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 .
Claim Rejections - 35 USC § 112
The following is a quotation of 35 U.S.C. 112(b):
(b) CONCLUSION.—The specification shall conclude with one or more claims particularly pointing out and distinctly claiming the subject matter which the inventor or a joint inventor regards as the invention.
The following is a quotation of 35 U.S.C. 112 (pre-AIA ), second paragraph:
The specification shall conclude with one or more claims particularly pointing out and distinctly claiming the subject matter which the applicant regards as his invention.
Claim 1, 8 and their dependent claims are rejected under 35 U.S.C. 112(b) or 35 U.S.C. 112 (pre-AIA ), second paragraph, as being indefinite for failing to particularly point out and distinctly claim the subject matter which the inventor or a joint inventor (or for applications subject to pre-AIA 35 U.S.C. 112, the applicant), regards as the invention.
Claim 1 recites the limitation “a flow anode” on line 12. It is not clear if this limitation is the same as “a screen current collector-based flow anode” on lines 1-2, or not. Examiner interprets them to be the same.
The term “a low voltage” in claim 1 on line 18 is a relative term which renders the claim indefinite. The term “low voltage” is not defined by the claim, the specification does not provide a standard for ascertaining the requisite degree, and one of ordinary skill in the art would not be reasonably apprised of the scope of the invention. It is not clear what is considered low versus high voltage.
The terms “an efficient removal” and “an effective interception” in claim 1 on line 21 are relative terms which renders the claim indefinite. The terms are not defined by the claim, the specification does not provide a standard for ascertaining the requisite degree, and one of ordinary skill in the art would not be reasonably apprised of the scope of the invention. It is not clear what is considered efficient or effective versus what would not be considered efficient or effective.
Claim 8 recites the limitations “an electrochemical treatment of wastewater” and “a screen current collector-based flow anode” on lines 1-2. It is not clear if these limitations are the same as “an/the electrochemical treatment of wastewater” and “a/the screen current collector-based flow anode” of Claim 1, or not. Examiner interprets them to be the same.
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, 3-9, 11, 12, 14, 15, 17, 18 & 20 is/are rejected under 35 U.S.C. 103 as being unpatentable over Murphy et al., (“Murphy”, US 5,460,705), in view of Nishimura et al., (“Nishimura”, US 6,939,458), and in further view of Menth et al., (“Menth”, US 4,416,747), as evidenced by “Mesh Size”, (“Mesh Size”, “Kramer Industries, Inc.”, https://www.kramerindustriesonline.com/resources/mesh-size/, obtained from Web 12/18/2025, 4 total pages).
Regarding Claims 1, 3-7, 11, 12, 14, 15, 17 & 18, Murphy discloses a device for an electrochemical treatment of a wastewater, (See column 12, lines 52-64, See column 15, lines 63-67, Murphy), with a screening current collector-based flow anode, (Anode 20, See Figure 2, 6, 7, See column 14, lines 47-49, Murphy), comprising: a shell, wherein an interior of the shell is a cavity structure, (End Plates 34/36 with interior and slot 59, See Figure 2, 6, 7, See column 14, lines 47-62), and the shell is provided with a water inlet and a water outlet each communicating with the cavity structure, (Inlet 28 and Outlet 32, See Figure 2, 6, 7, See column 14, lines 11-16, See column 15, lines 46-57, Murphy); and the water inlet is configured to feed the wastewater to be treated, and the water outlet is configured to discharge purified recycled water, (Inlet 28 and Outlet 32, See column 14, lines 11-16, See column 15, lines 46-57, Murphy); a screening current collector structure, wherein the screening current collector structure comprises a screening anode current collector and a cathode current collector, (Mesh 52 & 54, See Figures 2, 6, & 7), a cathode/anode separator is provided between the screening anode current collector and the cathode current collector, (Electrolyte 12 between Meshes 52 & 54, See Figures 2, 6 & 7, See column 13, lines 44-49, Murphy), and the screening anode current collector and the cathode current collector are each connected to an external circuit, (See column 13, lines 3-9; See column 15, lines 22-25; See column 14, lines 50-54, Murphy); an anode cell and a cathode cell, wherein the anode cell and the cathode cell are formed through a division of the cavity structure by the screening current collector structure, (Electrolyte 12 divides Mesh 54/Anode 20 into one compartment (anode cell) and Mesh 52/Cathode 16 into another compartment (cathode cell), See Figure 2, 6, 7, See column 14, lines 47-63, Murphy), and an electrolyte is provided in each of the anode cell and the cathode cell, (See column 14, lines 11-16, See column 14, lines 