EP3478877A1 - Electrolyte system for the synthesis of sodium perchlorate, comprising an anode having an outer surface of boron-doped diamond - Google Patents
Electrolyte system for the synthesis of sodium perchlorate, comprising an anode having an outer surface of boron-doped diamondInfo
- Publication number
- EP3478877A1 EP3478877A1 EP17740459.7A EP17740459A EP3478877A1 EP 3478877 A1 EP3478877 A1 EP 3478877A1 EP 17740459 A EP17740459 A EP 17740459A EP 3478877 A1 EP3478877 A1 EP 3478877A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- electrolyte
- anode
- cathode
- sodium
- boron
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 239000003792 electrolyte Substances 0.000 title claims abstract description 49
- BAZAXWOYCMUHIX-UHFFFAOYSA-M sodium perchlorate Chemical compound [Na+].[O-]Cl(=O)(=O)=O BAZAXWOYCMUHIX-UHFFFAOYSA-M 0.000 title claims abstract description 28
- 229910001488 sodium perchlorate Inorganic materials 0.000 title claims abstract description 28
- 229910003460 diamond Inorganic materials 0.000 title claims abstract description 16
- 239000010432 diamond Substances 0.000 title claims abstract description 16
- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 14
- 238000003786 synthesis reaction Methods 0.000 title claims abstract description 9
- BZSXEZOLBIJVQK-UHFFFAOYSA-N 2-methylsulfonylbenzoic acid Chemical compound CS(=O)(=O)C1=CC=CC=C1C(O)=O BZSXEZOLBIJVQK-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000006056 electrooxidation reaction Methods 0.000 claims abstract description 21
- 239000011651 chromium Substances 0.000 claims description 13
- 229910001092 metal group alloy Inorganic materials 0.000 claims description 13
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 11
- 229910052804 chromium Inorganic materials 0.000 claims description 11
- 239000011248 coating agent Substances 0.000 claims description 11
- 238000000576 coating method Methods 0.000 claims description 11
- 239000000758 substrate Substances 0.000 claims description 11
- -1 alkali metal dichromate Chemical class 0.000 claims description 8
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims description 6
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 claims description 6
- 229910052796 boron Inorganic materials 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 229910000990 Ni alloy Inorganic materials 0.000 claims description 3
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 229910001093 Zr alloy Inorganic materials 0.000 claims description 3
- 229910052783 alkali metal Inorganic materials 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- ONTRRWKYBVZWST-UHFFFAOYSA-L disodium chlorate perchlorate Chemical compound [Na+].[Na+].[O-][Cl](=O)=O.[O-][Cl](=O)(=O)=O ONTRRWKYBVZWST-UHFFFAOYSA-L 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 9
- 239000000463 material Substances 0.000 description 7
- XTEGARKTQYYJKE-UHFFFAOYSA-M Chlorate Chemical compound [O-]Cl(=O)=O XTEGARKTQYYJKE-UHFFFAOYSA-M 0.000 description 6
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 6
- 239000000654 additive Substances 0.000 description 6
- 230000000996 additive effect Effects 0.000 description 6
- 239000010936 titanium Substances 0.000 description 6
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 5
- SOCTUWSJJQCPFX-UHFFFAOYSA-N dichromate(2-) Chemical compound [O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O SOCTUWSJJQCPFX-UHFFFAOYSA-N 0.000 description 5
- 239000010955 niobium Substances 0.000 description 5
- 230000003071 parasitic effect Effects 0.000 description 5
- 229910052726 zirconium Inorganic materials 0.000 description 5
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- 229910052759 nickel Inorganic materials 0.000 description 3
- 229910052758 niobium Inorganic materials 0.000 description 3
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- VLTRZXGMWDSKGL-UHFFFAOYSA-M perchlorate Chemical compound [O-]Cl(=O)(=O)=O VLTRZXGMWDSKGL-UHFFFAOYSA-M 0.000 description 3
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 3
- 229910052719 titanium Inorganic materials 0.000 description 3
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 2
- 229910001515 alkali metal fluoride Inorganic materials 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 229940005989 chlorate ion Drugs 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 239000012809 cooling fluid Substances 0.000 description 2
