Ex Parte GunnermanDownload PDFBoard of Patent Appeals and InterferencesApr 23, 200911059115 (B.P.A.I. Apr. 23, 2009) Copy Citation UNITED STATES PATENT AND TRADEMARK OFFICE ________________ BEFORE THE BOARD OF PATENT APPEALS AND INTERFERENCES ________________ Ex parte RUDOLF W. GUNNERMAN ________________ Appeal 2009-2140 Application 11/059,115 Technology Center 1700 ________________ Decided:1 April 23, 2009 ________________ Before TERRY J. OWENS, LINDA M. GAUDETTE, and MICHAEL P. COLAIANNI, Administrative Patent Judges. OWENS, Administrative Patent Judge. DECISION ON APPEAL STATEMENT OF THE CASE 1 The two-month time period for filing an appeal or commencing a civil action, as recited in 37 C.F.R. § 1.304, begins to run from the Decided Date shown on this page of the decision. The time period does not run from the Mail Date (paper delivery) or Notification Date (electronic delivery). Appeal 2009-2140 Application 11/059,115 The Appellant appeals under 35 U.S.C. § 134(a) from the Examiner’s rejection of claims 1, 5-8 and 10-13, which are all of the pending claims. We have jurisdiction under 35 U.S.C. § 6(b). The Invention The Appellant claims a process for converting components of a petroleum or petroleum fraction feedstock to products having lower boiling points than those of the components. Claim 1 is illustrative: 1. A process for treating a feedstock consisting of petroleum or a fraction thereof to convert components of said feedstock to products having boiling points that are lower than the boiling points of said components, said method comprising: (a) combining said feedstock with an aqueous liquid at a (feedstock):(aqueous liquid) volume ratio of from about 20:1 to about 1:2 to form an emulsion, (b) exposing said emulsion to ultrasound, (c) subsequent to step (b), irradiating said emulsion with microwave radiation to separate said emulsion into aqueous and organic phases, and (d) recovering said organic phase, wherein steps (b) and (c) are performed continuously in flow-through reactors. The References Wolf 4,582,629 Apr. 15, 1986 Gregoli 5,110,443 May 5, 1992 2 Appeal 2009-2140 Application 11/059,115 The Rejection Claims 1, 5-8 and 10-13 stand rejected under 35 U.S.C. § 103 over Gregoli in view of Wolf.2 OPINION We affirm the Examiner’s rejection. Except for claim 11, the Appellant argues the claims as a group (Br. 7, Reply Br. 5-6). We therefore limit our discussion to claim 11 and one claim in the argued group, i.e., claim 1, which is the sole independent claim. See 37 C.F.R. § 41.37(c)(1)(vii) (2007). Claim 1 Issue Has the Appellant shown reversible error in the Examiner’s determination that the applied references would have rendered prima facie obvious, to one of ordinary skill in the art, exposing a feedstock/aqueous liquid emulsion to ultrasound continuously in a flow-through reactor, and then irradiating the emulsion with microwave radiation continuously in a flow-through reactor to separate the emulsion into aqueous and organic phases? Findings of Fact Gregoli forms an oil-in-water emulsion, especially for pipeline transmission, by mixing a hydrocarbon with water and an emulsifying agent and heating the mixture to about 100 to about 200 °F (col. 1, ll. 25-27; col. 2, ll. 35-40). The emulsion’s water content is about 15 to about 60 wt% 2 An obviousness-type double patenting rejection of claims 1-13 over U.S. Application 10/803,802 is withdrawn in the Examiner’s Answer in view of the Appellant’s filing of a terminal disclaimer on April 4, 2008 (Ans. 2). 3 Appeal 2009-2140 Application 11/059,115 (col. 2, ll. 40-45; col. 8, ll. 41-44). The emulsion can be pumped continuously through an ultrasonic reactor at a residence time of 1 second to several minutes to convert heavy hydrocarbons, crudes and the like into lighter products (col. 67, ll. 38-42; col. 68, ll. 47-56). The reacted emulsion exiting the ultrasonic reactor passes through a gas/liquid separator where gaseous reaction products are separated from the bulk emulsion, and then demulsifying chemicals are added to the emulsion and it is heated to 150- 300°F to break the oil/water emulsion (col. 69, ll. 1-7). Wolf discloses “enhancing separation of oil and water emulsions and dispersions by treating the same