DETAILED ACTION
Double Patenting
The nonstatutory double patenting rejection is based on a judicially created doctrine grounded in public policy (a policy reflected in the statute) so as to prevent the unjustified or improper timewise extension of the “right to exclude” granted by a patent and to prevent possible harassment by multiple assignees. A nonstatutory double patenting rejection is appropriate where the conflicting claims are not identical, but at least one examined application claim is not patentably distinct from the reference claim(s) because the examined application claim is either anticipated by, or would have been obvious over, the reference claim(s). See, e.g., In re Berg, 140 F.3d 1428, 46 USPQ2d 1226 (Fed. Cir. 1998); In re Goodman, 11 F.3d 1046, 29 USPQ2d 2010 (Fed. Cir. 1993); In re Longi, 759 F.2d 887, 225 USPQ 645 (Fed. Cir. 1985); In re Van Ornum, 686 F.2d 937, 214 USPQ 761 (CCPA 1982); In re Vogel, 422 F.2d 438, 164 USPQ 619 (CCPA 1970); In re Thorington, 418 F.2d 528, 163 USPQ 644 (CCPA 1969).
A timely filed terminal disclaimer in compliance with 37 CFR 1.321(c) or 1.321(d) may be used to overcome an actual or provisional rejection based on nonstatutory double patenting provided the reference application or patent either is shown to be commonly owned with the examined application, or claims an invention made as a result of activities undertaken within the scope of a joint research agreement. See MPEP § 717.02 for applications subject to examination under the first inventor to file provisions of the AIA as explained in MPEP § 2159. See MPEP § 2146 et seq. for applications not subject to examination under the first inventor to file provisions of the AIA . A terminal disclaimer must be signed in compliance with 37 CFR 1.321(b).
The filing of a terminal disclaimer by itself is not a complete reply to a nonstatutory double patenting (NSDP) rejection. A complete reply requires that the terminal disclaimer be accompanied by a reply requesting reconsideration of the prior Office action. Even where the NSDP rejection is provisional the reply must be complete. See MPEP § 804, subsection I.B.1. For a reply to a non-final Office action, see 37 CFR 1.111(a). For a reply to final Office action, see 37 CFR 1.113(c). A request for reconsideration while not provided for in 37 CFR 1.113(c) may be filed after final for consideration. See MPEP §§ 706.07(e) and 714.13.
The USPTO Internet website contains terminal disclaimer forms which may be used. Please visit www.uspto.gov/patent/patents-forms. The actual filing date of the application in which the form is filed determines what form (e.g., PTO/SB/25, PTO/SB/26, PTO/AIA /25, or PTO/AIA /26) should be used. A web-based eTerminal Disclaimer may be filled out completely online using web-screens. An eTerminal Disclaimer that meets all requirements is auto-processed and approved immediately upon submission. For more information about eTerminal Disclaimers, refer to www.uspto.gov/patents/apply/applying-online/eterminal-disclaimer.
Claim 1 and its dependent claims are rejected on the ground of nonstatutory double patenting as being unpatentable over claim 1 of U.S. Patent No. 11/629,301. Although the claim at issue is not identical, it is not patentably distinct because the patented claim anticipates the present claim.
Claims 2-6, 8-14 are rejected on the ground of nonstatutory double patenting as being unpatentable over claims 2-6, 7-13, respectively, of U.S. Patent No. 11/629,301. Although the claims at issue are not identical, they are not patentably distinct from each other because the patented claims anticipate the present claims.
Claim Rejections - 35 USC § 102
The following is a quotation of the appropriate paragraphs of 35 U.S.C. 102 that form the basis for the rejections under this section made in this Office action:
A person shall be entitled to a patent unless –
(a)(1) the claimed invention was patented, described in a printed publication, or in public use, on sale, or otherwise available to the public before the effective filing date of the claimed invention.
Claim(s) 1, 2, 5-7, 10-11 is/are rejected under 35 U.S.C. 102a1 as being anticipated by McAlister (US 8916735 B2).