- YADSGOSSYOOKMP-UHFFFAOYSA-N dioxolead Chemical compound O=[Pb]=O YADSGOSSYOOKMP-UHFFFAOYSA-N 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 229910052735 hafnium Inorganic materials 0.000 description 2
- VBJZVLUMGGDVMO-UHFFFAOYSA-N hafnium atom Chemical compound [Hf] VBJZVLUMGGDVMO-UHFFFAOYSA-N 0.000 description 2
- 239000011244 liquid electrolyte Substances 0.000 description 2
- 229910052750 molybdenum Inorganic materials 0.000 description 2
- 239000011733 molybdenum Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- KMUONIBRACKNSN-UHFFFAOYSA-N potassium dichromate Chemical compound [K+].[K+].[O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O KMUONIBRACKNSN-UHFFFAOYSA-N 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 229910052715 tantalum Inorganic materials 0.000 description 2
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 2
- 229910052720 vanadium Inorganic materials 0.000 description 2
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 2
- JHWIEAWILPSRMU-UHFFFAOYSA-N 2-methyl-3-pyrimidin-4-ylpropanoic acid Chemical compound OC(=O)C(C)CC1=CC=NC=N1 JHWIEAWILPSRMU-UHFFFAOYSA-N 0.000 description 1
- GDDNTTHUKVNJRA-UHFFFAOYSA-N 3-bromo-3,3-difluoroprop-1-ene Chemical compound FC(F)(Br)C=C GDDNTTHUKVNJRA-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000010405 anode material Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- NROKBHXJSPEDAR-UHFFFAOYSA-M potassium fluoride Chemical compound [F-].[K+] NROKBHXJSPEDAR-UHFFFAOYSA-M 0.000 description 1
- 239000003380 propellant Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- PUZPDOWCWNUUKD-UHFFFAOYSA-M sodium fluoride Chemical compound [F-].[Na+] PUZPDOWCWNUUKD-UHFFFAOYSA-M 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/28—Per-compounds
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
- C25B11/042—Electrodes formed of a single material
- C25B11/043—Carbon, e.g. diamond or graphene
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
- C25B11/051—Electrodes formed of electrocatalysts on a substrate or carrier
- C25B11/073—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material
- C25B11/075—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of a single catalytic element or catalytic compound
Definitions
- the invention relates in particular to an electrolytic system for the synthesis of sodium perchlorate by electrochemical oxidation of sodium chlorate.
- Ammonium perchlorate (NH 4 CIO 4 ) is used in the space industry as a constituent of propellant shipments and is typically synthesized from sodium perchlorate (NaClO 4 ).
- Sodium perchlorate can, for its part, be obtained by electrochemical oxidation of sodium chlorate (NaCIOs).
- the electrochemical oxidation of sodium chlorate to sodium perchlorate is carried out with an electrolytic system comprising an anode and a cathode present in a bath comprising sodium chlorate.
- the oxidation reaction of the chlorate ion at the anode is accompanied by parasitic reactions at the cathode generating for example the formation of chlorine.
- the invention aims specifically to meet the aforementioned need.
- an electrolytic system for the synthesis of sodium perchlorate by electrochemical oxidation of sodium chlorate comprising at least:
- an electrolyte comprising sodium chlorate
- an anode present in the electrolyte having a boron-doped diamond outer surface
- the electrolytic system according to the invention implements an anode having an electrically active outer surface formed of a particular material and advantageously makes it possible to improve the efficiency of the electrochemical oxidation of sodium chlorate to sodium perchlorate.
- the anode may comprise an electrically conductive substrate coated with a boron-doped diamond coating.
- Such a configuration is advantageous insofar as it implements an anode having a limited amount of boron doped diamond and therefore reduced cost.
- an entirely boron-doped diamond anode may be used.
- the cathode may have an outer surface of a metal alloy having a mass content of chromium of between 5% and 25%.
- the implementation of such a cathode makes it possible, therefore, to render superfluous the step of separating sodium perchlorate from the dichromate or fluoride additive and thus to simplify the process for obtaining sodium perchlorate by electrochemical oxidation of sodium chlorate.
- the electrolyte may be free of fluoride or alkali metal dichromate.
