Prosecution Insights
Last updated: April 19, 2026
Application No. 17/631,338

METHODS AND COMPOSITIONS FOR THE TREATMENT OF PRODUCED WATER

Non-Final OA §103
Filed
Jan 28, 2022
Examiner
NGUYEN, HAIDUNG D
Art Unit
1761
Tech Center
1700 — Chemical & Materials Engineering
Assignee
Solugen Inc.
OA Round
5 (Non-Final)
65%
Grant Probability
Favorable
5-6
OA Rounds
3y 2m
To Grant
93%
With Interview

Examiner Intelligence

Grants 65% — above average
65%
Career Allow Rate
401 granted / 616 resolved
At TC average
Strong +28% interview lift
Without
With
+28.1%
Interview Lift
resolved cases with interview
Typical timeline
3y 2m
Avg Prosecution
39 currently pending
Career history
655
Total Applications
across all art units

Statute-Specific Performance

§101
0.6%
-39.4% vs TC avg
§103
46.4%
+6.4% vs TC avg
§102
27.2%
-12.8% vs TC avg
§112
19.3%
-20.7% vs TC avg
Black line = Tech Center average estimate • Based on career data from 616 resolved cases

Office Action

§103
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 . Continued Examination Under 37 CFR 1.114 A request for continued examination under 37 CFR 1.114, including the fee set forth in 37 CFR 1.17(e), was filed in this application after final rejection. Since this application is eligible for continued examination under 37 CFR 1.114, and the fee set forth in 37 CFR 1.17(e) has been timely paid, the finality of the previous Office action has been withdrawn pursuant to 37 CFR 1.114. Applicant's submission filed on 1/1/2026 has been entered. Response to Amendment Claims 1, 4-9, 11-13, 15, 16, 19-24, and 26-29 are pending. Claims 7-9 are withdrawn from consideration as being drawn to a non-elected group. The previous rejection of claims 1, 4-6, 11-13, 15, 16, 19-24, and 26-29 under 35 U.S.C. 112(b) or 35 U.S.C. 112 (pre-AIA ), second paragraph, is withdrawn in view of applicant’s amendment. The previous rejection of claims 1, 11-13, 15-16, 19-24, 26-29 are rejected under 35 U.S.C. 103 as being unpatentable over Mittiga et al. (US2019/0380337) in view of Young et al (US 20160326443) is maintained in view of applicant’s amendment. The previous rejection of claims 4-6 under 35 U.S.C. 103 as being unpatentable over Mittiga et al. (US2019/0380337) in view of Young et al (US 20160326443) and Cox, Jr. (US 9, 701,556) is maintained in view of applicant’s amendment. The previous rejection of claims 4-6 under 35 U.S.C. 103 as being unpatentable over Mittiga et al. (US2019/0380337) in view of Young et al (US 20160326443) and Cox, Jr. (US 9, 701,556) is withdrawn in view of applicant’s amendment. Applicant's amendment necessitated the new ground(s) of rejection presented in this Office action. The text of those sections of Title 35, U.S. Code not included in this action can be found in a prior Office action. Claim Rejections - 35 USC § 103 Claims 1, 11-13, 15-16, 19-24, 26-29 are rejected under 35 U.S.C. 103 as being unpatentable over Mittiga et al. (US2019/0380337) in view of Young et al (US 20160326443). Regarding claims 1, 11-13, 19, 20, 21, and 27 and 29, Mittiga discloses a method of reducing microbial contamination in an aqueous fluid, wherein the aqueous fluid can be produced water (para 0006), the method comprising: contacting a produced water stream with a composition comprising a (i) a chelator (stabilizers, para 0029) including gluconic acid (aldonic acid, para 0029), wherein the concentration of the stabilizer can range from about 0.1% by weight to about 5% by weight (para 0030); (ii) an oxidizing agent (source of active oxygen including hydrogen peroxide, sodium peroxocarbonate, sodium peroxodicarbonate, potassium percarbonate, potassium peroxocarbonate, or potassium peroxodicarbonate (para 0017), wherein the concentration of the source of active oxygen can range from about 8% by weight to about 25% by weight (para 0018); and (iii) a surfactant (para 0021) under conditions suitable for the formation of a purified produced water. Mittiga also discloses the composition can include an organic acid, which can be diluted into water (para 0031 and 0049). Also See para 0004, 0021-0028, 0049 and 0051. Young teaches using alcohols such as glycols, glycol ethers, methanol, ethanol as a solvent for a produced water clarification composition (para 0055) in an amount from 0 to 70 weight percent (para 0016). It would have been obvious to one of ordinary skill in the art at the time of the invention to modify Mittiga with the teaching of Young, for the purpose of including a solvent such as ethanol for the composition used in the method, and thereby providing effective solubility for the composition as well as efficient cleaning properties, rinsing characteristics, wetting ability, and biodegradability (para 0023). Mittiga discloses the method of reducing microbial contamination in the aqueous fluid, wherein the aqueous fluid can be a brine, an oilfield fluid (para 0006). Mittiga discloses the methods for treatment of microbially contaminated water and microbially contaminated surfaces, wherein the compositions useful for the treatment of water used in industrial applications, for example, for water that flows through pipes or