EP3870686A1

EP3870686A1 - Decontamination paste and method for decontaminating a substrate made of a solid material using said paste

Info

Publication number: EP3870686A1
Application number: EP19868217.1A
Authority: EP
Inventors: Alban GOSSARD; Mohamed Nidal BEN ABDELOUAHAB; Philippe COUSSOT
Original assignee: Commissariat a lEnergie Atomique CEA; Commissariat a lEnergie Atomique et aux Energies Alternatives CEA
Current assignee: Commissariat a lEnergie Atomique et aux Energies Alternatives CEA
Priority date: 2018-12-07
Filing date: 2019-12-05
Publication date: 2021-09-01
Also published as: FR3089520A1; JP2022510938A; WO2020115443A1; KR20210110607A; US20220049189A1; FR3089520B1; CN113166685A

Abstract

The invention relates to a decontamination paste comprising at least one inorganic viscosifier selected from clays, at least one compound in the form of fibers and optionally further one or more optional components, the remainder being of solvent. The invention also relates to a method for decontaminating a substrate made of a solid material using said paste, said substrate being contaminated by at least one contaminant species referred to as the labile contaminant species and/or by at least one contaminant species referred to as the surface contaminant species located on one of the surfaces thereof, and/or by at least one contaminant species referred to as the subsurface contaminating species located just below said surface, and/or by at least one contaminant species located under said surface in the depth of the substrate.

Description

DECONTAMINATION PASTE AND METHOD FOR DECONTAMINATION OF A SUBSTRATE IN A SOLID MATERIAL USING THE SAME

DESCRIPTION

TECHNICAL AREA

The present invention relates to a decontamination paste usable for the decontamination of substrates made of solid, contaminated materials.

The present invention further relates to a decontamination process using this decontamination paste.

By decontamination or depollution of a substrate means the elimination of pollutants, contaminants of this substrate.

By contaminants, or contaminating species, we generally mean substances, compounds, which are not normally part of the substrate material and whose presence is not desired.

These contaminants can be found on a surface of the substrate, just below the surface of the substrate (subsurface), or deep in the substrate.

The process and the paste according to the invention allow the decontamination of all kinds of materials, such as metallic materials, plastics, minerals such as vitreous materials.

The process and the paste according to the invention apply as well to the decontamination of substrates made of dense materials as to the decontamination of substrates made of porous materials such as cementitious materials such as mortars and concretes; the bricks ; plasters; and natural stone.

The process and the paste according to the invention also allow the elimination of all kinds of contaminants and in particular chemical, biological, or nuclear, radioactive contaminants. The process and the paste according to the invention can therefore be qualified in particular as a NRBC decontamination process and paste (Nuclear, Radiological, Biological, Chemical).

The technical field of the invention can thus, in general, be defined as that of the decontamination of contaminated substrates with a view to eliminating pollutants, contaminants, contaminating species which are on their surface, just below their surface (in subsurface), or deep into the substrate.

PRIOR STATE OF THE ART

The decontamination or decontamination of solid materials is a problem which arises in many fields, in particular in the nuclear industry, for example for sanitation operations or maintenance of installations, in certain industries using toxic chemicals. , but also, for example, in the context of decontamination operations that may be necessary following an NRBC (Nuclear, Radiological, Biological and Chemical) type accident.

Different types of contamination of a solid material can be identified: labile contamination, in particular in the form of dust, not adhering to the surface to be decontaminated.

so-called “surface” contamination: the contaminants are present and adhere to the surface of the substrate in a solid material (within a layer of grease for example).

a so-called “sub-surface” contamination: the contamination is embedded in the first (ie) microns from the surface of the solid substrate (within an oxide layer of a metal for example).

deep contamination which is specific to substrates made of porous materials. Contaminants have diffused within the porous network and are found embedded in the material a few millimeters, even centimeters, deep.

In the context of decontamination operations, the process used is generally adapted to the type of contamination targeted and to the outlets for the final waste generated. Thus, labile contamination can be eliminated by using methods implementing a simple aspiration of this contamination. Labile contamination can also be eliminated by applying a peelable gel to the surface to be decontaminated, which will then act as an adhesive tape and remove the labile contamination from the support [1].

