DETAILED ACTION
Notice of Pre-AIA or AIA Status
The present application, filed on or after March 16, 2013, is being examined under the first inventor to file provisions of the AIA .
Specification
The disclosure is objected to because of the following informalities: on the top of page 8, “V4” is unclear whether it should be – V3--.
Appropriate correction is required.
Res
Claim Rejections - 35 USC § 103
The following is a quotation of 35 U.S.C. 103 which forms the basis for all obviousness rejections set forth in this Office action:
A patent for a claimed invention may not be obtained, notwithstanding that the claimed invention is not identically disclosed as set forth in section 102, if the differences between the claimed invention and the prior art are such that the claimed invention as a whole would have been obvious before the effective filing date of the claimed invention to a person having ordinary skill in the art to which the claimed invention pertains. Patentability shall not be negated by the manner in which the invention was made.
Claim(s) 20-21, 24-26, 29-32, 35-37 is/are rejected under 35 U.S.C. 103 as being unpatentable over Palmer (2023/0092811) in view of Porter (3575521) and any of Dittman (7251942), Smith (3238993) and/or Firey (5031397). Palmer [particularly, Fig. 6] teaches (20) A method of starting a liquid hydrogen fueled gas turbine engine of an aircraft propulsion system, the aircraft propulsion system comprising: a hydrogen storage tank 104 configured to store liquid hydrogen; a liquid hydrogen pump 301 or 607 configured to pump hydrogen in at least a liquid state; a core combustor 207 configured to receive hydrogen fuel from the hydrogen fuel pump 301 or 607; a pre-heater combustor 302, 207 404 [Fig. 4] downstream in hydrogen fuel flow of the liquid hydrogen pump 301 or 607; a core compressor 202 or 204 configured to provide pressurized air to the core combustor 207 and to the pre-heater combustor [air to 405 in Fig. 4; air 653 to 302 in Fig. 6]; and a hydrogen fuel vent [e.g. 633, 634, 635, 636; alternate vent is 631 - when pump is 607] provided downstream of the liquid hydrogen pump 301 or 607, and configured to selectively vent hydrogen fuel; the method comprising: in a liquid priming step, flowing hydrogen from the hydrogen storage tank 104 through the liquid hydrogen pump 301 or 607 [see e.g. ¶ 0167-0171] and the pre-heater combustor 302, 207 404 [done prior to startup and during startup, see ¶ 0118, 0121-0126], then, in a liquid pumping step, operating the liquid hydrogen pump to pump liquid hydrogen to the core combustor 207 at a required flow rate and pressure for engine ignition in an engine ignition step [¶ 0171-0172]. (31) An aircraft propulsion system comprising a hydrogen fueled gas turbine engine, the propulsion system comprising: a hydrogen storage tank 104 configured to store liquid hydrogen; a liquid hydrogen pump 301 or 607 configured to pump hydrogen in at least a liquid state; a core combustor 207 configured to receive hydrogen fuel from the hydrogen fuel pump 301 or 607; a pre-heater combustor 302, 207 404 [Fig. 4] downstream in hydrogen fuel flow of the liquid hydrogen pump 301 or 607; a core compressor 202 or 204 configured to provide pressurized air to the core combustor 207 and to the pre-heater combustor [air to 405 in Fig. 4; air 653 to 302 in Fig. 6]; and a hydrogen fuel vent [e.g. 633, 634, 635, 636; alternate vent is 631 - when pump is 607] provided downstream of the liquid hydrogen pump, and configured to selectively vent hydrogen fuel; an engine start controller 613 configured to: in a liquid priming step, flow hydrogen from the hydrogen storage tank 104 through the liquid hydrogen pump 301 or 607 and the pre-heater combustor 302, 207 404 [done prior to startup and during startup, see ¶ 0118, 0121-0126] then, in a liquid pumping step, operate the liquid hydrogen pump to pump liquid hydrogen to the core combustor 207 at a required flow rate and pressure for engine ignition in an engine ignition step. (21, 32) wherein the liquid hydrogen pump comprises one of a positive displacement pump wherein the positive displacement pump is a piston pump, and a variable displacement pump wherein the variable displacement pump is a centrifugal or axial flow pump [see ¶ 0113]. (24, 35) wherein the pre-heater 302 comprises a heat exchanger configured to heat hydrogen fuel flow with heated exhaust flow. (25, 36) wherein the vent [e.g. 634, 635] is provided downstream in hydrogen fuel flow of the pre-heater 302, and upstream in hydrogen fuel flow of the core combustor 207. (26, 37) wherein the hydrogen storage tank 104 is configured to store hydrogen at an above-ambient pressure, and is configured to store hydrogen at a pressure between 1 and 4 Bar [¶ 0108]. (29) wherein the method comprises, during the liquid pumping step, prior to the ignition step, operating the liquid hydrogen pump to provide liquid hydrogen to the core combustor 207 at a pressure greater than the compressor delivery pressure prior to the ignition step [inherent, fuel pressure to the combustor 207 must be greater than compressor delivery pressure supplied by the combustor 207 in order for fuel to flow into the combustor 207]. (30) wherein the method comprises operating the gas turbine engine at a minimum overall pressure ratio at idle greater than a hydrogen storage tank 104 pressure, wherein an overall pressure ratio at idle of 4 bar