Ex Parte Meinass et alDownload PDFPatent Trial and Appeal BoardApr 29, 201311493963 (P.T.A.B. Apr. 29, 2013) Copy Citation UNITED STATES PATENT AND TRADEMARK OFFICE ____________ BEFORE THE PATENT TRIAL AND APPEAL BOARD ____________ Ex parte HELMUT MEINASS and ERNST MIKLOS ____________ Appeal 2011-003085 Application 11/493,963 Technology Center 3700 ____________ Before EDWARD A. BROWN, RICHARD E. RICE and CARL M. DeFRANCO, Administrative Patent Judges. DeFRANCO, Administrative Patent Judge. DECISION ON APPEAL Appeal 2011-003085 Application 11/493,963 2 STATEMENT OF THE CASE Appellants appeal under 35 U.S.C. § 134(a) from the Examiner’s final rejection of claims 6, 8-11 and 13-19. App. Br. 2. Claims 1-5, 7, 12 and 20 are cancelled. Id. We have jurisdiction under 35 U.S.C. § 6(b). We REVERSE. CLAIMED INVENTION The claimed invention relates to a method and an apparatus for providing bubble-free liquid carbon dioxide to a user device. Spec. [0002]. Claims 11 and 17 are the only independent claims. We choose claim 17 as illustrative of the claims on appeal: 17. An apparatus for providing bubble-free liquid carbon dioxide to a user device, comprising: a liquid CO2 storage tank; an evaporator coupled to the liquid CO2 storage tank, wherein the evaporator converts liquid CO2 from the liquid CO2 storage tank into gaseous CO2; a gaseous CO2 supply line coupled to the evaporator; a condenser coupled to the gaseous CO2 supply line, wherein the condenser liquefies the gaseous CO2 received from the gaseous CO2 supply line; and a CO2 fluid line disposed between the condenser and the user device, wherein the CO2 fluid line transports the liquefied CO2 from the condenser to the user device. EVIDENCE The Examiner relied upon the following prior art as evidence of unpatentability: Messer US 1,521,385 Dec. 30, 1924 Heichberger US 4,498,303 Feb. 12, 1985 Wikstrom US 2004/0231358 A1 Nov. 25, 2004 Appeal 2011-003085 Application 11/493,963 3 Cryogenic Cooling for Temperature Chambers and Thermal Platforms Explained & Demystified, Sigma Systems Corp., pp. 1-16 (© 2000) (“Cryogenic Cooling”). REJECTIONS 1. Claims 8-11, 13-15, 17-19 stand rejected under 35 U.S.C. § 103(a) as unpatentable over Heichberger and Messer.1 Ans. 4. 2. Claim 6 stands rejected under 35 U.S.C. § 103(a) as unpatentable over Heichberger, Messer and Cryogenic Cooling. Id. at 5. 3. Claims 10, 16 and 18 stand rejected under 35 U.S.C. § 103(a) as unpatentable over Heichberger, Messer and Wikstrom. Id. at 6. ANALYSIS Claim 17 calls for an apparatus comprising, in relevant part, an evaporator for converting liquid carbon dioxide (CO2) to gaseous CO2, a condenser for receiving the gaseous CO2 from the evaporator and liquefying it, and a gaseous CO2 supply line coupled between the evaporator and the condenser. App. Br., Claims Appx. In other words, the phase of the CO2 is transformed twice by the claimed apparatus, first from a liquid-to-gas state and then from a gas-to-liquid state. That the carbon dioxide undergoes two phase transformations is consistent with Appellant's Specification, which provides that: “Figure 1 shows the upright CO2 tank 1, in which liquid CO2 is stored. An evaporator 2 can convert this fluid into its gaseous state. . . . The supply line 6 leads to condenser 8 in which the CO2 is liquefied and then transported to the user by way of a CO2 fluid line 9.” Spec. [0026] (emphasis added). 1 The Examiner rejected apparatus claims 10 and 18 on alternative bases, first, as unpatentable over Heichberger and Messer (Ans. 5), and second, as unpatentable over the same references with the added teaching of Wikstrom (id. at 6). Appeal 2011-003085 Application 11/493,963 4 The Examiner found that Heichberger teaches a condenser for “liquefying [] gaseous CO2 gas received from [a] gaseous CO2 supply line,” but acknowledged that it does not teach an evaporator that “converts liquid CO2 from [a] liquid CO2 storage tank into gaseous CO2.” Ans. 4. For that teaching, the Examiner relied upon Messer, finding that it teaches “an evaporator” for “supply[ing] a liquefied gas to a supply line.” Ans. 4. In essence, the Examiner relied upon Heichberger as teaching the condenser for the gas-to-liquid phase change and Messer as teaching the evaporator for the liquid-to-gas phase change. In justifying the proposed combination, the Examiner found that “Heichberger explicitly requires a source of CO2 gas” and “Messer explicitly teaches a well known means of providing gaseous CO2.”2 Ans. 7. As such, the Examiner concluded that a skilled artisan would have found it obvious to supply the gaseous CO2 required by Heichberger via the system of Messer “for the purpose of providing the required CO2 for the operation of Heichberger” (id.) and for the purpose of “achieving a greater purity carbon dioxide where needed” (id. at 5; see also id. at 7). Appellants contend that the Examiner’s combination of Heichberger and Messer lacks rational basis because neither reference discloses or suggests the double transformation of CO2. App. Br. 2, 4-5. Specifically, Appellants assert that “there is no need for modifying the system of Heichberger by Messer” because Heichberger’s system “only requires supply of gaseous CO2 at one location, i.e., the condenser.” App. Br. 5, 6 (emphasis omitted). Thus, according to Appellants, modifying Heichberger to introduce an additional gaseous CO2 supply, as taught by Messer, “would have no purpose in the system of Heichberger.” Id. at 5. 