other subterranean formations, such as in the energy industry, for example in oil- and gasfield operations as well as in paper or pulp industries. The compositions disclosed herein are also generally useful for cleaning and sanitizing surfaces or equipment, particularly equipment used in oil and gasfield operations (para 0015). Mittiga does not expressly disclose the method comprising separating/removing hydrocarbons contained in the produced water and the separating/removing hydrocarbons from the produced water comprises breaking an emulsion to allow the hydrocarbons to separate from the produced water. Young discloses oil and gas filed operations or “petroleum industry operations,” includes, but not is limited to, activities and processes for exploration, production, refining and chemical processing of hydrocarbons including, but not limited to, crude oil, gas and their derivatives. Production operations include, but are not limited to, pumping large quantities of water into the ground, as described above, which commensurately generates large quantities of “formation water,” an oil in water dispersion or emulsion. Breaking of such emulsions with additives to remove and recover oil from the produced water is a common and beneficial practice (para 0036). Persons of ordinary skill in the art will readily recognize the many various operations performed in the gas and oil industry is reasonably applicable and is intended to include all such applications including breaking of such emulsions to remove and recover oil (hydrocarbons) from the produced water in the method of Mittiga is obvious in view of Mittiga and Young’s methods. Regarding claims 15 and 16, Mittiga discloses the surfactant can be a non-ionic surfactant, an anionic surfactant or a cationic surfactant. In some embodiments, the surfactant can be a linear alcohol or derivative of a linear alcohol. The linear alcohol can be a C6-C12 linear alcohol. In some embodiments, the surfactant can be an alcohol ethoxylate, an alkoxylated linear alcohol, ethoxylated castor oil, an alkoxylated fatty acid, an alkoxylated coconut oil, an alcohol sulfate, a phosphated mono glyceride, a phosphated diglyceride, or a combination thereof, the surfactant can be a linear alcohol or a derivative of a linear alcohol, wherein the derivative of a linear alcohol can be an ester and the concentration of the surfactant can range from about 0.5% by weight to about 20% by weight (para 0004, 0021-0028). Regarding claim 22, Mittiga does not disclose the purified produced water has a dissolved organic carbon content that is reduced by from about 1 mg/l to about 10,000 mg/l when compared to a dissolved organic carbon content of the produced water. However, composition disclosed by Mittiga is considered to be similar to that of the claimed composition and therefore, a person of ordinary skill in the art would expect such a composition to be capable of reducing a dissolved organic carbon content from about 1 mg/ to about 10,000 mg/ when compared to a dissolved organic carbon content of the produced water. Regarding claim 23, Mittiga does not disclose the purified produced water has a multivalent ion content that is reduced by from about 1 mg/l to about 10,000 mg/l when compared to a multivalent ion content of the produced water. However, composition disclosed by Mittiga is considered to be similar to that of the claimed composition and therefore, a person of ordinary skill in the art would expect such a composition to be capable of reducing a multivalent ion content from about 1 mg/l to about 10,000 mg/l when compared to a multivalent ion content of the produced water. Regarding claim 24, Mittiga does not disclose the purified produced water has an oil content that is reduced by from about 1 mg/l to about 10,000 mg/l when compared to an oil content of the produced water. However, composition disclosed by Mittiga is considered to be similar to that of the claimed composition and therefore, a person of ordinary skill in the art would expect such expect such a composition to be capable of reducing an oil content from about 1 mg/l to about 10,000 mg/l when compared to an oil content of the produced water. Regarding claim 26, Mittiga and Young do not specific disclose the solvent is included in an amount sufficient to provide a composition having suitable rheological properties. However, since the composition disclosed by Mittiga and Young is to be used for the same purpose, i.e. treatment of contaminated water, there is a reasonable basis for one skilled in the art to reasonably expect that the composition of Mittiga and Young would have suitable rheological properties to carry out said treatment. Regarding claim 28, Mittiga discloses the surfactant is present in the composition in an amount of from about 0.5 to 20% by weight (para 0028). Claims 4-6 are rejected under 35 U.S.C. 103 as being unpatentable over Mittiga et al. (US2019/0380337) in view of Young et al (US 20160326443) as applied above, further in view of Cox, Jr. (US 9, 701,556). Regarding claims 4-6, Mittiga in view of Young discloses a method of reducing microbial contamination in