or greater [note that the disclosed hydrogen storage pressure may as low as 1 bar, which is around atmospheric pressure, and any compression from the high pressor compressor at idle is many times higher than atmospheric pressure / 1 bar by the nature of compression; alternately, even the italicized range is virtually inherent, the examiner takes official notice that the high pressure compressors typically operate at much higher pressures than 4 bar at idle, e.g. above 30 bar are common ranges in aircraft gas turbines. To the point not already inherent, it would have been obvious to one of ordinary skill in the art to employ an overall pressure ratio at idle of 4 bar or greater, as an obvious matter of using the workable ranges in the art]. Note that Palmer teaches flowing / flow hydrogen from the hydrogen storage tank through the liquid hydrogen pump but do not teach in the liquid priming step, venting / vent hydrogen through the hydrogen fuel vent until the hydrogen pump is primed with liquid hydrogen. However, Porter teaches in the liquid priming step, flowing / flow liquid from the liquid storage tank 11 through the liquid pump 16-18 and teach venting / vent through the vent 45 until the liquid pump 16-18 is primed with liquid where the vent 45 provided is downstream of the liquid pump. Porter teaches that the vent valve is open during the priming to vent any gases during the priming [col. 3, line 69 - col. 4, line 35] which facilitates having only liquid flow through the pump. It would have been obvious to one of ordinary skill in the art to apply this liquid priming technique to Palmer, by venting / vent hydrogen through the hydrogen fuel vent until the hydrogen pump is primed with liquid hydrogen, as taught by Porter, as venting through the vent until the pump is primed with liquid facilitates priming of the pump and having only liquid flow through the pump.
As for crank(ing) the core compressor to generate sufficient compressed airflow and pressure to support combustion within the pre-heater combustor, before or during flowing / flow hydrogen from the hydrogen storage tank through the liquid hydrogen pump and the pre-heater combustor, it is noted that the flowing / flow hydrogen from the hydrogen storage tank through the liquid hydrogen pump and the pre-heater combustor occurs prior to start-up was already taught, Palmer already teaching flowing / flow hydrogen from the hydrogen storage tank 104 through the liquid hydrogen pump 301 or 607 [see e.g. ¶ 0167-0171] and the pre-heater combustor 302, 207 404 [done prior to startup and during startup, see ¶ 0118, 0121-0126]. As for crank(ing) the compressor 102 to generate sufficient compressed airflow and pressure to support combustion within the pre-heater combustor 104, before flowing fuel to the pre-heater combustor 104, it noted that Dittmar et al teach crank(ing) [108 in motor mode turns the compressor 102, see col. 7, lines 15-32; col. 4, lines 43-45] the compressor 102 to generate sufficient compressed airflow and pressure to support combustion within the [pre-heater] combustor 104, and flowing fuel to the [pre-heater] combustor 104. Smith teaches cranking the core compressor 34 to generate sufficient compressed airflow and pressure to support combustion within the [pre-heater] combustor 30, and flowing fuel from the fuel storage tank 38 through the liquid fuel pump 40 and [pre-heater] combustor 30. Smith teaches that the fuel injection is after the initiation of the cranking of the core compressor, so as to prevent explosions from excessive fuel – see col. 1, lines 12+. While the combustors 104, 30, respectively, of Dittmar et al et al and Smith are core combustors, their teachings are applicable to the pre-heater combustor of Palmer, which also utilizes compressed air to operate and start. Alternately, Firey teaches crank(ing) the core compressor 1 to generate sufficient compressed airflow 13 and pressure to support combustion within the pre-heater combustor 12 [col. 7, lines 36-55] prior to steady state operation of the core “combustors” 5, 6 [see col. 3, lines 3-17] and flowing fuel from the fuel storage tank [implied or obvious, compare with other applied art which uses a tank to supply the liquid fuel, e.g. Smith, Palmer, etc.] through the liquid fuel pump 23 and the pre-heater combustor 12 [col. 8, line 49-col. 9, line 5. Firey teaches this sequence is the typical starting sequence during liquid fuel priming step. It would have been obvious to one of ordinary skill in the art to employ crank(ing) the core compressor to generate sufficient compressed airflow and pressure to support combustion within the pre-heater combustor, during the liquid priming step, as taught by any of Dittmar et al, Smith, and/or Firey, as they teach the cranking of the compressor is done to ensure sufficient compressed air is for combustion of the [pre-heater] combustor and where Smith and Firey specifically teach compressor cranking is required prior to fuel delivery to the [pre-heater] combustor as the typical sequence utilized in the art for safety and for priming / supplying the liquid fuel. It would have been obvious to be cranking the compressor prior to flowing the hydrogen through the liquid fuel pump and pre-heater combustor, during the liquid priming step, in order to ensure that the compressed air is available for combustion within the pre-heater combustor before the fuel is delivered thereto.