These peelable gels are organic and are only effective for labile contamination. They therefore generate organic waste. In addition, their application with an excessively large thickness (for example greater than 2 mm) may cause gel drips which will weaken the mechanical properties of the peelable gel formed.

Different methods exist for treating surface and sub-surface contamination:

mechanical processes based on cutting, physical abrasion, shot blasting or shaving techniques. Although these methods are inexpensive and relatively simple to implement, they prove to be very tedious and painful for operators, they degrade the structure of the material and generate a large volume of waste.

chemical processes using acid, basic or oxidizing solutions. Such methods rely on corrosion of the material over a few microns in order to extract the contaminants. The material is therefore slightly degraded and its decontamination is carried out only at shallow depths. In addition, liquid waste is produced which must then be treated and recovered. These acidic, basic or oxidizing solutions can also be incorporated into decontamination gels [2] or foams [3] in order to improve their efficiency and reduce the volume of secondary waste generated.

Foam processes generate small amounts of liquid effluent.

The methods using gels generate solid waste of millimeter size which can be aspirated, if their implementation by spraying is controlled. In fact, controlling the thickness of the deposited gel is essential in these processes in order to avoid the formation of a waste of a thickness that is too thin and too adherent to the substrate (in the event of deposit of a thickness of gel that is too fine) or the appearance of streaks on non-horizontal surfaces (in the event of depositing a thickness of gel that is too thick). These gels do not allow the treatment of porous materials and generally do not contain contaminating species well.

Finally, the chemical processes are thus above all effective for surface and sub-surface decontamination and are very ineffective at removing contaminants deeply embedded in a substrate.

methods based on laser ablation [4]. This type of process consists in eroding successive layers of the contaminated material using a laser beam coupled to a suction system allowing the recovery of the generated waste. These “laser” processes are however quite expensive and restrictive to implement.

Deep decontamination of porous materials is much more complex than labile, surface or sub-surface decontamination because contaminants tend to be incorporated deep into the porous network.

The methods presented above for surface and sub-surface decontamination can still be used for deep decontamination but, on the one hand, their effectiveness is limited and, on the other hand, they produce a very large amount of waste. which may prove problematic to manage, especially in the case of a nuclear decontamination operation.

However, there are specific methods for deep decontamination of porous materials.

These are first of all electrokinetic processes [5] which are based on the electro-migration of ionic contamination within the porous material, and in particular within reinforced concrete, thanks to the placement of electrodes and to the application of a current. These processes have a high cost price and require fairly substantial resources for their implementation. In addition, the application of excessively large currents can lead to the degradation of the infrastructures during treatment.

Document [6] presents a process for decontaminating porous materials deeply contaminated by radionuclides. The process described is dedicated to ionic nuclear contamination, and no indication is given as to the possibility of modifying it for use in fields other than nuclear. This document presents a two-step process. In a first step, the porous material is soaked in an ionic solution capable of dissolving the radionuclides present in the porosity. This first step can cause sagging and the production of liquid effluents that are difficult to recover and treat. In addition, in the case of areas with complex geometries or large surfaces such as installation walls, the porous material may be inhomogeneously imbibed, consequently reducing the efficiency of the process. Following this first soaking step, an organic hydrogel containing radionuclide chelating agents is brought into contact with the soaked porous material in order to extract the solubilized contaminants.

Document [6] only mentions organic gelling agents which can be sensitive to irradiation, in particular in the specific case of nuclear decontamination, and which could produce radiolysis gases (H2 in particular).

This problem can prove to be prohibitive when packaging the final waste.

The claims of this document relate to a dry composition before mixing with an aqueous solution but no information is given on the composition of the hydrogel and in particular on the influence of the amount of aqueous solution to be added. In addition, no clear indication regarding the application process and the use of the hydrogel is given. In particular, this document does not discuss the influence of the thickness of the hydrogel deposited, the means of implementation of this hydrogel as well as the quantities of hydrogel necessary to treat a given surface.

Document [7] presents a dry composition for a compress to be used for cleaning or desalination of porous materials, more particularly for the treatment of polluted stones in the context of the restoration of monuments.

