Ex Parte Zia et alDownload PDFPatent Trial and Appeal BoardSep 6, 201311174602 (P.T.A.B. Sep. 6, 2013) 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. 11/174,602 07/06/2005 Jalal Hunain Zia 21500 2156 27182 7590 09/06/2013 PRAXAIR, INC. LAW DEPARTMENT - M1-04 39 OLD RIDGEBURY ROAD DANBURY, CT 06810-5113 EXAMINER PETTITT, JOHN F ART UNIT PAPER NUMBER 3744 MAIL DATE DELIVERY MODE 09/06/2013 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 JALAL HUNAIN ZIA, NANCY JEAN LYNCH, JOHN HENRI ROYAL, THURMAN GORDON, RICHARD JOHN JIBB, and BARRY ALAN MINBIOLE ____________________ Appeal 2011-009919 Application 11/174,602 Technology Center 3700 ____________________ Before: PHILLIP J. KAUFFMAN, CHARLES N. GREENHUT, and PATRICK R. SCANLON, Administrative Patent Judges. KAUFFMAN, Administrative Patent Judge. DECISION ON APPEAL Appeal 2011-009919 Application 11/174,602 2 STATEMENT OF CASE Appellants appeal under 35 U.S.C. § 134 from the Examiner’s decision to reject claims 9-12 and 14. We have jurisdiction under 35 U.S.C. § 6(b). We affirm. The Invention Appellants’ claimed invention “relates generally to tank systems for the containment and the dispensing of cryogenic liquids.” Spec., para. [0001]. Claim 9 is the sole independent claim on appeal and is reproduced below: 9. A method for operating a cryogenic tank system comprising: withdrawing a liquid cryogen stream from a primary tank, passing the liquid cryogen stream through a cryocooler and subcooling the liquid cryogen stream within the cryocooler to produce subcooled liquid cryogen; passing a subcooled liquid cryogen stream composed of the subcooled liquid cryogen from the cryocooler into an auxiliary tank that is separate from the cryocooler so that the sub cooled liquid cryogen collects within the auxiliary tank; pressurizing the subcooled liquid cryogen collected within the auxiliary tank to an auxiliary tank pressure; passing a pressurized liquid cryogen stream, composed of the subcooled liquid cryogen, from the auxiliary tank into a location of the primary tank having a primary tank pressure and under impetus of the auxiliary tank pressure; and the auxiliary tank pressure decreasing as the pressurized liquid cryogen stream is passed from Appeal 2011-009919 Application 11/174,602 3 the auxiliary tank into the primary tank such that when the auxiliary tank pressure is below the primary tank pressure, flow of the pressurized liquid cryogen stream ceases and the liquid cryogen is passed from the primary tank to the cryocooler and the subcooled liquid cryogen stream is in turn passed to the auxiliary tank. Evidence Relied Upon Hansen Tyree US 2,964,918 US 5,934,095 Dec. 20, 1960 Aug. 10, 1999 The Rejections The following rejections are before us on appeal: I. Claims 9-12 under 35 U.S.C. § 102(b) as anticipated by Tyree. II. Claims 10 and 14 under 35 U.S.C. § 103(a) as unpatentable over Tyree and Hansen. OPINION I. Anticipation by Tyree Claim 9 The Examiner’s determination that Tyree discloses the method of claim 9 includes a finding that Tyree discloses a cryocooler (evaporator 78 and compressor 79), and a finding that Tyree discloses an auxiliary tank (batch pressure transfer system, an alternative embodiment of pump 84) that passes a pressurized liquid cryogen stream (in line 85) from that auxiliary tank (of the batch pressure transfer system) to the primary tank (inner vessel 11'). Ans. 3-4 (citing Tyree, col. 10, ll. 8-14). Appeal 2011-009919 Application 11/174,602 4 Appellants’ arguments are prefaced by a description of the operation of Tyree’s system that includes reference to pump 84. Br. 8-9. The Examiner did not rely upon Tyree’s pump 84 in the rejection of claim 9. Ans. 3-4. Rather, the Examiner relied upon Tyree’s batch pressure transfer system, an alternative embodiment of pump 84, as corresponding to the claimed auxiliary tank. Ans. 4, 7; see Tyree, col. 10, ll. 8-12. The failure to address the rejection as articulated by the Examiner runs throughout Appellants’ arguments. Appellants make several arguments that Tyree’s evaporator 78 does not correspond to the claimed auxiliary tank. Specifically, Appellants argue that Tyree does not disclose passing a pressurized liquid cryogen stream from the auxiliary tank into the primary tank as claimed because the flow of cryogen to and from evaporator tank 78 is controlled by level controllers 82a and 82b. Br. 9. Appellants also argue that Tyree’s tank 78 is not separate from the cryocooler. Br. 10. Additionally, Appellants argue that Tyree does not disclose pressurizing the subcooled liquid cryogen collected within the auxiliary tank to an auxiliary tank pressure as claimed, because Tyree’s evaporator tank 78 is never appreciably pressurized. Br. 10. This line of argument is unpersuasive because the Examiner interpreted that Tyree’s batch pressure transfer system corresponds as the claimed auxiliary tank, not evaporator 78. Ans. 4, 7. Two other arguments regarding evaporator 78 merit further analysis. First, Appellants argue that the Examiner’s finding that Tyree discloses passing subcooled liquid cryogen