Classifications

• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F9/00—Multistage treatment of water, waste water or sewage
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/24—Treatment of water, waste water, or sewage by flotation
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/34—Treatment of water, waste water, or sewage with mechanical oscillations
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
  • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
  • C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
  • C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
  • C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
  • C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
  • C02F1/56—Macromolecular compounds
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/72—Treatment of water, waste water, or sewage by oxidation
  • C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2209/00—Controlling or monitoring parameters in water treatment
  • C02F2209/06—Controlling or monitoring parameters in water treatment pH
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2209/00—Controlling or monitoring parameters in water treatment
  • C02F2209/08—Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2209/00—Controlling or monitoring parameters in water treatment
  • C02F2209/40—Liquid flow rate
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2301/00—General aspects of water treatment
  • C02F2301/02—Fluid flow conditions
  • C02F2301/024—Turbulent
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2301/00—General aspects of water treatment
  • C02F2301/04—Flow arrangements
  • C02F2301/046—Recirculation with an external loop
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2305/00—Use of specific compounds during water treatment
  • C02F2305/02—Specific form of oxidant
  • C02F2305/023—Reactive oxygen species, singlet oxygen, OH radical
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2305/00—Use of specific compounds during water treatment
  • C02F2305/02—Specific form of oxidant
  • C02F2305/026—Fenton's reagent

Definitions

• the present invention relates to a process for the purification of liquid effluents containing organic and / or mineral substances, dissolved or not.
• the invention also relates to a device for purifying such effluents. It finds a particularly important application although not exclusive in the field of the purification of the petroleum effluents or the effluents resulting from processes of manufacture of products resulting from
• COD or Chemical Oxygen Demand is the oxygen consumption by strong chemical oxidants, necessary for the oxidation of organic (and mineral) substances of water. It assesses the pollutant load of wastewater and measures all oxidizable substances, including those that are biodegradable.
• the quantity of biodegradable materials by biochemical oxidation (oxidation by aerobic bacteria that derive their energy from oxidation-reduction reaction) contained in the water to be analyzed is, for its part, defined by the BOD (Biological Oxygen Demand) parameter. .
• Liquid effluents often referred to as wastewater and the main example of this, are known to contaminate the environment in which they are discharged.
• non-biodegradable materials they contain are caused to be slowly oxidized by oxygen dissolved in water or by that of the air at the surface of the effluent.
• the present invention aims to provide such a method, and a corresponding effluent treatment device, better than those previously known to the requirements of practice, particularly in that it allows a compact, economical and effective treatment based on a combination of successive single or multiple treatments, comprising one or more clearly differentiated stages, namely: on the one hand, a step of mechanical and chemical aggression, the latter being either oxidizing, or reducing, or oxidizing / reducing, depending on the type of effluents to be treated, knowing that in the embodiments more particularly described, it is a radical oxidation also called hyperoxidation, and secondly a flotation step with skimming.
• the invention essentially proposes a process for the purification of liquid effluents charged with organic and / or mineral substances, dissolved or not, fed continuously at a flow rate Df, characterized in that, after a prior flotation operation if necessary, at least one treatment cycle is carried out, said treatment cycle comprising a first step in which a radical oxidation and / or a radical reduction of the effluents is effected by circulation in a first compartment, generating a very strong turbulence, then a second step in which is agglomerated by coagulation / flocculation the undissolved elements contained in the effluents before circulation of these last in a second compartment with free surface, with scraping sludge obtained in the upper part, by bubbling and maintaining a low turbulence in said compartment.
• the oxidation and / or reduction is done by electrolytic treatment.
• electrolytic treatment is meant here an oxidation and / or a reduction by an electrolysis process with very high electrochemical reactivity allowing the production of radical chemical species.
• Such a method makes it possible to obtain a COD below determined threshold values and, if necessary, to lower the COD / BOD5 ratio and / or the rate of MES below a second and a second, respectively.
• third threshold determined.
• stirring by recirculation pump in the compartment concerned such as the flow rate of the pump and greater than five times the flow Df continuous supply, and advantageously greater than ten times, see up to fifty times, see more of said flow Df.
• the vertical hydraulic regime in the chamber is in a highly turbulent regime (Re >> 3000 m 2 s-1) resulting, in combination with hyperoxidation, bursting and breaking long polluting molecules.
