Prosecution Insights
Last updated: October 01, 2026
Application No. 18/718,993

WATER TREATMENT SYSTEM AND METHOD INCLUDING A DRAFT TUBE SYSTEM AND EDUCTOR

Non-Final OA §102§103
Filed
Jun 12, 2024
Priority
Jan 05, 2022 — nonprovisional of PCTUS2022011272
Examiner
GONZALEZ, MADELINE
Art Unit
Tech Center
Assignee
Siemens Energy AG
OA Round
1 (Non-Final)
73%
Grant Probability
Favorable
1-2
OA Rounds
7m
Est. Remaining
88%
With Interview

Examiner Intelligence

Grants 73% — above average
73%
Career Allowance Rate
600 granted / 826 resolved
+12.6% vs TC avg
Strong +16% interview lift
Without
With
+15.7%
Interview Lift
resolved cases with interview
Typical timeline
2y 11m
Avg Prosecution
42 currently pending
Career history
854
Total Applications
across all art units

Statute-Specific Performance

§101
0.5%
-39.5% vs TC avg
§103
48.8%
+8.8% vs TC avg
§102
21.4%
-18.6% vs TC avg
§112
21.7%
-18.3% vs TC avg
Black line = Tech Center average estimate • Based on career data from 826 resolved cases

Office Action

§102 §103
DETAILED ACTION Claim Status Claims 1-18 are rejected. 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) 1-9 and 11 are rejected under 35 U.S.C. 102(a)(1) as being anticipated by Felch et al. (US 2018/0078880) [hereinafter Felch]. With respect to claim 1, Felch discloses a water treatment system 100, as shown in Fig. 1, having: a vessel 107, as shown in Fig. 1; a filter media 160 positioned in the vessel 107, as shown in Fig. 1; a feed steam 170 (feed inlet) positioned in the vessel 107 above the filter media 160, as shown in Fig. 1; a separation device 115 (knockout pot) coupled to the vessel 107 and arranged to collect a gas 140 discharged from the vessel 107, as shown in Fig. 1; a draft tube 112 positioned in the vessel 107 and filled with the filter media 160 (see paragraph 0058); an eductor including a fluid inlet, a fluid suction port, and a fluid outlet directed into the draft tube 112 (see paragraph 0073); a first fluid supply 165 coupled to the fluid inlet to deliver a flow of a first fluid, as shown in Fig. 1; and a conduit 145 arranged to connect the knockout pot 115 to the fluid suction port, as shown in Fig. 1, the eductor operable to draw a portion of the gas into the eductor in response to the flow of the first fluid, the first fluid and the gas forming a backwash mixture that is discharged into the draft tube 112 via the fluid outlet to induce a roll of the filter media 160 during a backwash process (see paragraphs 0054-0055, 0062). With respect to claims 2 and 11, Felch discloses wherein the filter media 160 includes a walnut shell filter media (see paragraphs 0036, 0041, 0043). With respect to claim 3, Felch discloses wherein the draft tube 112 is cylindrical and cooperates with the vessel 107 to define a peripheral zone 114 positioned between a side wall of the draft tube 112 and a side wall of the vessel 107, as shown in Fig. 1. With respect to claim 4, Felch discloses wherein the draft tube 112 comprises one or more side walls that are open at a lowermost end and an uppermost end, as shown in Fig. 3 (see paragraph 0055). With respect to claim 5, Felch discloses wherein the eductor is positioned below the filter media 160 to deliver the mixture to the lowermost end of the draft tube 112 (see paragraph 0073). With respect to claim 6, Felch discloses wherein the draft tube 112 is a first draft tube of a plurality of draft tubes positioned in the vessel 107 to form a peripheral zone 114 external to each draft tube of the plurality of draft tubes and internal to the vessel 107 (see paragraphs 0054, 0062-0063). With respect to claims 7 and 9, Felch discloses wherein the gas includes methane (see paragraph 0025). With respect to claim 8, Felch discloses a water treatment system 100, as shown in Fig. 1, having: directing a flow of wastewater 170 into a vessel 107 containing a filter media 160 and a draft tube 112 positioned within the vessel 107, as shown in Fig. 1; collecting a gas 140 from the vessel 107 and directing it to a knockout pot 115, as shown in Fig. 1; initiating a backwash process (see paragraph 0061); directing a flow of fluid to an eductor (see paragraph 0073), the eductor coupled to the knockout pot 115 (see paragraph 0073); drawing a portion of the gas into the eductor in response to the flow of fluid (see paragraph 0073); mixing the gas and the flow of fluid within the eductor to produce a backwash mixture (see paragraphs 0073-0074); discharging the backwash mixture into a lowermost end of the draft tube 112 (see paragraph 0073-0074); and inducing a roll of the filter media 160 in response to the flow of the backwash mixture into the draft tube 112 process (see paragraphs 0054-0055, 0062). 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) 10 and 12-18 are rejected under 35 U.S.C. 103 as being unpatentable over Felch (US 2018/0078880). With respect to claim 10, Felch discloses wherein the draft tube is one of a plurality of draft tubes (see paragraphs 0054, 0062-0063). Felch does not disclose the eductor being one of a plurality of eductors, and wherein the directing a flow of fluid, the drawing step, and the mixing step are repeated for each eductor which is associated with one of the plurality of draft tubes. However, this would have been obvious to one of ordinary skill in the art in order to effectively backwash each draft tube and since to provide a second eductor is considered to be a duplication of parts, and the courts have held that mere duplication of parts has no patentable significance unless a new and unexpected result is produced. (See In re Harza, 274 F. 2d 669, 124 USPQ 378 (CCPA 1960)). With respect to claim 12, Felch discloses a water treatment system 100, as shown in Fig. 1, having a vessel 107 including a walnut shell filter media 160 disposed therein (see paragraphs 0036, 0041, 0043); a knockout pot 115 coupled to the vessel 107 and arranged