3-10); and a flow anode, (Anode 20 in this portion/compartment of overall Cell, See Figure 2, 6, 7, See column 14, lines 47-49, Murphy); wherein an unidirectional anodic bias voltage is applied to the screening current collector structure to allow a polarization of the flow anode in contact with the screening current collector structure, (See column 2, lines 66-67, column 3, lines 1-5), and a water oxidation reaction is further allowed on a surface of the flow anode at a low voltage, (See column 2, lines 66-67, column 3, lines 1-2, See column 6, lines 30-31, See column 13, lines 60-65), to produce an adsorbed hydroxyl, (See column 2, lines 33-50), to make the flow anode conduct a filtering solid-liquid separation (SLS) on a surface of the screening current collector structure, such that a particulate space stacking effect is formed to allow an efficient removal of pollutants and an effective interception of the flow anode, (See column 15, lines 63-67, column 16, lines 1-10, See column 2, lines 45-50; organic/biological material/contaminants are treated); and wherein the screening anode current collector has a porous structure, (See column 14, lines 47-57, Murphy).
Murphy does not explicitly disclose that its anode and cathode meshes are anode and cathode current collectors, the flow anode suspended in the cell or the screening anode current collector has a pore size smaller than a particle size of the flow anode, and the flow anode has the particle size in a range of 0.1 pm to 1,000 micron.
Nishimura discloses that the flow anode is suspended in the cell, (See column 12, lines 20-25, Nishimura), and the flow anode has the particle size in a range of 0.1 micron to 1,000 micron, (See column 14, lines 54-61, Nishimura; anticipates the claimed range from 0.5 mm or less, which overlaps from 0.1 micron to 500 micron). Additional features of this embodiment are included as part of the overall combination.
It would have been obvious to one of ordinary skill in the art before the effective filing date of the invention to have modified the device of Murphy by incorporating that the flow anode has the particle size in a range of 0.1 micron to 1,000 micron as in Nishimura because “the surface area of electrodes can be substantially increased by incorporating electrically conductive particles into an influent….so that the conductive particles present in the influent can substantially serve as an electrode”, (See column 12, lines 20-26, Nishimura), so that “a large amount of electric power can be supplied…to greatly improve throughput and process efficiency”, (See column 12, lines 53-57, Nishimura).
Modified Murphy does not disclose that its anode and cathode meshes are anode and cathode current collectors or the screening anode current collector has a pore size smaller than the particle size of the flow anode.
Menth discloses its anode and cathode meshes are anode and cathode current collectors, (Collectors 4, See Figure 1, See column 2, lines 3-6, Menth), and the screening anode current collector has a pore size smaller than the particle size of the flow anode, (See column 3, lines 50-59; the mesh for the current collectors is 70 mesh which converts to 210 microns as evidenced by “Mesh Size”, which is smaller than the disclosed range of Nishimura from 210 to 500 microns).
It would have been obvious to one of ordinary skill in the art before the effective filing date of the invention to have modified the device of Murphy by incorporating its anode and cathode meshes are anode and cathode current collectors and the screening anode current collector has a pore size smaller than the particle size of the flow anode as in Menth for “ensuring that a good current-distribution is obtained over the membrane [electrolyte]”, (See column 2, lines 3-5, Menth).
Additional Disclosures Included:
Claim 3: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 1, wherein the device is a flat plate-type device, (See column 7, lines 14-16, Murphy); and the screening anode current collector, the cathode current collector, and the cathode/anode separator are arranged in parallel inside the shell in a clamping manner, (See column 7, lines 14-16, Murphy).
Claim 4: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 1, further comprising: an anode terminal post, wherein the anode terminal post is connected to the screening anode current collector and extends out of the shell, (Terminal/Bushbar 46, See Figure 2, 6, 7, See column 14, lines 37-46, Murphy); and a cathode terminal post, wherein the cathode terminal post is connected to the cathode current collector and extends out of the shell, (Terminal/Bushbar 48, See Figure 2, 6, 7, See column 14, lines 37-46, Murphy); and the screening anode current collector and the cathode current collector are connected to the external circuit through the anode terminal post and the cathode terminal post, respectively, (See column 14, lines 43-46, See column 13, lines 4-10, Murphy).