- the metal alloy of the cathode may have a chromium mass content of between 10% and 25%, for example between 10% and 20%.
- the metal alloy of the cathode may be a steel, a nickel alloy or a zirconium alloy.
- a cathode having an outer surface of nickel or zirconium could be used.
- a cathode made entirely of nickel or zirconium could be used.
- the concentration of sodium chlorate in the electrolyte may be greater than or equal to 0.1 mol / L.
- the concentration of sodium chlorate in the electrolyte may be greater than or equal to 0.5 mol / L.
- the concentration of sodium chlorate in the electrolyte may for example be between 0.5 mol / L and Cs where Cs denotes the saturation concentration of sodium chlorate in the electrolyte, for example between 0.5 mol / L and 5 mol / L.
- the system may comprise a first chamber in which the electrolyte, the anode and the cathode are present and a second chamber, distinct from the first chamber, in which the electrolyte is present, the system being able to further comprising an electrolyte circulation circuit configured to flush the electrolyte between the first and second chambers.
- the invention provides a process for the manufacture of sodium perchlorate comprising a step of electrochemical oxidation of sodium chlorate to sodium perchlorate by implementing a system as described above.
- the current density imposed during the electrochemical oxidation can be between 1000 A / m 2 and 20000 A / m 2 , for example between 1000 A / m 2 and 5000 A / m 2 .
- FIG. 1 schematically represents an example of a system according to the invention
- FIGS. 2 and 3 schematically represent anode structures that can be used in the system of FIG. 1,
- FIGS. 4 and 5 schematically represent cathode structures that can be used in the system of FIG. 1;
- FIG. 6 is a graph obtained experimentally comparing the formation kinetics of sodium perchlorate obtained by implementing a system according to the invention with that obtained by implementing a system outside the invention, and
- FIG. 7 is a graph obtained experimentally comparing the gas flow rates generated during the use of a system according to the invention and a system outside the invention.
- FIG. 1 shows schematically an example of electrolytic system 1 according to the invention.
- This system 1 is configured to manufacture sodium perchlorate by electrochemical oxidation of sodium chlorate.
- the System 1 comprises a first chamber 3 in which a liquid electrolyte is present.
- the electrolyte 10 comprises sodium chlorate.
- the concentration of sodium chlorate in the electrolyte 10, before initiation of the electrochemical oxidation may be greater than or equal to 0.1 mol / L, for example 0.5 mol / L and for example be between 0, 5 mol / L and 5 mol / L.
- the electrolyte 10 may be an aqueous electrolyte.
- the electrolyte 10 is, moreover, free of fluoride or alkali metal dichromate.
- the electrolyte 10 is devoid of the following compounds: sodium fluoride (NaF), potassium fluoride (KF), sodium dichromate (Na 2 Cr 2 O 7 ) and potassium dichromate (K 2 Cr 2 O 7 ) .
- the system 1 further comprises an anode 15 and a cathode
- the anode 15 has an outer surface, corresponding to its active surface, diamond doped with boron.
- the boron-doped diamond may typically have a boron mass content of between 0.005% and 0.55%, the remainder being diamond. This external surface is present in the electrolyte 10.
- FIG. 2 illustrates the structure of an exemplary anode 15 that can be used in the system 1 of FIG. 1.
- the anode 15 comprises a conductive substrate of the Electricity 28 covered with a diamond coating doped with boron.
- the coating 26 defines the outer surface Si of the anode 15.
- the substrate 28 is formed of a material different from that constituting the coating 26.
- the material forming the substrate 28 may comprise titanium, zirconium, hafnium, vanadium , niobium, tantalum, palladium, molybdenum or an alloy thereof.
- the material forming the substrate 28 may for example be chosen from: titanium, zirconium, hafnium, vanadium, niobium, tantalum, palladium, molybdenum and their alloys.
- the material forming the substrate 28 may still be graphite.
- the thickness ei of the coating 26 may for example be greater than or equal to 0.5 ⁇ m, and for example be between 1 ⁇ m and 5 ⁇ m.
- an anode 115 made entirely of boron-doped diamond may be used. This anode 115 defines an outer surface S2.