Regarding claim 1, McAlister discloses a biosolids treatment system that treats human biosolids to produce beneficial use products including low carbon ash, high carbon activated biochar, and Class A biosolids (the system is capable of treating human biosolids and producing the biochar and biosolids, i.e., renewable fuel/carbon byproducts; see col. 14, lines 33-36 and abstract), the system comprising:
a variable feed conveyor (352+356) that conveys a biosolid feed (Fig. 2; 214) into a dryer (222/314/614);
a dryer that dries the biosolid feed to a predetermined moisture content to create one of a beneficial use products, wherein the predetermined moisture content is controlled by varying a speed of the variable feed conveyor (desired feed throughput controlled by the engine; col. 6, lines 17-19 and col. 7, lines 3-8); and
a gasifier (220/341/610) that converts the biosolid feed into usable thermal energy (renewable fuels such as hydrogen) for system use and at least one of the beneficial use products (carbon byproducts) (see abstract and col. 6, lines 28-38).
Regarding claim 2, McAlister discloses the biosolids treatment system of claim 1, wherein the dryer creates low carbon ash and the gasifier creates high carbon activated biochar and Class A biosolids (the dryer is capable of creating low carbon ash and the gasifier is capable of creating high carbon activated biochar and Class A biosolids, since all of the elements necessary to produce these products are recited in claim 1).
Regarding claim 5, McAlister discloses the biosolids treatment system of claim 1, wherein the system is configured to control carbon content of the biochar. The carbon content is what remains after the water and gases are expelled from the biosolid feed. The amount of water expelled can be controlled by the extruder/conveyor of the dryer, and the volume of gases released is controlled by the drying and gasification temperatures.
Regarding claim 6, McAlister discloses the biosolids treatment system of claim 1, wherein the biochar is used to filter air emissions from the system prior to discharge to atmosphere (the biochar is capable of being used to filter air emissions) (note: this is an intended use claim and is not given patentable weight).
Regarding claim 7, McAlister discloses the biosolids treatment system of claim 1, wherein the biochar is mixed with the human biosolids as exclusive fuel for the gasifier. The system is capable of treating biochar mixed with human biosolids as exclusive fuel for the gasifier.
Regarding claim 10, McAlister discloses the biosolids treatment system of claim 1, wherein the treatment system is capable of using different moisture content biosolid fuel sources. The system discloses all of the elements recited in claim 1; therefore, it is capable of using different moisture content biosolid fuel sources.
Regarding claim 11, McAlister discloses the biosolids treatment system of claim 1, wherein the treatment system is configured to use comingled materials generated by a wastewater treatment facility (WWTF) including grit and screenings, fats/oils/grease (FOG), anaerobically digested biosolids, biosolids post thermal hydrolysis treatment, primary/secondary waste activate sludge, non-activated sludge in varying percent of composition as fuel sources for the gasifier without need for supplemental fuel. The system discloses all of the elements recited in claim 1; therefore, it is capable of using different moisture content biosolid fuel sources.
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.
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.
Claim(s) 3, 4 is/are rejected under 35 U.S.C. 103 as being unpatentable over McAlister (US 8916735 B2) in view of Srinivasachar (US 20100178624 A1).
Regarding claim 3, McAlister discloses the biosolids treatment system of claim 1, except wherein the treatment system includes a blended air intake to temper flue gas entering a dryer, wherein the blended air controls a target temperature in the dryer.
However, Srinivasachar teaches a system for producing carbon-rich products, wherein a treatment system includes a blended air intake to temper flue gas entering a dryer, wherein the blended air controls a target temperature in the dryer (para. 180).
It would have been obvious to a person skilled in the art at the time of effective filing of the application to modify McAlister wherein the treatment system includes a blended air intake to temper flue gas entering a dryer, wherein the blended air controls a target temperature in the dryer. The motivation to combine is to help expel moisture from the biosolids using convective drying. For example, the biosolids could first be dried using convective drying (Srinivasachar) and then squeeze-dried (McAlister).