with microwave radiation, whether alone or in conjunction with more conventional separating devices” (col. 1, ll. 12-15). The “[m]icrowave treatment disrupts the emulsion and allows for more rapid separation of the oil and water” (col. 3, ll. 6-8). “[H]ydrocarbon and water emulsions and dispersions can be separated and the separation can be enhanced by the application of microwave radiation in the range of from 1 millimeter to 30 centimeters for a time sufficient to separate the dispersion or emulsion to the extent desired” (col. 2, ll. 15-20). “Normally the microwave radiation will be used only for a short period of time, and the emulsion or dispersion will be heated to separation temperature by conventional means” (col. 2, ll. 21-23). “The power used will range from a level of from about 300 to about 50,000 watts” (col. 2, ll. 42-44), and “normally the higher the wattage used to produce the microwave radiation, the more quickly the dispersion or emulsion can be separated” (col. 2, ll. 40- 42). Wolf’s process is effective for oil external emulsions or dispersions containing more than 50 wt% oil, and water external emulsions or dispersions containing about 1 to about 50 wt% oil (col. 3, ll. 15-16, 24-30). 4 Appeal 2009-2140 Application 11/059,115 The microwaves can be used either directly in a tank to generate heat and interfacial disruption, or in a section of the flow line just ahead of the tank (col. 3, ll. 35-40). Analysis The Appellant argues that Wolf’s emulsions result from mere mixing of oil and water, and that one of ordinary skill in the art would not have expected Wolf’s microwaves to be effective for breaking Gregoli’s ultrasonic-treated emulsion (Br. 5; Reply Br. 4). One of ordinary skill in the art, the Appellant argues, would have expected that Gregoli’s heating in the presence of a demulsifying agent would be needed to break Gregoli’s ultrasonic-treated emulsion which, the Appellant asserts, is more difficult to break than Wolf’s emulsion. See id. Wolf’s disclosures that the “[m]icrowave treatment disrupts the emulsion and allows for more rapid separation of the oil and water” (col. 3, ll. 6-8) and that the microwave treatment can be used in conjunction with more conventional separating devices (col. 1, ll. 12-15) would have led one of ordinary skill in the art, through no more than ordinary creativity, to use Wolf’s microwave treatment in conjunction with Gregoli’s heating in the presence of a demulsifying agent to disrupt the emulsion and allow for more rapid separation of the oil and water. See KSR Int’l. Co. v. Teleflex Inc., 550 U.S. 398, 418 (2007) (In making an obviousness determination one “can take account of the inferences and creative steps that a person of ordinary skill in the art would employ”). The Appellant’s “comprising” transition term opens the claims to additional steps such as Gregoli’s heating in the presence of a demulsifying agent. See In re Baxter, 656 F.2d 679, 686 (CCPA 1981). Moreover, Wolf does not indicate that the microwave 5 Appeal 2009-2140 Application 11/059,115 treatment is limited to simple oil/water mixtures such that one of ordinary skill in the art would have expected it to be ineffective for breaking an ultrasonic-treated emulsion, especially at Wolf’s disclosed power of 50,000 watts (col. 2, ll. 39-44). The Appellant has provided mere attorney argument to that effect, and such argument of counsel cannot take the place of evidence. See In re De Blauwe, 736 F.2d 699, 705 (Fed. Cir. 1984). The Appellant argues that although Wolf discloses that the emulsion can be oil-external (water-in-oil), in Wolf’s examples water is the much larger phase (oil-in-water) and, consequently, one of ordinary skill would not have expected Wolf’s microwave treatment to be effective for Gregoli’s water-in-oil emulsion (Br. 6). Wolf’s disclosure that the emulsion can be oil external or water external (col. 3, ll. 15-16 and 24-30) would have indicated to one of ordinary skill in the art that the disclosed microwave treatment is applicable to both water-in-oil and oil-in-water emulsions. Furthermore, in Wolf’s Example 1 the emulsion is a water-in-oil emulsion (3:7 water:oil ratio) (col. 4, ll. 15- 18). The Appellant argues, regarding