxidation, which is involved in the use of the pyrolyzing tank at temperatures of 120°C to 220°C, whereas Sato et al expressly teaches the process for recovering the acrylic acid from the by-product mixture produced by the catalytic vapor Appeal 2009-012733 Application 10/853,199 3 phase oxidation reaction of propylene or acrolein by using the decomposition evaporator at temperatures of 120-220°C and at pressures of 20-500 mmHg (2.7-67 pKa). Both prior art processes are commonly involved with the recovery process of acrylic acid using the pyrolyzing tank under a similar reaction condition (i.e. temperature). Therefore, it would have been obvious to the skilled artisan in the art to be motivated to incorporate Sato's et al cracking pressure into the Uemura et al process in order to achieve the optimum pressure for the pyrolysis because the skilled artisan in the art would expect the incorporation of Sato's et al cracking pressure knowledge into the Uemura's et al pyrolysis to be successful and effective for the process as shown in the Sato et al process. Appellants contend that Uemura fails to disclose the claimed pyrolysis pressure, and the pressure disclosed by Sato is outside the claimed pressure of 70-130kPa. There is no dispute that it would have been obvious to one of ordinary skill in the art to carry out the process of Uemura at a pressure within the range disclosed in Sato. Rather, the issue in this appeal is whether the cited references render obvious the claimed pyrolysis pressure. FINDINGS OF FACT 1. The Examiner finds that Uemura et al teaches a method for recovering acrylic acid obtained from the gasphase catalytic oxidation in the following step (see co1.3, lines 15-45): (1) introducing said high boiling impurities containing acrylic acid dimcr, acrylic acid and maleic acid into an acrylic acid recovery column composed of a distillation column equipped with a thin film vaporizer, wherein conducting distillation under conditions of 10 to 100 mmHg and at the Appeal 2009-012733 Application 10/853,199 4 bottom temperature of the column of 60 to 120° C., distilling acrylic acid off from the column top and recovering the same; (2) introducing bottom liquid A from said thin film vaporizer into a pyrolizing tank, whererat decomposing acrylic acid dimer in said bottom liquid A at temperatures of 120 to 220° C.; and thereafter (3) recirculating at least a part of bottom liquid B of said pyrolyzing tank into said thin film vaporizer and/or the distillation column, at a ratio of 1 to 20 times the high boiling impurities containing acrylic acid dimer, acrylic acid and maleic acid. (Ans. 4.) 2. The Examiner finds that “the instant invention differs from the prior art in that the claimed pressure for the pyrolysis is from 70 to 130 kpa.” (Id.) 3. The Examiner finds that Sato et al teaches a process for recovering the acrylic acid from the by-product mixture produced by the catalytic vapor phase oxidation reaction of propylene or acrolein which is concentrated in a bottom liquor of a final step rectification tower for acrylic acid; furthermore, the by-product mixture is thermally decomposed to efficiently recover them as acrylic acid (see col. 1, lines 12-19). (Ans. 5.) 4. The Examiner finds that, in Sato, “operation conditions of the decomposition evaporator, [include] a heating temperature ranges 120- 220°C and the operating pressure ranges 20-500 mmHg (2.7-67 pKa) (see from col. 5, line 66 to col. 6, line 2).” (Id.) 5. The Examiner finds that “[w]ith respect to the cracking pressure difference between the prior art and the instant invention, the claimed ranges and the prior art do not overlap but are very close enough that one skilled Appeal 2009-012733 Application 10/853,199 5 artisan in the art would have expected them to have the similar reaction condition.” (Ans. 5.) PRINCIPLES OF LAW In order to determine whether a prima facie case of obviousness has been established, we consider the factors set forth in Graham v. John Deere Co., 383 U.S. 1, 17 (1966): (1) the scope and content of the prior art; (2) the differences between the prior art and the claims at issue; (3) the level of ordinary skill in the relevant art; and (4) objective evidence of nonobviousness, if present. In Titanium Metals v. Banner, 778 F.2d 775, 783 (Fed. Cir. 1985) it was held that where the proportions of alloys are so close that prima facie one skilled in the art would have expected to them to have the same properties, they were considered to be obvious from known alloys. “Although it is well settled that comparative test data showing an unexpected result will rebut a prima facie case of obviousness, the comparative testing must be between the claimed invention and the closest prior art.” In re Fenn, 639 F.2d 762, 765 (CCPA 1981). ANALYSIS We agree with the Examiner’s fact finding, statement of the rejection and responses to Appellants’ argument and adopt them as our own. We provide the following additional comment. Appellants contend that Uemura fails to disclose the claimed pyrolysis pressure, and the pressure disclosed by Sato is outside the claimed pressure of 70-130kPa. Appellants argue that comparative example 1 (pyrolysis Appeal 2009-012733 Application 10/853,199 6 pressure of 27 kPa) of the application demonstrates that at lower pressures as in Sato the system is subject to apparatus clogging. (App. Br. 6.) The Examiner contends that the Appellants have arbitrarily selected 27 kPa from the range of pressures disclosed in Sato. The Examiner points out that Sato expressly discloses a pressure as high as 67 kPa. The Examiner explains that the difference between the prior art pressure (67 kPa) and the claimed pressure (70 kPa) is as little as 3 kPa which is so close that one of ordinary skill in the art would have expected the two pressures to achieve the same results. (Ans. 9-10.) We conclude that the Examiner has established a prima facie case of obviousness on the evidence before us which has not been rebutted by Appellants with evidence. Appellants argue that In re Sebek, 175 USPQ 93, 95 (CCPA 1972) is controlling here and that the prior art discloses that the determination of optimum values outside the disclosed range of Sato, according to Sebek, may not be obvious. (Reply Br. 5.) We are not persuaded. The issue in this case does not involve optimization. Rather, this case is similar to the situation in Titanium Metals. That is, the pressure value of 70 kPa in the claimed method is so close to 67 kPa pressure in the process of Sato, that prima facie one skilled in the art would have expected the claimed process to be obvious and produce the same results as the process suggested by the prior art combination of Uemura and Sato. Appellants do not provide any evidence to the contrary. As noted by the Court in KSR, 550 U.S. 398, 418 (2007), “[a] person of ordinary skill is also a person of ordinary creativity, not an automaton.” 550 U.S. at 418. We conclude that the pressure value of Sato and that Appeal 2009-012733 Application 10/853,199 7 claimed are so close that one of ordinary skill in the art would have expected that the pressure of Sato would have provided the same or substantially the same results to the claimed pressure. We have no sufficient comparative evidence showing an unexpected result. For the reasons set forth above, the obviousness rejection is affirmed. CONCLUSION OF LAW The cited references support the Examiner’s obviousness rejection and disclose a pyrolysis pressure so close as to be obvious. No time period for taking any subsequent action in connection with this appeal may be extended under 37 C.F.R. § 1.136(a). AFFIRMED cdc OBLON, SPIVAK, MCCLELLAND MAIER & NEUSTADT, L.L.P. 1940 DUKE STREET ALEXANDRIA, VA 22314 Copy with citationCopy as parenthetical citation