Response to Arguments
Applicant's arguments filed 4/02/2026 have been fully considered but they are not persuasive.
Applicant argues
“Claim 20, and similarly claim 31, recites in part: (a) a pre-heater combustor downstream in hydrogen fuel flow of the liquid hydrogen pump;
(b) a core compressor configured to provide pressurized air to the
core combustor and to the preheater; and
(c) in a liquid priming step, cranking the core compressor to
generate sufficient compressed airflow and pressure to support
combustion within the preheater combustor” . Palmer and Porter do not teach or suggest at least the above claim features. [paragraphs (a), (b), (c) added for review]”
Contrary to applicant’s assertions, Palmer already teaches (a) and (b). Newly cited Dittmar et al, Smith and Firey teach the cranking of the compressor is done to ensure sufficient compressed air is for combustion of the combustor, and the pre-heater combustor of Palmer, is one of the combustors that requires the compressed air and would be operated in an analogous fashion. Contrary to applicant’s assertions that
“Palmer fails to disclose the vent system and the operation of a vent during operation of the preheater”
Palmer was clearly applied previous to teach a hydrogen fuel vent [e.g. 633, 634, 635, 636; alternate vent may be 631 - when pump is 607] provided downstream of the liquid hydrogen pump 301 or 607. In response to applicant's argument that the references fail to show certain features of the invention, it is noted that the features upon which applicant relies (i.e., a vent during operation of the preheater) are not recited in the rejected claim(s). Although the claims are interpreted in light of the specification, limitations from the specification are not read into the claims. See In re Van Geuns, 988 F.2d 1181, 26 USPQ2d 1057 (Fed. Cir. 1993). Even if it were claimed, note that Porter teach operating the vent during the priming step and it would be obvious to operate the vent during operation of the pre-heater, since that is occurring during the liquid priming step.
Applicant’s arguments that the system of Palmer would be difficult to start and fails to recognize this as a problem is not persuasive. Applicant’s arguments rely on the problem-solution approach to determine an inventive step. This does not apply to U.S. patent law, which relies on e.g. a determination of obviousness to arrive at the claim limitations. Palmer, as modified by Porter, clearly primes the liquid pump system and Palmer teaches the use of a pre-heater combustor which is used during starting and even before starting. Note the pre-burner is used to vaporize hydrogen fuel, and is taught to be used to vaporize liquid hydrogen fuel during and before starting, see ¶ 0118, 0121-0126. Furthermore, applicant’s arguments are not persuasive because applicant’s invention also relies on a pre-heater combustor for starting – which is similar to Palmer. While applicant may incorporate a vent system during priming, Porter in combination already teaches using the vent system of Palmer, to facilitate liquid priming of the pump. As for the cranking of the core compressor, this is well known in the art -- and Dittmar et al, Smith and/or Firey teach the cranking of the compressor is done to ensure sufficient compressed air is for combustion of the [pre-heater] combustor, where Smith and Firey specifically teach compressor cranking is required prior to fuel delivery to the [pre-heater] combustor.
Applicant's amendment necessitated the new ground(s) of rejection presented in this Office action. Accordingly, THIS ACTION IS MADE FINAL. See MPEP § 706.07(a). Applicant is reminded of the extension of time policy as set forth in 37 CFR 1.136(a).
A shortened statutory period for reply to this final action is set to expire THREE MONTHS from the mailing date of this action. In the event a first reply is filed within TWO MONTHS of the mailing date of this final action and the advisory action is not mailed until after the end of the THREE-MONTH shortened statutory period, then the shortened statutory period will expire on the date the advisory action is mailed, and any nonprovisional extension fee (37 CFR 1.17(a)) pursuant to 37 CFR 1.136(a) will be calculated from the mailing date of the advisory action. In no event, however, will the statutory period for reply expire later than SIX MONTHS from the mailing date of this final action.
Contact Information
Any inquiry concerning this communication or earlier communications from the Examiner should be directed to TED KIM whose telephone number is 571-272-4829. The Examiner can be reached on regular business hours before 5:00 pm, Monday to Thursday and every other Friday.
The fax number for the organization where this application is assigned is 571-273-8300.
If attempts to reach the examiner by telephone are unsuccessful, the examiner’s supervisor, Devon Kramer, can be reached at 571-272-7118 Alternate inquiries to Technology Center 3700 can be made via 571-272-3700.
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/Ted Kim/
Telephone
571-272-4829
Primary Examiner
Fax
571-273-8300
June 9, 2026