2 While Appellants make much of Messer’s focus on transformation of “liquid oxygen” (Reply Br. 1-2), we note that it also teaches transformation of “other liquefied gases.” See Messer, col. 2, ll. 76-77 (“The method can be applied also in connection with other liquefied gases”). Appeal 2011-003085 Application 11/493,963 5 Likewise, Appellants contend that the Examiner’s reason of “achieving a greater purity carbon dioxide” would be redundant because “Heichberger already supplies higher CO2 purity to a location that requires it.” Id. at 6 (emphasis added). In other words, Appellants assert that a skilled artisan would not look to Messer because it would be “of no concern, or benefit to Heichberger.” Id. at 7. We agree with Appellants that neither Heichberger nor Messer, as relied on by the Examiner, teaches double transformation of CO2. While each reference teaches a single transformation of CO2 (Heichberger from a gas-to-liquid state and Messer from a liquid-to-gas state), a claimed invention “composed of several elements is not proved obvious merely by demonstrating that each of its elements was, independently, known in the prior art.” KSR Int’l Co. v. Teleflex Inc., 550 U.S. 398, 418 (2007). Rather, the Examiner must “identify a reason that would have prompted a person of ordinary skill in the relevant field to combine the elements in the way the claimed [] invention does.” See id. We agree with Appellants that the Examiner has not identified an adequate reason that would have led a skilled artisan to look to Messer for a gaseous supply for Heichberger. The express purpose of Heichberger’s condenser and associated system is to selectively liquefy contaminated CO2 gas and thereby produce a virtually pure liquid CO2 product. See, e.g., Heichberger, col. 1, ll. 5-10, & col. 2, ll. 9-15. While Heichberger discloses a gaseous supply pipe 52 “connected to a supply (not shown) of gaseous carbon dioxide under pressure” (id. at col. 3, ll. 22- 29), it further discloses that the gaseous CO2 supplied through pipe 52 is contaminated with one or more other gases: Gaseous carbon dioxide containing at least one contaminating gas having a lower liquification temperature than the liquid carbon dioxide, such as oxygen and nitrogen, at a pressure of between Appeal 2011-003085 Application 11/493,963 6 approximately 70 and 1050 psig, having corresponding condensation temperatures of approximately -69.9° and 87.8° F, respectively, preferably between approximately 225 and 300 psig is delivered to the gas distributor 54 through the pipe 52. Id. at col. 4, ll. 21-29 (emphasis added). Thus, Heichberger’s system does not require just any gaseous CO2, as the Examiner suggested in making the asserted combination with Messer. Rather, Heichberger is focused on purifying “gaseous carbon dioxide containing at least one contaminating gas.” See, e.g., id. at col. 1, ll. 7-8, ll. 62-63, and col. 4, ll. 21- 22, ll. 51-52. Heichberger explains that “in order for the carbon dioxide to be of maximum usefulness [for carbonating beverages], it must be as pure as possible, i.e. free of contaminating gas such as oxygen and to a lesser extent nitrogen.” Id. at col. 1, ll. 37-40. In other words, Heichberger’s system requires a supply of contaminated gaseous CO2 that is in need of purification. Nowhere does Messer teach or suggest that its gaseous CO2 output contains contaminants or requires purification. Because Heichberger requires gaseous CO2 that contains “at least one contaminating gas,” a skilled artisan would not have been prompted to look to Messer, which is silent on purity and contaminants. As such, the Examiner's reason for modifying Heichberger to use the gas supply of Messer lacks a rational basis. Without a persuasive articulated reason based on some rational underpinning for modifying the reference as proposed, the Examiner’s rejection cannot stand. See In re Kahn, 441 F.3d 977, 988 (Fed. Cir. 2006) (cited with approval in KSR Int'l Co. v. Teleflex, Inc., 550 U.S. 398, 418 (2007)) (“rejections on obviousness grounds cannot be sustained by mere conclusory statements; instead, there must be some articulated reasoning with some rational underpinning to support the legal Appeal 2011-003085 Application 11/493,963 7 conclusion of obviousness”). Based on the record before us, we fail to see any rational basis that would have led a skilled artisan to look to Messer for the purpose of supplying gaseous CO2 that required greater purity, as the Examiner proposes. The Examiner has not provided us with any findings that Heichberger recognized a problem in its ability to accomplish this function. Accordingly, we cannot sustain the rejection of apparatus claim 17, and its respective dependent claims 8-10, 18 and 19, as unpatentable over Heichberger and Messer. Likewise, we cannot sustain the rejection of method claim 11 and its respective dependent claims 13-15, as they are directed to a method that includes the steps of converting liquid CO2 into gaseous CO2 in an evaporator and then liquefying the gaseous CO2 in a condenser. Dependent claims 6, 10, 16 and 18 The Examiner rejected dependent claim 6 as being unpatentable over Heichberger, Messer, and the additional reference of Cryogenic Cooling, and rejected dependent claims 10, 16 and 18 as being unpatentable over Heichberger, Messer, and the additional reference of Wikstrom. Ans. 5-6. Neither of these additional references cures the above-noted deficiencies with the Examiner’s proposed combination of Heichberger and Messer. Accordingly, for the reasons given with respect to the erroneous rejection of independent claims 11 and 17, we cannot sustain the rejection of dependent claims 6, 10, 16, and 18, which depend from those independent claims. DECISION We reverse the Examiner’s decision rejecting claims 6, 8-11, and 13-19. REVERSED Klh Copy with citationCopy as parenthetical citation