This dry composition comprises a binder, a filler and a mineral fiber. Due to the intended application which is very restrictive, namely the desalination and cleaning of historic monuments, very specific criteria must be met (mainly safety criterion), giving rise to dry compositions of fairly complex compresses with at least minus 3 components.

This document also relates to a cleaning or desalination pad ready for use which comprises the dry composition, from 50% to 80% by weight of a solvent, and optionally a solubilization reagent. The compress is then deposited on the surface to be treated.

The compress is then allowed to dry and the salts dissolved in the solvent which has penetrated into the material to be treated are extracted by migration to the compress. After drying, the remains of the compress are removed by a final rinse, producing liquid effluents, and by simultaneous aspiration.

The effectiveness of the cleaning and / or desalination obtained by the compress of the document [7] is not demonstrated, in particular by concrete examples, and is probably weak. In general, the use of compresses today remains strictly limited to the desalination of stones in the context of the restoration of monuments.

Furthermore, it should be noted that the treatment of vertical walls poses particular problems. Thus, in order to treat a vertical wall over a large area using a gel or a compress, a significant thickness of deposit is sometimes necessary in order to obtain a high decontamination efficiency and a non-pulverulent waste (in for example the decontamination of dense substrates with gels) or in order to decontaminate a vertical porous surface by extraction mechanisms based on physical phenomena such as the transfer of fluids or advection. However, the composition of the gels and compresses described respectively in documents [2] and [7] does not allow these gels and compresses "to hold" on a vertical wall, to hang on this wall, without sagging, to flow, when 'They are applied to this vertical wall with a significant thickness, in particular a centimeter thickness.

The maximum thickness of these gels and compresses that can be applied without sagging is a few millimeters.

There is therefore, in light of the above, a need for a composition, decontamination product, and for a decontamination process which does not have the drawbacks, defects, limitations and disadvantages of the compositions, decontamination products of the prior art as represented in particular by the compositions and methods described above in documents [1] to [7]. In particular, there is a need for a composition, decontamination product, and for a decontamination method which provide the following improvements, in particular with respect to aspirable decontamination gels and methods implementing these gels. :

an improvement in the properties of the ultimate waste. In fact, aspirable gels do not generally confine contaminating species which are only adsorbed on the surface of the final waste or mechanically trapped within the flakes of dry gel.

an improvement in the size of final waste. In fact, the aspirable gels used for surface or sub-surface decontamination generate non-pulverulent waste of millimeter size. It would therefore be desirable to obtain larger waste to avoid resuspension in the air.

an improvement in the versatility, reliability and reproducibility of the process. Indeed, the effectiveness of the processes using vacuum gels is largely based on spraying which must be well controlled. In some cases, improper application of the gel, in particular if the applied gel layer is too thin, results in poor decontamination and the formation of solid waste which is also too fine and too adherent to the substrate. This too fine and too adherent waste proves difficult to recover. It would therefore be desirable to have a method which is easy to implement, reliable, reproducible, precise, and more robust than known methods and which is much less sensitive to the hazards that may occur during its implementation.

apart from the deep abrasion methods, there is currently no composition and decontamination method which allow effective decontamination of a material in depth. It would therefore be desirable to have a composition and a process which allow such deep decontamination while generating a small volume of final waste.

In summary, there is currently no composition or decontamination process which satisfactorily allows decontamination that is at the same time labile, surface, sub-surface and in depth of solid materials. And so there is a need for such a composition and such a process which are, in addition, among others, of a low cost, reliable, simple to implement, which do not produce liquid effluents but only solid waste of large size, know generally greater than the centimeter.

In particular, there is a need for an effective composition and process for deep nuclear decontamination of porous materials. These materials can have a large surface.

STATEMENT OF THE INVENTION

This object, and still others are achieved, in accordance with the invention, by a decontamination paste comprising, preferably consisting of:

at least one inorganic viscosifier chosen from clays, said inorganic viscosifier representing from 20% to 70% by mass, preferably from 35% to 70% by mass, more preferably from 40% to 65% by mass, better still 45 to 55% by mass of the total mass of the dough, and said inorganic viscosifying agent being in the form of particles of micron and / or nanometric size;

at least one compound in the form of fibers;

optionally, in addition, one or more component (s) chosen from the following components:

at least one surfactant;

at least one active decontamination agent;

at least one agent extracting contaminating species;

at least one agent chelating contaminating species;

at least one coloring agent;

and the rest of the solvent.