Wolf’s disclosure that “[f]or continuous treatment, a power level of from about 1 watt to about 500 watts per gallon of emulsion or dispersion will be used” (col. 2, ll. 46-48), that Wolf does not describe what “continuous” means (Br. 6). The Appellant argues that Wolf’s term “continuous” means relatively continuous or uninterrupted treatment as opposed to intermittent treatment. See id. Wolf does not limit the term “continuous” to relatively continuous. The ordinary meaning of “continuous” is “marked by uninterrupted 6 Appeal 2009-2140 Application 11/059,115 extension in space, time, or sequence”.3 Hence, Wolf’s term “continuous” appears to refer to uninterrupted microwave treatment, such as in the flow- through reactor recited in the Appellant’s claim 1. The Appellant argues that “[a]s shown by the use of the word ‘tank’, Wolf refers to the use of microwaves in a line leading to a bulk reactor, not their use in a continuous-flow reactor” (Br. 7). Wolf discloses that the microwaves can be used either directly in a tank or in a section of the tank’s flow line (col. 3, ll. 35-38). The disclosure that microwaves can be used in a section of the tank’s flow line would have indicated to one of ordinary skill in the art that emulsion is flowing through the line and that, accordingly, when microwaves are used directly in the tank emulsion also is flowing through the line, i.e., the tank is a continuous flow- through reactor. Conclusion of Law The Appellant has not shown reversible error in the Examiner’s determination that the applied references would have rendered prima facie obvious, to one of ordinary skill in the art, exposing a feedstock/aqueous liquid emulsion to ultrasound continuously in a flow-through reactor, and then irradiating the emulsion with microwave radiation continuously in a flow-through reactor to separate the emulsion into aqueous and organic phases. 3 Webster’s New Collegiate Dictionary 246 (G. & C. Merriam 1973). 7 Appeal 2009-2140 Application 11/059,115 Claim 11 Issue Has the Appellant shown reversible error in the Examiner’s determination that the applied references would have rendered prima facie obvious, to one of ordinary skill in the art, a microwave exposure time of from about 0.1 second to about 1 second? Analysis The Appellant argues that a treatment time of 1 second is much shorter than Wolf’s exemplified times of 20 and 30 seconds (Table 1, col. 4, ll. 35-37) (Br. 7: Reply Br. 5-6). Wolf’s disclosure is not limited to the working examples. See In re Fracalossi, 681 F.2d 792, 794 n.1 (CCPA 1982); In re Kohler, 475 F.2d 651, 653 (CCPA 1973); In re Mills, 470 F.2d 649, 651 (CCPA 1972); In re Bozek, 416 F.2d 1385, 1390 (CCPA 1969). Instead, all disclosures in the reference must be evaluated for what they would have fairly suggested to one of ordinary skill in the art. See In re Boe, 355 F.2d 961, 965 (CCPA 1966). Wolf’s disclosures that the microwave treatment is for a normally short time sufficient to separate the emulsion or dispersion to the extent desired (col. 2, ll. 16-22), the microwave treatment power can be as high as 50,000 watts (col. 2, ll. 42-44), and “normally the higher the wattage used to produce the microwave radiation, the more quickly the dispersion or emulsion can be separated” (col. 2, ll. 40-42) would have led one of ordinary skill in the art, through no more than ordinary creativity, to use combinations of power and time such as high power and short time (e.g., 1 second) to separate the emulsion to the extent desired. See KSR, 550 U.S. at 418. 8 Appeal 2009-2140 Application 11/059,115 Conclusion of Law The Appellant has not shown reversible error in the Examiner’s determination that the applied references would have rendered prima facie obvious, to one of ordinary skill in the art, a microwave exposure time of from about 0.1 second to about 1 second. DECISION/ORDER The rejection of claims 1, 5-8 and 10-13 under 35 U.S.C. § 103 over Gregoli in view of Wolf is affirmed. It is ordered that the Examiner’s decision 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). AFFIRMED ssl TOWNSEND AND TOWNSEND AND CREW, LLP TWO EMBARCADERO CENTER EIGHTH FLOOR SAN FRANCISCO CA 94111-3834 9 Copy with citationCopy as parenthetical citation