- the cathode 17 has, for its part, an external surface, corresponding to its active surface which may, for example, be formed of a metal alloy having a mass content of chromium of between 5% and 25%.
- the outer surface of the cathode may alternatively be formed of zirconium or nickel. This outer surface is present in the electrolyte 10.
- the cathode may have an outer surface formed of a metal alloy having a chromium mass content of between 10% and 25%, for example between 10% and 20% .
- the metal alloy of the cathode 17 may be a stainless steel, for example 316L stainless steel, a nickel alloy or a zirconium alloy.
- the cathode 17 consists entirely of a metal alloy with a content mass of chromium of between 5% and 25% (massive metal alloy cathode with a mass content in chromium of between 5% and 25%).
- This cathode 17 defines an outer surface S 3 .
- the coating 118 defines the outer surface S 4 of the cathode 117.
- the substrate 119 is formed of a material different from that constituting the coating 118.
- the system 1 illustrated in FIG. 1 furthermore comprises an electric generator 20 connected to the anode 15 and to the cathode 17.
- the anode 15 is connected via the conductor 16 to the positive terminal 18 of the generator 20.
- cathode 17 is connected via the conductor 19 to the negative terminal 21 of the generator 20.
- the system 1 further comprises a second chamber 5, separate from the first chamber 3, wherein the liquid electrolyte is present.
- the presence of this second chamber 5 is optional.
- the second chamber 5 is in communication with the first chamber 3.
- the electrolyte 10 is intended to flow between the first 3 and second 5 chambers during the electrochemical oxidation.
- the system 1 comprises a circulation circuit of the electrolyte 7 which comprises in the illustrated example:
- the second channel 8 can, as illustrated, be provided with a valve 13, and
- a third channel 11 connecting an output of the pump 9 to an inlet 3e of the first chamber 3.
- the electrolyte 10 flows between the first 3 and second 5 chambers according to the path shown by the arrows F1. During its circulation, the electrolyte 10 passes through the first channel 12, the second channel 8 and the third channel 11.
- the second chamber is maintained at a substantially constant temperature by a thermostat 23 in which a temperature control fluid circulates (arrows F2).
- the thermostat 23 can for example, maintain the temperature of the second chamber at about 20 ° C.
- the system 1 may further include a condenser 25 for condensing at least a portion of the vapors produced during the electrochemical oxidation.
- a cooling fluid circulates in the refrigerant 25 to achieve this condensation (arrows F3).
- the cooling fluid is for example before heat exchange at a temperature of -5 ° C.
- the electrolyte 10 can flow continuously. It is possible to impose a flow rate of the electrolyte in the circuit 7 of between 250 liters / hour and 350 liters / hour, for example.
- the current density imposed during the electrochemical oxidation can be between lkA / m 2 and 20 kA / m 2 , for example between 1 kA / m 2 and 5 kA / m 2 .
- sodium perchlorate is obtained using a system without the second chamber 5. In the latter case, there is not necessarily movement of the electrolyte in the system.
- the experimental setup that has been used is of the type shown in Figure 1.
- the assembly has been equipped with a flow meter at the refrigerant outlet which quantifies the flow (in liters per hour: L / h) and the quantity of gases produced during electrolysis.
- the electrolytic system included a stainless steel cathode (316L steel having a chromium content of 18%). Two separate anode materials were tested. A first test according to the invention was carried out with a Nb / DDB anode having a niobium substrate coated with a boron-doped diamond coating. A second test outside the invention was carried out with a Ti / Pb0 2 anode having a titanium substrate covered with a coating of lead dioxide.
- Table 1 below and Figure 6 highlight the advantages conferred by the system according to the invention. It is found that the efficiency and the formation kinetics of sodium perchlorate are improved thanks to the system according to the invention in comparison with the system outside the invention using a Ti / Pb0 2 anode.
- chlorate ion and perchlorate ion material were determined by ion chromatography during the tests carried out.
- the current yield (Rdtcurrent) of the reaction is calculated as the ratio of the feedstock used for the oxidation of chlorate ions to perchlorate ions and the total load applied to the system.
- n io4- C designates the number of moles of ions perchlorates end of the synthesis
- F is the Faraday constant (96485 C.mol "1), the impressed current I (A) and t electrolysis time (s).