Advantageously, the said component (s) is (are) present in the following proportions: 0.1 to 8 or 10% by mass, preferably 0.1 to 5% by mass, more preferably 0.5 to 5% by mass, better 1 to 5% by mass, better still 1 to 3% by mass relative to the mass of the dough, of the at least one compound in the form of fibers;

optionally, 0.1% to 2% by mass, relative to the mass of the paste, of the at least one surfactant;

optionally, 0.1 to 10 mol / L of dough, preferably 0.5 to 10 mol / L of dough, more preferably 1 to 10 mol / L of dough, and better still 3 to 6 mol / L of dough, at least one active decontamination agent;

optionally, 0.1% to 5% by mass, relative to the mass of the paste, of the at least one agent extracting contaminating species;

optionally, 0.1% to 5% by mass, relative to the mass of the paste, of the at least one chelating agent for the contaminating species;

optionally 0.01% to 10% by mass, preferably 0.1% to 5% by mass, relative to the mass of the paste, of the at least one coloring agent;

and the rest of the solvent.

The sum of the percentages by mass of all the components, constituents of the dough is obviously 100% by mass.

By "solvent residue" is meant that the solvent is always present in the paste, and that the amount of solvent is such that when added to the amounts of the components of the paste other than the solvent (that these components are mandatory or possible components mentioned above, or other optional additional components mentioned or not mentioned), the total amount of all the components of the dough is 100% by mass.

By particles of micron size, it is meant that these particles have an average size, generally defined by their largest dimension of more than 0.1 µm to 100 µm, preferably from 1 to 100 µm, for example more than 0.1 pm to 4, 5 or 10 pm.

Preferably, said inorganic viscosity agent is present only in the form of particles of micron size. By nanometric size particles, it is meant that these particles have an average size, generally defined by their largest dimension of 1 to 100 nm.

The dough according to the invention comprises a specific amount of a specific clayey inorganic viscosifying agent giving the dough a viscosity suitable for its use, at least one compound in the form of fibers, and a solution comprising a solvent, and optionally one or more optional components which are generally chosen according to the particular application which is made of the dough.

The term "paste" is well known to those skilled in the art, who know that a paste is intrinsically different from a gel constituted by a colloidal solution.

The dough according to the invention generally has a viscosity greater than or equal to 100 Pa.s at 20 ° C for a shear less than 1 s ¹ .

Depending on the component (s) it contains, the solution allows attack of the substrate, solubilization of the contaminating species, or fixation of the contaminating species during the decontamination step (see below).

The decontamination paste according to the invention has never been described or suggested in the prior art.

The decontamination paste according to the invention differs fundamentally from the decontamination compositions according to the prior art and in particular from the aspirable gels of the prior art in that it contains a specific inorganic viscosifying agent chosen from clays and not from silicas and aluminas, and in that the amount of this inorganic viscosity agent in the dough is greater than the amount of inorganic viscosity agent in the aspirable gels. In fact, the amount of this inorganic viscosifying agent in the dough is from 20% to 70% by mass, preferably from 35% to 70% by mass, more preferably from 40% to 65% by mass, better still from 45 to 55% The decontamination paste according to the invention also differs fundamentally from decontamination compositions according to the prior art and in particular from the aspirable gels of the prior art in that it contains at least one compound in the form of fibers.

In addition, preferably, the inorganic viscosifier is present only in the form of particles of micron size.

This micron size also favors obtaining large solid waste. The paste according to the invention meets all the needs listed above, achieves the goals mentioned above and solves the problems of the decontamination compositions of the prior art.

Thus, the paste according to the invention makes it possible, surprisingly, to eliminate both labile contamination, sub-surface contamination, and deep contamination (for example contamination embedded in a porous network of a substrate made of a porous material).