Claim 5: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 1, wherein a material of the screening anode current collector is selected from the group consisting of SnO2-Sb, PbO2, a flexible carbon material, a platinum mesh, IrTa, and IrRu, (See column 13, lines 36-43, Murphy; lead oxide).
Claim 6: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 1, wherein a material of the cathode current collector is selected from the group consisting of a titanium mesh, a platinum mesh, and a stainless steel mesh, (See column 13, lines 32-35, Murphy, platinum composition; See column 2, lines 6-15, Menth, titanium mesh).
Claim 7: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 1, wherein a material of the flow anode is selected from the group consisting of a metal oxide and a carbon material, (See column 13, lines 36-43, Murphy; lead oxide).
Claim 11: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 3, wherein a material of the screening anode current collector is selected from the group consisting of SnO2-Sb, PbO2, a flexible carbon material, a platinum mesh, IrTa, and IrRu, (See column 13, lines 36-43, Murphy; lead oxide).
Claim 12: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 4, wherein a material of the screening anode current collector is selected from the group consisting of SnO2-Sb, PbO2, a flexible carbon material, a platinum mesh, IrTa, and IrRu, (See column 13, lines 36-43, Murphy; lead oxide).
Claim 14: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 3, wherein a material of the cathode current collector is selected from the group consisting of a titanium mesh, a platinum mesh, and a stainless steel mesh, (See column 13, lines 32-35, Murphy, platinum composition; See column 2, lines 6-15, Menth, titanium mesh).
Claim 15: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 4, wherein a material of the cathode current collector is selected from the group consisting of a titanium mesh, a platinum mesh, and a stainless steel mesh, (See column 13, lines 32-35, Murphy, platinum composition; See column 2, lines 6-15, Menth, titanium mesh).
Claim 17: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 3, wherein a material of the flow anode is selected from the group consisting of a metal oxide and a carbon material, (See column 13, lines 36-43, Murphy; lead oxide).
Claim 18: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 4, wherein a material of the flow anode is selected from the group consisting of a metal oxide and a carbon material, (See column 13, lines 36-43, Murphy; lead oxide).
Regarding Claims 8, 9 & 20, Murphy discloses a process for an electrochemical treatment of wastewater with a screening current collector-based flow anode, wherein the process is implemented by the device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 1, and comprises the following steps: introducing the wastewater through the water inlet, (Inlet 28 and Outlet 32, See Figure 2, 6, 7, See column 14, lines 11-16, See column 15, lines 46-57, Murphy), and starting stirring to keep an anode material suspended, (See column 17, lines 35-47, Nishimura); applying the unidirectional anodic bias voltage to the screening current collector structure to allow the polarization of the flow anode in contact with the screening current collector structure, (See column 2, lines 66-67, column 3, lines 1-5), and further allowing the water oxidation reaction on the surface of the flow anode at the low voltage, (See column 2, lines 66-67, column 3, lines 1-2, See column 6, lines 30-31, See column 13, lines 60-65), to produce the adsorbed hydroxyl (See column 2, lines 33-50), to make the flow anode conduct the filtering SLS on the surface of the screening current collector structure, such that the particulate space stacking effect is formed to allow the efficient removal of pollutants and the effective interception of the flow anode, (See column 15, lines 63-67, column 16, lines 1-10, See column 2, lines 45-50; organic/biological material/contaminants are treated); and discharging the purified recycled water through the water outlet, (Inlet 28 and Outlet 32, See column 14, lines 11-16, See column 15, lines 46-57, Murphy).
Additional Disclosures Included:
Claim 9: The process for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 8, further comprising one or more selected from the group consisting of the following technical features: A. an applied anode potential is 0.5 V to 2.0 V vs a standard hydrogen electrode (SHE) potential, (See column 20, lines 59-64 and See column 20, lines 27-35; actual potential applied is 3 V and standard potential is 1.23 V, the difference is 1.73 V, anticipating the claimed range at this value); B. the device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode operates in a continuous flow mode, and a water flux of the screening anode current collector is 0 m3/m2/h to 1 m3/m2/h, (optional, not required); and C. a magnetic stirring or a mechanical stirring at a stirring rate of 100 rpm to 250 rpm is adopted to keep the flow anode suspended in the electrolyte, (optional, not required).