• Low turbulence means the maintenance of the hydraulic regime in the close compartment of the laminar flow (Re ⁇ 2000 m2 s-1), for example by a slight stirring obtained by recirculation of the effluents at a flow rate close to or less than that of the continuous supply, ie at a rate q ⁇ Df.
• the water to be purified is here itself used as a reagent by pumping and recirculation of the product itself purified and carrying an oxidizing function.
• the electrolytic treatment is an oxidation;
• a strong turbulence is generated in the first compartment by stirring by circulating the effluent between the top and bottom of said compartment at a flow rate Q> 5 Df;
• the recirculation flow rate is such that Q> 25 Df, advantageously Q> 40 Df or> 50 Df;
• the electrolytic treatment is carried out by circulation of the effluents collected in the lower part of the first compartment and reintroduction in the upper part of said compartment through an electrolysis circuit; the electrolytic treatment is carried out by electrolysis on electrodes coated with a layer comprising diamond and boron; the electrolytic treatment is carried out by electrolysis on electrodes coated with a layer comprising carbon and nitrogen atoms; low turbulence is maintained in the second compartment by circulating the effluents in the lower part of said compartment at a rate q ⁇ Df by means of external cavitation means to generate a vertical bubbling;
• the effluents are degassed at the outlet of the electrolysis circuit and the gases obtained are used to feed the external cavitation means of the vertical bubbling;
• the process comprises at least two treatment cycles;
• the process comprises at least one strongly oxidizing treatment cycle and at least one strongly reducing treatment cycle.
• strongly oxidizing or conversely strongly reducing
• one means essentially oxidant that is to say which makes lose (conversely gain) electrons to the chemical bodies present in the effluents;
• the effluents are circulated in series through n treatment cycles, the number n> 2 being arranged to gradually obtain a solid / liquid phase separation on the surface of the free surface compartments so as to bring the effluents out treatment at a given COD;
• each treatment cycle additionally comprises an intermediate step between the first and second stages, in which an operation of post-oxidation and / or reduction with catalyst is carried out.
• this operation is carried out in a third intermediate compartment, allowing the flow and the electrolytic bubbles to rise upwards.
• Advantageously also generates a mean turbulence in said third compartment; the flow Df is injected into the third compartment in the lower part of said compartment from a bypass of the electrolysis circuit, for example by circulating the effluents in the lower part of said medium flow compartment (Df ⁇ d ⁇ 3 Df).
• the post-oxidation and / or reduction operation is carried out by withdrawing the flow rate Df at the outlet of the electrolysis circuit;
• the pre-floating operation is carried out by bubbling after coagulation / flocculation then recirculation of the effluents in the lower part of a low-turbulence free-surface enclosure provided with scraping means in the upper part and cavitation means for generating vertical bubbling.
• the radical oxidant is, alone or in combination, chosen from the oxidants H2O2, O3, O0 or OH °; the process furthermore comprises a biological filtration.
• the invention also proposes a device implementing one or more of the embodiments of the method described above.
• a device for the purification of liquid effluents charged with organic and / or mineral substances, dissolved or not, fed continuously at a flow rate Df characterized in that it comprises at least a first set of two successive vertical compartments. , i.e. a first compartment provided with oxidation and / or radical reduction means of effluents and comprising means for generating in said first compartment a very high turbulence and a second compartment with a free surface of oxidation / separation arranged for maintain a low turbulence in said second compartment, said second compartment being provided with external coagulation / flocculation means, scraping means in the upper part, and bubbling means, the compartments communicating with each other at the bottom.
• a first compartment provided with oxidation and / or radical reduction means of effluents and comprising means for generating in said first compartment a very high turbulence and a second compartment with a free surface of oxidation / separation arranged for maintain a low turbulence in said second
• the coagulation / flocculation steps take place outside the second compartment by means of said external means.
• the effluents that have benefited from these two actions are then introduced into the second compartment, and will then be dissociated in water on one side and polluting supernatant on the other, by the action of bubbling in said effluents.
• the device comprises electrolytic treatment means for carrying out the oxidation and / or the reduction.
