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 .
DETAILED ACTION
This Final Office action is based on the 18/901042 application originally filed September 30, 2024.
Claims 1-10, filed September 24, 2025, are pending and have been fully considered. Claims 6-9 are withdrawn from consideration due to being drawn to a nonelected invention.
Election/Restrictions
Applicant’s election without traverse of Group I claims 1-5 in the reply filed on June 18, 2025 is acknowledged.
Claims 6-9 are withdrawn from further consideration pursuant to 37 CFR 1.142(b) as being drawn to a nonelected invention, there being no allowable generic or linking claim. Election was made without traverse in the reply filed on June 18, 2025.
Claim Rejections - 35 USC § 103
In the event the determination of the status of the application as subject to AIA 35 U.S.C. 102 and 103 (or as subject to pre-AIA 35 U.S.C. 102 and 103) is incorrect, any correction of the statutory basis (i.e., changing from AIA to pre-AIA ) for the rejection will not be considered a new ground of rejection if the prior art relied upon, and the rationale supporting the rejection, would be the same under either status.
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.
The factual inquiries for establishing a background for determining obviousness under 35 U.S.C. 103 are summarized as follows:
1. Determining the scope and contents of the prior art.
2. Ascertaining the differences between the prior art and the claims at issue.
3. Resolving the level of ordinary skill in the pertinent art.
4. Considering objective evidence present in the application indicating obviousness or nonobviousness.
This application currently names joint inventors. In considering patentability of the claims the examiner presumes that the subject matter of the various claims was commonly owned as of the effective filing date of the claimed invention(s) absent any evidence to the contrary. Applicant is advised of the obligation under 37 CFR 1.56 to point out the inventor and effective filing dates of each claim that was not commonly owned as of the effective filing date of the later invention in order for the examiner to consider the applicability of 35 U.S.C. 102(b)(2)(C) for any potential 35 U.S.C. 102(a)(2) prior art against the later invention.
Claim(s) 1-5 and 10 is/are rejected under 35 U.S.C. 103 as being unpatentable over Seidner (US 2021/0214617).
Regarding Claims 1, 3-5 and 10
Seidner discloses in paragraph 0035, a method for compounding a non-aqueous biofuel derived from various solid but specially processed biomass furnishes into a liquid fuel that may be used in engines such as diesel engines and other internal combustion engines, combustion turbines or aero-derivative turbines, conventional boilers as well used in non-internal combustion devices where the fuel is burned to provide indirect generation of heat or energy, including diesel, gas or steam driven turbines.
Seidner discloses in paragraph 0038, the feedstock for the special process used to create the biocarbon may include not only raw biomass, but also the waste product from processes that create liquid biofuels such as bio-gasoline, bio-oil, or various other energy containing liquid fuels, such as, for example, ethanol and methanol.
Seidner discloses in paragraph 0039, the biofuel is a colloidal dispersion of micronized and nano-particulate biocarbon in a petroleum or oil-biofuel base. Such a dispersion is advantageous in that it provides for supplementation of a petroleum based fuel in such a manner as to maintain or increase the energy content of the fuel while reducing the amount of petroleum product consumed while reducing the harmful environmental impact of use of the petroleum based fuel.
Seidner discloses in paragraph 0040, the biofuel is added to heavy fuel oil such as, for example, bunker fuel oil to dilute or blend with the fuel oil, reducing both the percentage of harmful sulfur or other mineral components of the bunker fuel and reducing the overall price of the blended or diluted fuel while maintaining or increasing the energy content, lubricity, cetane value and other characteristics of the heavy fuel oil without increasing the amount of harmful emissions resulting from the combustion of the blended mix of biofuel and bunker fuel oil.
Seidner discloses in paragraph 0050, a particulate solid biomass derived fuel dispersed into a non-aqueous liquid to form a combustible colloidal suspension. In an alternative aspect, the solid biomass derived fuel has an average particle size of less than or equal to 10 microns. In another alternative aspect, the solid biomass derived fuel has an average particle size in the range of one micron to 100 nanometers.
Seidner discloses in paragraph 0058, a method of making a green biofuel based on renewable biomass feedstock, comprising: receiving biomass feedstock; combining the biomass feedstock with a biocarbon colloidal dispersion into a blend; and pumping the blend through a length of first pipe having a first diameter surrounded by second pipe having a second diameter larger than the first diameter, the second pipe being supplied with a continuous flow of heat exchange fluid, the length of the first pipe having an input end for receiving the blend, and an output end for outputting a second blend of torrefied biomass and biocarbon colloidal dispersion generated within the length of the first pipe. In one alternative aspect, the heat exchange fluid is molten salt. In a further aspect, the method includes particulating the second blend to have a particle distribution in the range of 10 micron to 100 nanometers. In one alternative aspect, the particle distribution has an average particle size of 200 nanometers to 400 nanometers. In another aspect, the torrefied biomass is friable. In still another aspect, the biomass feedstock includes waste from a process that produces a combustible liquid from raw biomass. In another aspect, generating the second blend produces a low moisture biocarbon, a condensable gas and a liquid component. In another aspect, the condensable gas is further processed to produce a mixture of suspended solids and non-condensed gas. In still another aspect, the suspended solids are further processed to produce biochar, carbon black, fertilizer, or activated carbon. In yet another aspect, the non-condensed gas is combustible. In another aspect, the liquid component is a pyrolysis liquid. In an aspect, the second blend is inputted into a tertiary reactor. In yet another aspect, the tertiary reactor is heated by a heat exchange fluid, the heat exchange fluid being a molten salt. In still another aspect, the pyrolysis liquid is stored in a storage container. In yet another aspect, the stored pyrolysis liquid is provided as an input to a tertiary reactor for further processing. In yet another aspect, the blend includes coal or non-green material feedstocks.