Claim 20: The process for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 8, wherein the device is a flat plate-type device, (See column 7, lines 14-16, Murphy); and the screening anode current collector, the cathode current collector, and the cathode/anode separator are arranged in parallel inside the shell in a clamping manner, (See column 7, lines 14-16, Murphy).
Claim(s) 2, 10, 13, 16 & 19 is/are rejected under 35 U.S.C. 103 as being unpatentable over Murphy et al., (“Murphy”, US 5,460,705), in view of Nishimura et al., (“Nishimura”, US 6,939,458), and in further view of Menth et al., (“Menth”, US 4,416,747), in further view of DeNora et al., (“DeNora”, US 4,177,116).
Regarding Claims 2, 10, 13 & 16, modified Murphy discloses the device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 1, but does not disclose wherein the device is a tube-in-tube device; and the cathode/anode separator and the cathode current collector are wound sequentially around the screening anode current collector. Nishimura suggests its device is a tube-in-tube device, and the cathode current collector is wound sequentially around the screening anode current collector, (See column 2, lines 16-31, Nishimura).
DeNora discloses wherein the device is a tube-in-tube device; and the cathode/anode separator and the cathode current collector are wound sequentially around the screening anode current collector, (See column 4, lines 44-68, column 5, lines 1-11, DeNora).
It would have been obvious to one of ordinary skill in the art before the effective filing date of the invention to have modified the device of modified Murphy by incorporating wherein the device is a tube-in-tube device; and the cathode/anode separator and the cathode current collector are wound sequentially around the screening anode current collector because the separator “preferably tubular, is…fastened” and “this fastening is particularly easy and forms a perfect hydraulic seal between the membranes and the…anodes which is difficult to obtain in conventional filter press cells”, (See column 4, lines 66-68, column 5, lines 1-5, DeNora).
Additional Disclosures Included:
Claim 10: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 2, wherein a material of the screening anode current collector is selected from the group consisting of SnO2-Sb, PbO2, a flexible carbon material, a platinum mesh, IrTa, and IrRu, (See column 13, lines 36-43, Murphy; lead oxide).
Claim 13: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 2, wherein a material of the cathode current collector is selected from the group consisting of a titanium mesh, a platinum mesh, and a stainless steel mesh, (See column 13, lines 32-35, Murphy, platinum composition; See column 2, lines 6-15, Menth, titanium mesh).
Claim 16: The device for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 2, wherein a material of the flow anode is selected from the group consisting of a metal oxide and a carbon material, (See column 13, lines 36-43, Murphy; lead oxide).
Regarding Claim 19, modified Murphy discloses the process for the electrochemical treatment of the wastewater with the screening current collector-based flow anode according to claim 8, but does not disclose wherein the device is a tube-in-tube device; and the cathode/anode separator and the cathode current collector are wound sequentially around the screening anode current collector. Nishimura suggests its device is a tube-in-tube device, and the cathode current collector is wound sequentially around the screening anode current collector, (See column 2, lines 16-31, Nishimura).
DeNora discloses wherein the device is a tube-in-tube device; and the cathode/anode separator and the cathode current collector are wound sequentially around the screening anode current collector, (See column 4, lines 44-68, column 5, lines 1-11, DeNora).
It would have been obvious to one of ordinary skill in the art before the effective filing date of the invention to have modified the process of modified Murphy by incorporating wherein the device is a tube-in-tube device; and the cathode/anode separator and the cathode current collector are wound sequentially around the screening anode current collector because the separator “preferably tubular, is…fastened” and “this fastening is particularly easy and forms a perfect hydraulic seal between the membranes and the…anodes which is difficult to obtain in conventional filter press cells”, (See column 4, lines 66-68, column 5, lines 1-5, DeNora).
Conclusion
Any inquiry concerning this communication or earlier communications from the examiner should be directed to JONATHAN M PEO whose telephone number is (571)272-9891. The examiner can normally be reached M-F, 9AM-5PM.
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/JONATHAN M PEO/Primary Examiner, Art Unit 1779