• treatment means for oxidation and / or reduction by electrolysis including electrodes
• the means for generating a very strong turbulence comprise a first circuit for recirculating the effluents collected in the lower part of the compartment and reintroduced in the upper part at a flow rate Q> 5 Df;
• the device comprises a low-turbulence free surface preliminary floating vessel comprising external coagulation / flocculation means and effluent recirculation means in the lower part, said enclosure being provided with scraping means at the top and cavitation means for generating a vertical bubbling for oxidation / separation in said enclosure;
• the electrolytic treatment means comprise electrodes coated with a layer comprising diamond and boron;
• the electrolytic treatment means e comprise electrodes coated with a layer comprising carbon and nitrogen atoms;
• the electrolytic treatment means are located on the first circuit for recirculating the effluents;
• the second compartment comprises a second circuit for re-circulating the effluents in the lower part comprising cavitation means for generating a vertical bubbling in said compartment;
• the second recirculation circuit is at a low flow rate, between 1/20 Df (one twentieth of Df) and 1/2 Df (one half Df);
• the device comprises at least a second set of compartments in series with the first; the device comprises n sets of compartments in which the effluents are circulated in series, the number n> 2 being arranged to gradually obtain a solid / liquid phase separation on the surface of the free surface compartments so as to bring the effluents at the end of treatment at a determined COD;
• each set of compartments comprises at least a third compartment intermediate between the first and second compartments, in which a post-oxidation and / or reduction operation is carried out with a catalyst while stirring with medium turbulence;
• the device comprises in the lower part of said third compartment a third effluent circulation circuit at a flow rate Df ⁇ d ⁇ 3 Df to generate a mean turbulence in said third compartment;
• the third intermediate compartment is supplied at the bottom from the first circulation circuit itself provided with electrolytic treatment means;
• the cavitation bubbling is carried out with air, the average dimension of the equivalent diameter of the bubbles being between 0.2 mm and 1 mm;
• the compartments have a useful height of between 3 m and 5 m;
• Figure 1 is an operating diagram of a first embodiment of a device according to the invention.
• Figure 2 is an operating diagram of a second embodiment of a device according to the invention.
• FIG. 3 is an operating diagram of a third embodiment of a device according to the invention.
• FIG. 4 is a schematic view illustrating a succession of processing cycles according to FIG. 3.
• FIG. 5 is a graph showing the decay of the COD in a succession of cycles of the type corresponding to FIG. 4.
• FIG. 6 is a diagram showing the steps implemented in one embodiment of a method according to the invention.
• FIG. 1 shows an effluent purification device 1 introduced continuously at 2 at a flow rate D f , for example Im3 / h.
• the effluents are loaded with organic and / or mineral substances, dissolved or not, for example with a COD of 30,000 mg of oxygen O 2 /! -
• the device 1 is for example formed by a tank
• the device comprises a pre-compartment or a floating chamber
• the float chamber 4 has a free surface 8 and comprises scraping means 9 for discharging the floating solid materials, for example in a recovery tank (not shown).
• a device formed by an open cylindrical vessel whose compartments and the preliminary chamber form radially arranged quarters, a sludge recovery compartment then being provided in said cylinder, after the second compartment, the scraping means being circular and rotating continuously.
• the float chamber 4 is fed at 10 via an inlet pump 11 at the top of the enclosure.
• the effluents are previously treated online via mixing tanks 12 and 13 by coagulating and flocculating.
• means 14 for supplying reagents comprise, for example, a first continuous supply tank 15, by metering pump 16 and solenoid valve 17, a coagulation reagent known per se and a second tank 18 for continuous supply by metering pump 19 and solenoid valve 20.
• a flocculation reagent also of known type adapted to each other depending on the effluent to be treated so as to reach the skilled person.
• the float chamber further comprises effluent recirculation means 21 at the lower part 22 at a low flow rate, for example substantially equal to the flow rate Df.
• These recirculation means 21 comprise a pump 23, for example 0.1 m 3 / hr, and cavitation means 24 for generating a vertical bubbling 25 in the float compartment via a pipework bent for optimum oxidation. and thus opening in the lower part of the enclosure 4.
• the first root oxidation compartment 5, also subsequently called hyperoxidation, is connected to the pre-floating chamber 4 in the lower part 27, via a passage for example of diameter corresponding to the flow Df, which is either formed by an orifice 28 formed in the partition wall 29 between the first compartment and floating chamber, or in the case where the enclosure float is remote from this compartment, via piping authorizing a flow Df.
• the first compartment 5 comprises external root oxidation means 30 comprising a circulating pump 31 for a large flow rate, for example 30 m 3 / h, and electrolysis oxidation means 32 comprising a plurality of electrodes 33, for example diamond, for example three sets of five consumable electrodes, arranged in parallel and in line with a supply pipe 34 opening in the upper part 35 of the first compartment 5.