from the bottom of tank 78 into an auxiliary tank (batch pressurization transfer system) is incorrect because Tyree discloses that cold vapor is passed from a condenser 36’ to tank 78. Appeal 2011-009919 Application 11/174,602 5 Br. 10. This argument is based upon an erroneous factual premise. Specifically, Tyree does not disclose passing cold vapor from condenser 36’ to evaporator 78. Tyree, fig. 2. More importantly, this argument is nonresponsive because the Examiner did not find that Tyree discloses that vapor from condenser 36’ is passed to tank 78. Rather, the Examiner found that Tyree discloses that CO2 vapor from condenser 36’ is used by (transferred to) the batch transfer pressurization system. Ans. 6, 12; see also Tyree, col. 10, ll. 8-11. Second, Appellants argue that Tyree does not disclose passing a subcooled liquid cryogen stream from a cryocooler into an auxiliary tank as claimed because Tyree’s evaporator tank 78 performs evaporative cooling. Br. 9. Tyree’s compressor 79 removes vapor from evaporator 78, causing evaporative cooling of the liquid CO2 in evaporator 78. Tyree, col. 9, ll. 60- 63. However, the fact that Tyree’s cryocooler (compressor 79 and evaporator 78) performs evaporative cooling does not demonstrate that Tyree does not disclose passing a subcooled liquid cryogen stream from a cryocooler (compressor 79 and evaporator 78) into an auxiliary tank (batch pressure transfer system). See Ans. 3-4. As such, Appellants have not apprised us of error in the rejection of claim 9. Regarding claims 10-12, Appellants merely recite what the claim calls for and repeat the arguments used for claim 9. Br. 11-12. Our analysis of claim 9, supra, applies equally well to these claims. Appeal 2011-009919 Application 11/174,602 6 II. Obviousness over Tyree and Hansen Claim 10 Appellants argue that claim 10 depends from claim 1 and is allowable on the same basis as claim 1. Br. 13. We presume Appellant meant claim 9, not claim 1, because claim 10 depends from claim 9. Such arguments are unconvincing for the reasons given in the analysis of claim 9 as anticipated by Tyree, supra. Appellants argue that modifying Tyree so that liquid is pressurized in the auxiliary tank “is not an obvious modification of Tyree given that the rise in pressure within the evaporation tank 78 would raise the temperature of the cryogen.” Br. 13. Such argument is not responsive because the Examiner relied upon Tyree’s batch pressurization transfer system as corresponding to the claimed auxiliary tank, not evaporator 78. Ans. 3-4, 7- 9. As such, Appellants have not apprised us of error in the rejection of claim 10. Claim 14 Claim 14 depends from claim 9 and recites “wherein some of the subcooled liquid cryogen passed into the auxiliary tank is vaporized, and the resulting vapor is passed into the primary tank.” The Examiner found that Tyree disclosed the method of claim 14 except Tyree does not explicitly state that the subcooled liquid cryogen collected within the auxiliary tank is vaporized and the passed into the primary tank. Ans. 6. The Examiner concluded that it would have been obvious to employ the pressure building tank (container 16) of Hanson in the Appeal 2011-009919 Application 11/174,602 7 cryogenic system of Tyree for the purpose of pressurizing the batch transfer system in a simple and well-known manner that avoids additional and longer piping from condenser 36’. Id. Appellants present three arguments. First, Appellants repeat the arguments for claim 9. Br. 13. These arguments are unconvincing for the reasons given in the analysis of claim 9, supra. Second, Appellants argue that the configuration of Hansen’s system would not permit the gas in the pressure building circuit to be passed to another tank. Br. 13. We agree with the Examiner that the rejection incorporates Hansen’s pressure building circuit into Tyree’s system and does not rely upon the remaining configuration of Hansen. Ans. 16-17. As such, this contention is not persuasive.Third, Appellants argue that the proposed modification would not have been obvious because vapor from condenser 36’ is needed to perform evaporative cooling of tank 78. Br. 14. As explained in the analysis of claim 9, supra, Tyree’s compressor 79 removes vapor from evaporator 78, causing evaporative cooling of the liquid CO2 in evaporator 78. Tyree, col. 9, ll. 60- 63. Tyree does not disclose that vapor from condenser 36’ is utilized for evaporative cooling of the contents of evaporator 78. Further, the Examiner has not proposed to replace the line from condenser 36’ to evaporator 78. Instead, the Examiner proposed to replace the line from condenser 36’ to the batch pressure transfer system. See Ans. 6-7, 16-17. As such, we sustain the rejection of claim 14. Appeal 2011-009919 Application 11/174,602 8 DECISION We affirm the Examiner’s decision to reject 9-12 and 14. No time period for taking any subsequent action in connection with this appeal may be extended under 37 C.F.R. § 1.136(a). See 37 C.F.R. § 1.136(a)(1)(iv). AFFIRMED Klh/rvb Copy with citationCopy as parenthetical citation