an aqueous fluid described above and is incorporated herein by reference. Mittiga disclose the composition comprises gluconic acid (aldonic acid), which meet the claimed biochelant. Cox discloses that it is known in the art to utilize a chelant such as gluconic acid (aldonic acid) and/or sodium gluconate, which is the sodium salt of gluconic acid (col 5, In 14-24), and hydrogen peroxide, for reducing contaminants in wastewater (example 1). It would have been obvious to one of ordinary skill in the art before the filling date of the invention to modify Mittiga reference with the teaching of Cox, for the purpose of including sodium gluconate in the composition, and thereby reducing desired contaminants in the produced water (abstract, col 1, In 25-32, col 3, In 29- 45, col 4, In 3-11). Response to Arguments Applicant’s arguments filed 1/1/2026 have been considered but they are not persuasive. Applicant asserted that the Office suggests that step of separating hydrocarbons from produced water stream to form a purified produced water would have been inherent and would necessarily have resulted in the performance of Mittiga’s method. The Examiner respectfully disagrees with applicant’s statement. The law held that one cannot show nonobviousness by attacking references individually where the rejections are based on combinations of references. See In re Keller, 642 F.2d 413, 208 USPQ 871 (CCPA 1981); In re Merck & Co., 800 F.2d 1091, 231 USPQ 375 (Fed. Cir. 1986). Applicant's argument does not address the reasons presented by the Examiner for combining the teachings of the prior art. That is, the examiner did not suggest that Mittiga’s method inherently includes separating hydrocarbons from produced water by breaking an emulsion contained in the produced water to allow the hydrocarbons to separate from produced water. The present claims were rejected on a combination of Mittiga and Young. Mittiga discloses the method of purifying a produced water (reducing microbial contamination in the aqueous fluid), wherein the produced water (aqueous fluid) can be an oilfield fluid (para 0006). Mittiga discloses the treatment of water is used in oil and gasfield operations (para 0015). Young discloses oil and gas filed operations or “petroleum industry operations,” includes, but not is limited to, activities and processes for exploration, production, refining and chemical processing of hydrocarbons including, but not limited to, crude oil, gas and their derivatives. Production operations include, but are not limited to, pumping large quantities of water into the ground, as described above, which commensurately generates large quantities of “formation water,” an oil in water dispersion or emulsion. Breaking of such emulsions with additives to remove and recover oil from the produced water is a common and beneficial practice (para 0036). Based on the teachings of Young, persons of ordinary skill in the art will readily recognize that breaking of such emulsions to remove and recover oil (hydrocarbons) from the produced water is known in the art, and is reasonably applicable and obvious to apply in Mittiga’s method. There is a reasonable basis for one skilled in the art to expect that operations performed in the gas and oil industry including breaking of such emulsions to remove and recover oil (hydrocarbons) from the produced water would success in view of Mittiga and Young’s method. "For obviousness under § 103, all that is required is a reasonable expectation of success." In re O'Farrell, 853 F.2d 894, 904 (Fed. Cir. 1988) . “Obviousness does not require absolute predictability of success.” Id. at 903, 7 USPQ2d at 1681. Claims 1, 4-6, 11-13, 15, 16, 19-24, and 26-29 remain unpatentable for the reasons of record. Conclusion Any inquiry concerning this communication or earlier communications from the examiner should be directed to HAIDUNG D NGUYEN whose telephone number is (571)270-5455. The examiner can normally be reached M-Th: 10a-3p. 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, Angela Brown-Pettigrew can be reached on 571-272-2817. 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. /HAIDUNG D NGUYEN/ Primary Examiner, Art Unit 1761 1/24/2026
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Prosecution Timeline

Jan 28, 2022
Application Filed
Jun 06, 2024
Non-Final Rejection — §103
Sep 12, 2024
Response Filed
Dec 09, 2024
Final Rejection — §103
Mar 13, 2025
Response after Non-Final Action
Apr 01, 2025
Request for Continued Examination
Apr 02, 2025
Response after Non-Final Action
May 16, 2025
Non-Final Rejection — §103
Aug 20, 2025
Response Filed
Sep 29, 2025
Final Rejection — §103
Dec 01, 2025
Response after Non-Final Action
Jan 01, 2026
Request for Continued Examination
Jan 02, 2026
Response after Non-Final Action
Jan 24, 2026
Non-Final Rejection — §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

5-6
Expected OA Rounds
65%
Grant Probability
93%
With Interview (+28.1%)
3y 2m
Median Time to Grant
High
PTA Risk
Based on 616 resolved cases by this examiner. Grant probability derived from career allow rate.

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