• external root oxidation means 30 comprising a circulating pump 31 for a large flow rate, for example 30 m 3 / h
• electrolysis oxidation means 32 comprising a plurality of electrodes 33, for example diamond, for example three sets of five consumable electrodes, arranged in parallel and in line with a supply pipe 34 opening in the upper part 35 of the first compartment 5.
• this first compartment also has a free surface 8, but is closed at the top by a cover 36.
• the electrolytic radical oxidation means 30 are arranged to recirculate in the first compartment a flow rate of the order of 29 m 3 / h. (An average residence time of 1 hour is observed in the compartment of 1 m 3 , also fed via the orifice 28 at this rate of Im 3 / h).
• the circuit 30 also makes it possible to divert to the third intermediate compartment 6 a Df flow rate for post oxidation treatment.
• Control valves 37 arranged in parallel on the circuit 38 downstream of the electrodes 33 make it possible to regulate the flow rates between the first compartment 5 and the third intermediate compartment 6.
• the flow Df is injected at the bottom of the compartment here again and for example by a pipe 39 with a bend.
• a 40-introduction of a catalyst for example ferrous Fe2 + ions, or cuprous Cu + ions, or more generally metals close to losing an electron, such as sodium, which thus allow a treatment as effective as possible post oxidation.
• the catalysts will complete the work of free radical chemistry generated by electrochemistry, disproportioning the hydrogen or organic peroxides produced for example by incorporation in the downstream flow of Fe, Fe2O3, Fe3O4 in the form of solids.
• granular material implemented by a filter or a fluidized bed or by the injection of a solution of reduced ions such as Fe2 +.
• micro or nano porous supports such as activated carbons, resins or zeolites can be integrated either on each bottom zone or on the last zone. The function of these supports is then to fix, concentrate the diffuse pollutions on absorbent sites so that the water leaves definitively purified.
• the device 1 comprises the second compartment 7 with a free surface 41 of oxidation / separation, arranged to maintain a low turbulence in said compartment through a small pump 42 recirculation subject to bubbling oxidation means 43 via a cavitation device 44 known in itself.
• the scraping means 9 of the enclosure beforehand can for example also be used to scrape the free surfaces of all the compartments and in particular and more specifically the second and third compartments 7 and 6, which allow the separation by flotation of solidified products on the surface.
• the third intermediate compartment and the second compartment are interconnected at the bottom by means of coagulation / flocculation means 45 comprising a flow pump 46 Df and two reagent mixing blocks 47 and 48 known in themselves and located in line on the circuit. Finally, the flow Df is discharged at the top 49, for example by overflow, for possible subsequent treatment.
• FIG. 2 shows another embodiment of a device 50 according to the invention.
• the same reference numbers will be used to designate identical or similar elements.
• the device 50 comprises a preliminary floating chamber 4 provided with coagulation / flocculation means as described with reference to Figure 1 fed at the flow rate Df, for example 5 m3 / h.
• first hyperoxidation compartment provided with very high turbulence stirring means 51 comprising a high flow pump 52 and electrolysis oxidation means 53, for example with diamond electrodes as described above.
• the effluents are entering eg 50 rr / h in the lower part 54 of the first compartment 5 and reject in the upper part 56.
• the first compartment 5 which is here closed at 57, and although it has a free surface 58, by an optionally removable sealed cover, comprises a vertical chamber 59 of small parallelepipedic suction volume in the upper part 60 by a Df pump 61 supplying coagulation means / flocculation 62, known in themselves, before rejection in the lower part 63 of a second compartment 7 of the type described with reference to Figure 1.
• This second compartment which furthermore comprises cavitation bubbling means 43, is connected in the lower part 64 to an additional compartment 5A identical to the first compartment 5 described here before.
• FIG. 3 shows another embodiment of a device 70 according to the invention.
• This device 70 comprises a preliminary chamber 4 provided with flocculation / coagulation means as described above.
• An intermediate compartment 6 is advantageously supplied with 40-type catalyst Fe2 + as described herein. -before.
• FIG. 4 shows a device 80 according to a particularly advantageous embodiment of the invention comprising in this case more than two cycles, namely four identical treatment cycles of the type of those described with reference to FIG.
• a first compartment 5 itself hyperoxidized with very high turbulence, is supplied at the bottom.