to collect a combustible gas 140 discharged from the vessel 107, as shown in Fig. 1, the knockout pot 115, as shown in Fig. 1; a draft tube 112 having a lowermost end and positioned in the vessel 107, as shown in Fig. 1, the draft tube 112 filled with the walnut shell filter media 160 (see paragraph 0058); an eductor including a fluid inlet, a fluid suction port, and a fluid outlet directed into the lowermost end of the draft tube 112 (see paragraph 0073); a first fluid supply 165 coupled to the fluid inlet to deliver a flow of a first fluid to the eductor (see paragraph 0073); and a conduit 145 arranged to connect the knockout pot 115 to the fluid suction port, the eductor operable to draw a portion of the gas into the eductor in response to the flow of the first fluid (see paragraph 0073), the first fluid and the gas forming a backwash mixture that is discharged into the draft tube 112 via the fluid outlet to induce a roll of the walnut shell filter media 160 (see paragraphs 0054-0055, 0062). Felch does not disclose a flare arranged to combust the combustible gas; and to reduce the quantity of combustible gas directed to the flare during a backwash process. However, Felch teaches in the prior art methods, the separated liquid phase is disposed of either by pumping it to an upstream separation step or to a slop tank for disposal, and the separated gas phase, which potentially contains hydrogen sulfide gas and hydrocarbons, is sent to a gas disposal device such as a scrubber or flare (see paragraph 0024). Felch also teaches that in the process 200, mixed liquid and gas is separated into a liquid and a gas, and at least a portion of the separated gas is recycled to the water treatment device (see paragraph 0075). It would have been obvious to one of ordinary skill in the art to provide the knockout pot disclosed by Felch with a flare, as claimed by applicant, in order to further dispose of the excess gas that is not recycled, since Felch states that a portion of the gas is recycled and one or ordinary skill would recognize that there may be excess gas in need of disposal and the use of a flare is common for gas disposal (see paragraph 0024). With respect to claim 13, Felch discloses wherein the draft tube 112 is centrally located in the vessel 107 and defines a peripheral zone 114 positioned between a side wall of the draft tube 112 and a side wall of the vessel 107, as shown in Figs. 1 and 3. With respect to claim 14, Felch discloses a baffle positioned in the draft tube 112 (see paragraph 0060). With respect to claim 15, Felch discloses wherein the baffle comprises a hollow cylinder having an axis substantially co-axial with an axis of the draft tube 112 (see paragraph 0060). With respect to claim 16, Felch discloses wherein the draft tube 112 is a first draft tube of a plurality of draft tubes positioned in the vessel 107 to form a peripheral zone 114 external to each draft tube of the plurality of draft tubes and internal to the vessel 107 (see paragraphs 0054, 0062-0063). With respect to claim 17, Felch discloses wherein the gas includes methane (see paragraph 0025). With respect to claim 18, Felch teaches wherein the first fluid includes wastewater (see paragraph 0044). Felch lacks wastewater at a pressure between 1 bar and 10 bars. However, Felch teaches that the water treatment device 105 may be open to the environment or may be closed to operate under pressure (see paragraph 0044). It would have been obvious to one of ordinary skill in the art to provide the wastewater disclosed by Felch at a pressure between 1 bar and 10 bars, as claimed by applicant, since one of ordinary skill would recognize to choose a desired pressure according to a desired application (see paragraph 0044). Conclusion The prior art made of record and not relied upon is considered pertinent to applicant's disclosure. Felch et al. (US 8,747,667) and Felch et al. (US 9,580,335) teach related water treatment apparatuses having walnut shell filter media. Crits et al. (US 2009/0178555) teaches a degassing process in water treatment having an eductor. Any inquiry concerning this communication or earlier communications from the examiner should be directed to MADELINE GONZALEZ whose telephone number is (571)272-5502. The examiner can normally be reached M-F 9-5:30. 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, Benjamin Lebron can be reached at 571-272-0475. The fax phone number for the organization where this application or proceeding is assigned is 571-273-8300. Information regarding the status of published or unpublished applications may be obtained from Patent Center. Unpublished application information in Patent Center is available to registered users. To file and manage patent submissions in Patent Center, visit: https://patentcenter.uspto.gov. Visit https://www.uspto.gov/patents/apply/patent-center for more information about Patent Center and https://www.uspto.gov/patents/docx for information about filing in DOCX format. For additional questions, contact the Electronic Business Center (EBC) at 866-217-9197 (toll-free). If you would like assistance from a USPTO Customer Service Representative, call 800-786-9199 (IN USA OR CANADA) or 571-272-1000. /MADELINE GONZALEZ/Primary Examiner, Art Unit 1773
Read full office action

Prosecution Timeline

Jun 12, 2024
Application Filed
Sep 02, 2026
Non-Final Rejection mailed — §102, §103 (current)

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Study what changed to get past this examiner. Based on 5 most recent grants.

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Prosecution Projections

1-2
Expected OA Rounds
73%
Grant Probability
88%
With Interview (+15.7%)
2y 11m (~7m remaining)
Median Time to Grant
Low
PTA Risk
Based on 826 resolved cases by this examiner. Grant probability derived from career allowance rate.

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