- the chemical yield (Rdtchim.) Of the synthesis is calculated by relating the number of moles of perchlorate ions formed to the number of moles of chlorate ions consumed.
- the progress of the synthesis (Av) is in turn determined by making the ratio between the number of moles of chlorate ions consumed and the number of moles of initial chlorate ions. n C107 (consumed) """
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Electrolytic Production Of Metals (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1656236A FR3053363B1 (en) | 2016-06-30 | 2016-06-30 | ELECTROLYTIC SYSTEM FOR THE SYNTHESIS OF SODIUM PERCHLORATE WITH ANODE WITH EXTERNAL SURFACE IN DIAMOND DOPED WITH BORON |
PCT/FR2017/051760 WO2018002548A1 (en) | 2016-06-30 | 2017-06-29 | Electrolyte system for the synthesis of sodium perchlorate, comprising an anode having an outer surface of boron-doped diamond |
Publications (1)
Publication Number | Publication Date |
---|---|
EP3478877A1 true EP3478877A1 (en) | 2019-05-08 |
Family
ID=57137057
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP17740459.7A Withdrawn EP3478877A1 (en) | 2016-06-30 | 2017-06-29 | Electrolyte system for the synthesis of sodium perchlorate, comprising an anode having an outer surface of boron-doped diamond |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP3478877A1 (en) |
JP (1) | JP2019520482A (en) |
FR (1) | FR3053363B1 (en) |
WO (1) | WO2018002548A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20230005243A (en) * | 2020-04-24 | 2023-01-09 | 파마젤 게엠베하 | Regioselective oxidation of heterocyclic alpha-amino amides |
FR3130856A1 (en) * | 2021-12-17 | 2023-06-23 | Arianegroup Sas | Electrolytic system for the synthesis of sodium perchlorate |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52120975A (en) * | 1976-04-06 | 1977-10-11 | Showa Denko Kk | Electrolytic cathode manufacturing of chlorates |
US4377454A (en) * | 1980-05-09 | 1983-03-22 | Occidental Chemical Corporation | Noble metal-coated cathode |
JPS596386A (en) * | 1982-06-30 | 1984-01-13 | Hodogaya Chem Co Ltd | Corrosion resistant activated cathode |
US5041196A (en) * | 1989-12-26 | 1991-08-20 | Olin Corporation | Electrochemical method for producing chlorine dioxide solutions |
JP3334996B2 (en) * | 1994-03-11 | 2002-10-15 | クロリンエンジニアズ株式会社 | Reduction-suppressed cathode and method for producing the same |
DE10258652A1 (en) * | 2002-12-13 | 2004-06-24 | Degussa Ag | Electrolytic manufacture of inorganic peroxygen compound, e.g. perhalogen acids, involves anodically oxidizing inorganic halogen compound in aqueous solution using anode with doped diamond coating |
JP2004202283A (en) * | 2002-12-20 | 2004-07-22 | Kurita Water Ind Ltd | Method and apparatus for treating organic compound-containing water |
JP4778320B2 (en) * | 2006-01-24 | 2011-09-21 | ペルメレック電極株式会社 | Electrosynthesis of perchloric acid compounds |
CN202246889U (en) * | 2011-10-24 | 2012-05-30 | 龚家正 | Novel perchlorate electrolytic bath |
EP2841625A4 (en) * | 2012-04-23 | 2015-08-05 | Chemetics Inc | Surface modified stainless steel cathode for electrolyser |
-
2016
- 2016-06-30 FR FR1656236A patent/FR3053363B1/en active Active
-
2017
- 2017-06-29 WO PCT/FR2017/051760 patent/WO2018002548A1/en unknown
- 2017-06-29 JP JP2018568887A patent/JP2019520482A/en active Pending
- 2017-06-29 EP EP17740459.7A patent/EP3478877A1/en not_active Withdrawn
Also Published As
Publication number | Publication date |
---|---|
WO2018002548A1 (en) | 2018-01-04 |
JP2019520482A (en) | 2019-07-18 |
FR3053363A1 (en) | 2018-01-05 |
FR3053363B1 (en) | 2021-04-09 |
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