• the effluents are then discharged for example by overflow to a second identical cycle 5 ', 6', 7 ', itself similarly feeding a third cycle 5'',6'',the''connected in turn in series with a fourth cycle 5 ''',6''', ⁇ ⁇ ⁇ r before evacuation for further treatment for example for biological treatment (not shown).
• FIG. 5 shows the graphical evolution (curve 81) of the COD content of pretreated effluents as a function of the addition of successive cycles of the type of those described with reference to FIG. 4, in which one sees therefore that said curve 81 decreases regularly.
• the effluent is, as we have seen, itself used to perform the desired physical and chemical work.
• a first step 82 of separation of suspended solids and colloids with low flow recirculation 83 within the preliminary chamber 84 is carried out hyper-oxidation or radical oxidation in circulation at a very high flow rate with recirculation 85 on diamond electrodes.
• the preliminary step 82 has made it possible, by means of the physicochemical treatment with flotation and micro-bubbling, to significantly reduce the COD on the elements most easily accessible by a conventional method.
• Step 84 proceeds, as we have just said, to a radical oxidation which will then be optionally repeated several times depending on the number of cycles.
• This phase of hyper-oxidation is the one that will really allow, especially if it is repeated, to destroy complex molecules.
• the hyperoxidation is carried out from OH 0 ions, obtained by electrolysis.
• a mass transfer is caused in contact with the electrodes and the presence of the most turbulent flow possible at the crossing thereof causes entrainment of microbubbles.
• the electrolysis also produces a very large concentration of micro bubbles which will turn out to work as surface-active structures of the organic molecule.
• the effluent to be treated thus consists of: "proteins, 2 to 3% of the dry matter.” Oily residues not recovered by centrifugation, including waxes (fatty acids with
• the effluent is mainly composed of carbon structures with long chains or assemblies of these molecular structures.
• Such an effluent after treatment with a two or even three hyperoxidation flotation cycle as described above has an initial flow rate of 5 m 3 / h for a total enclosure volume of the order of 26 m 3. allows to go down to a COD much lower than 500 mg / 1 or even 100 mg / 1.
• the following step is an intermediate stage 86 of natural flotation with bubbles via a cavitation circuit, before coagulation at 87, flocculation at 88 and then evacuation at 89 in a compartment with a free surface of type second compartment 7 described above, by recirculating low flow 90 with bubbling by cavitation to allow a flotation.
• the flow Df is also withdrawn at the top continuously in 91, with scraping solid foams obtained.
• This device has successfully treated the water of a chemical storage site containing traces of the products listed below, for a total COD of 500 to 2,000 mg / 1.
• the electrolytic treatment here has allowed oxidation and / or reduction depending on the molecule concerned, the following molecules being present Ethyl Acetate, Acetone, Heptanoic Acid, Sulfuric Acid, Benzene and Bitumen, Butyldiglycolether, Methylene Chloride, 1,2-Dichloroethane , Petrol, Ethanol, ethyl hexanol, Oils and additives, ISI butanol, Potash detergent, Methanol, methylethylcetone, Monoethylene glycol, Normal butanol, rather ethanol, propylene glycol, carbon tetrachloride, tetrahydrofuran, toluene, 1,1,1-trichloroethane, trichloromethane, trichlorethylene, heavy fuel, xylene.
• Table 1 shows the results obtained in tests carried out with a 3m 3 reactor, the simplified results of these tests are given in columns 1 to 11.
• Table 2 shows more particularly and by way of example the results obtained with some of the polluting molecules before and after treatment during one of the tests (test 2) of Table 1.
• Step No. 4 produces the hydroxyl radical used in the hyperoxidation reaction.
• the present invention is not limited to the embodiments more particularly described. On the contrary, it encompasses all the variants and in particular those where the gas recovery means are provided for supplying the venturi in the cavitation circuits of the second compartment, those where the first and second compartments are arranged one above the other. other to increase the compactness or those as described above where the radical oxidation means are combined (or not) with radical reduction means.

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• Life Sciences & Earth Sciences (AREA)
• Hydrology & Water Resources (AREA)
• Engineering & Computer Science (AREA)
• Environmental & Geological Engineering (AREA)
• Water Supply & Treatment (AREA)
• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Water Treatment By Electricity Or Magnetism (AREA)
• Physical Water Treatments (AREA)
• Treatment Of Water By Oxidation Or Reduction (AREA)
• Separation Of Suspended Particles By Flocculating Agents (AREA)

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