Regarding claim 4, McAlister discloses the biosolids treatment system of claim 1, except wherein the treatment system includes a fan to recirculate moist dryer exhaust to temper flue gas entering a dryer, wherein blended air controls a target temperature in the dryer and reduces NOx emissions.
However, Srinivasachar teaches a system for producing carbon-rich products, wherein the treatment system includes a fan to recirculate moist dryer exhaust to temper flue gas entering a dryer (see para. 206 and Fig. 5), wherein blended air controls a target temperature in the dryer and reduces NOx emissions (this is intended use language and is given limited patentable weight; moreover, this intended use would inherently be present if the first limitation in this claim is present).
It would have been obvious to a person skilled in the art at the time of effective filing of the application to modify McAlister wherein the treatment system includes a fan to recirculate moist dryer exhaust to temper flue gas entering a dryer, wherein blended air controls a target temperature in the dryer and reduces NOx emissions. The motivation to combine is to help expel moisture from the biosolids using convective drying. For example, the biosolids could first be dried using convective drying (Srinivasachar) and then squeeze-dried (McAlister).
Claim(s) 8, 9 is/are rejected under 35 U.S.C. 103 as being unpatentable over McAlister (US 8916735 B2) in view of Hansen (US 20120308441 A1).
Regarding claims 8, 9, McAlister discloses the biosolids treatment system of claim 1, except further including a water quench that cools the low carbon ash or the high carbon biochar prior to leaving the gasifier (as recited in claim 8), and further including a water quench that serves as an air lock to the gasifier enabling a negative pressure draft to be controlled within the gasifier (as recited in claim 9).
However, Hansen teaches a water quench that cools the carbon ash/ char prior to leaving the gasifier (para. 66), and further including a water quench that serves as an air lock to the gasifier enabling a negative pressure draft to be controlled within the gasifier (paras. 26, 42).
It would have been obvious to a person skilled in the art at the time of effective filing of the application to modify McAlister to further include a water quench that cools the low carbon ash or the high carbon biochar prior to leaving the gasifier (as recited in claim 8), and to further include a water quench that serves as an air lock to the gasifier enabling a negative pressure draft to be controlled within the gasifier (as recited in claim 9). The motivation to combine is to cool the ash/biochar so it can be used for downstream purposes.
Claim(s) 16-18 is/are rejected under 35 U.S.C. 103 as being unpatentable over McAlister (US 8916735 B2) in view of Leary (US 4954066 A).
Regarding claims 16-18, McAlister discloses the biosolids treatment system of claim 1, except wherein the variable feed conveyor is driven by a chain (as recited in claim 16), wherein the chain is cooled by cooling rails that extend along a length of the chain (as recited in claim 17), and wherein the cooling rails comprise a duct with an inlet and outlet (as recited in claim 18).
However, Leary teaches a feed conveyor driven by a chain (abstract), wherein the chain is cooled by cooling rails (26) that extend along a length of the chain (24), and wherein the cooling rails comprise a duct (78) with an inlet and outlet (col. 5, lines 36-45).
It would have been obvious to a person skilled in the art at the time of effective filing of the application to modify McAlister to include a chain driven variable feed conveyor, wherein the chain is cooled by cooling rails that extend along a length of the chain, and wherein the cooling rails comprise a duct with an inlet and outlet. The motivation to combine is to provide a conveyor that is resistant to the heat from the hopper (see McAlister, col. 3, lines 54-67, discussing where the hopper is heated). Cooling the conveyor would prolong the life of the conveyor.
Allowable Subject Matter
Claims 12-15, 19, 20 are objected to as being dependent upon a rejected base claim, but would be allowable if rewritten in independent form including all of the limitations of the base claim and any intervening claims, and by filing a terminal disclaimer for the double patenting rejections.
Conclusion
Any inquiry concerning this communication or earlier communications from the examiner should be directed to JASON LAU whose telephone number is (571)270-7644. The examiner can normally be reached Mon-Fri 8:00-5:00.
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/JASON LAU/Primary Examiner, Art Unit 3762