Therefore, through the teachings of Seidner it would have been obvious before the effective filing date of the claimed invention to a person having ordinary skill in the art that the particle size distribution of Seidner is bimodal due to the size distribution is made of two different modes of particle sizes.
Seidner discloses in paragraph 0134, the biofuel manufactured in accordance with the various embodiments may be used as a standalone fuel to be used in burners and engines such as diesel engines, or it may also be used to fuel a jet or combustion turbine engine. The biofuel can be blended with a bio-oil liquid for a 100% green liquid solution or a petroleum based fuel oil for an environmentally improved petroleum based fuel oil. It is also contemplated that the liquid biofuel may be used as an additive to petroleum based fuels, such as heavy fuel oil or bunker oil marine diesel fuel or to make renewable green carbon black oil, or green renewable activated carbon feedstock.
Seidner discloses in paragraph 0133, the liquid biofuel based on the biochar of the various embodiments is easier and safer for all purposes than a powdered, pelletized or cubed form of processed biomass to transport and store, deliver and convey, and may be used in directly in burners, misters, boilers, or gasifiers, compression ignition and combustion engines, and turbines that are designed to burn conventional petroleum distillates or liquid green energy oil derived fuels or solid coal boilers. The energy provided by such a fuel produces increased energy, gallon for gallon, or pound for pound, with a reduced carbon footprint, reduced atmospheric emissions and reduced residual left-over ash when compared to other solid raw biomass fuels and all other solid non-biomass fuels.
Seidner discloses in paragraph 0136, liquid biofuel may be priced lower than petroleum based bunker fuel. It may be added to low sulfur bunker fuel oil such that it comprises, for example, 25% to 40% of the total volume of the fuel mix, thereby significantly reducing the cost of the combined fuel per gallon or per ton, while not compromising the efficacy of the primary bunker fuel oil component and without increasing any adverse effects of sulfur or other minerals, yet maintaining, or increasing, the energy value of the combination fuel. Even if this blended mix resulted in increased the consumption of the fuel oil mix to provide the same operating parameters for ship's engines, the increased amount of energy provided at a lower cost in the blend more than offsets the marginally increased consumption. It is to be noted, the remainder of the fuel is in the amount of 60% to 100%.
Seidner does not disclose the biofuel having a ash content and therefore Seidner has met the limitation of the present invention of having a low ash content.
Seidner does not disclose the biofuel having a low inorganic ash content and therefore Seidner has met the limitation of the present invention of having a low inorganic ash content of less than 1 percent (less than 1 percent encompasses zero).
In the case where the claimed ranges “overlap or lie inside ranges disclosed by the prior art” a prima facie case of obviousness exists. In re Wertheim, 541 F.2d 257, 191 USPQ 90 (CCPA 1976); In re Woodruff, 919 F.2d 1575, 16 USPQ2d 1934 (Fed. Cir. 1990).
Regarding Claim 2
Seidner discloses in paragraph 0134, the biofuel manufactured in accordance with the various embodiments may be used as a standalone fuel to be used in burners and engines such as diesel engines, or it may also be used to fuel a jet or combustion turbine engine. The biofuel can be blended with a bio-oil liquid for a 100% green liquid solution or a petroleum based fuel oil for an environmentally improved petroleum based fuel oil. It is also contemplated that the liquid biofuel may be used as an additive to petroleum based fuels, such as heavy fuel oil or bunker oil marine diesel fuel or to make renewable green carbon black oil, or green renewable activated carbon feedstock.
Response to Arguments
Applicant’s arguments directed to the newly submitted claimed amendments, filed September 24, 2025, with respect to the rejection(s) of claim(s) 1-5 under Gosselink et al. (US 2012/0289752) have been fully considered and are persuasive. Therefore, the rejection has been withdrawn. However, upon further consideration, a new ground(s) of rejection is made in view of Seidner (US 2021/0214617).
Conclusion
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.
Any inquiry concerning this communication or earlier communications from the examiner should be directed to LATOSHA D HINES whose telephone number is (571)270-5551. The examiner can normally be reached Monday thru Friday 9:00 AM - 6:00 PM.
Examiner interviews are available via telephone, in-person, and video conferencing using a USPTO supplied web-based collaboration tool. To schedule an interview, applicant is encouraged to use the USPTO Automated Interview Request (AIR) at http://www.uspto.gov/interviewpractice.
If attempts to reach the examiner by telephone are unsuccessful, the examiner’s supervisor, Prem Singh can be reached at 571-272-6381. The fax phone number for the organization where this application or proceeding is assigned is 571-273-8300.
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/Latosha Hines/Primary Examiner, Art Unit 1771