Due to the specific inorganic viscosity agent, chosen from clays, that it contains, the large, specific amount of inorganic viscosity agent and preferably the presence of the inorganic viscosity agent in the specific form of particles. micron-sized, the paste according to the invention can, surprisingly hold, without flowing, without sagging on vertical walls even when applied to these walls with a thickness much greater than that with which the gels are applied. aspirable. This thickness is in particular from 2 to 5 mm.

As the dough according to the invention also contains a compound in the form of fibers, then this thickness can be greater than 5 mm.

Thanks to the significant and significantly increased deposit thickness (compared to aspirable gels) that can be obtained with the paste according to the invention, the decontamination effect, in particular the corrosive effect, is greater, which thus allows deeper and sub-surface decontamination.

Despite the large, specific amount of inorganic viscosity agent it contains, the paste according to the invention nevertheless retains a handy consistency allowing its easy application on any surface. In addition, the number of fractures which appear during the drying of the dough according to the invention is considerably reduced compared to aspirable gels and a solid waste consisting of pieces, non-pulverulent particles, and of much larger sizes than the waste obtained. after drying vacuum gels is obtained.

The waste obtained after drying the gel according to the invention generally has a size (the size being defined by their largest dimension) greater than or equal to one cm, or even greater than or equal to 10 cm. Often, the final dry waste presents little fractures (one, two, for example), or even no fracture, and it is then the same size as the “wet” gel deposit initially deposited (see examples).

The fact of using clays in fact makes it possible to avoid fractures because the latter are better organized during drying.

Within waste, which is large, contaminating species can be chemically adsorbed.

The presence in the dough according to the invention, of a compound in the form of fibers, even in the small quantities mentioned above, ensures better internal resistance of the dough without modifying the advantageous properties of decontamination and drying. Thus, the compound in the form of fibers ensures that an even greater thickness of dough, for example greater than or equal to 5 mm, preferably greater than or equal to 6, 7, 8 or 9 mm, more preferably at least 10 mm -and up to 50 mm, for example, on a vertical wall without sagging, and after drying a solid non-pulverulent waste is always obtained. This is demonstrated in Example 4.

It should be noted that it is not necessary for the dough to contain one or more of the optional components mentioned above.

Indeed, for certain types of contaminating species, a paste comprising only the solvent, the viscosifying agent, and the compound in the form of fibers, makes it possible to successfully implement the method according to the invention by trapping, capturing, capturing contaminating species, and allows to obtain the effects and advantages listed above. In this case, for these types of contaminating species, the clays play both the role of viscous agent and the role of "trapper", "fixer".

However, for other types of contaminating species, which are not "trapped" by clay, optional components are required to trap these contaminating species. These optional components can be extracting agents from contaminating species and / or chelating agents from contaminating species.

The presence of a surfactant in the paste according to the invention has a favorable and significant influence on the rheological properties of the paste. This surfactant in particular promotes the recovery of viscosity of the paste after its application and prevents risk of spreading or sagging when the paste is deposited on vertical surfaces and ceilings.

The presence in the dough of at least one active decontamination agent makes it possible to eliminate, destroy, inactivate, kill, extract the contaminating species whether they are labile, surface, sub-surface or deep below the surface of the substrate of the solid substrate.

The presence in the paste of at least one extracting and fixing agent for the contaminating species, such as an inorganic adsorbent makes it possible to facilitate the capture and the fixing of the contaminating species, and also makes it possible to avoid a release of the contaminating species in the case of a possible leaching, in particular of an undesired leaching, of the final dry and solid residue. The treatment of the waste resulting from the decontamination operation using the paste according to the invention is greatly facilitated.

As already specified above, the clays can possibly, in certain cases play both the role of viscous agent and the role of “trapper”, “fixative”.

The presence in the paste of at least one agent chelating contaminating species also makes it possible to facilitate the capture and the fixation of the contaminating species.

In particular, the presence of extracting and / or chelating agents in the paste, or more exactly in the solution forming part of the paste makes it possible to promote the recovery of contaminants chemically linked within the porosity of a material, such as, for example a cementitious material.

The presence of at least one coloring agent in the paste makes it possible to better visualize, locate the final dry and solid residue at the end of the process, whatever the surface on which it is deposited, which facilitates the recovery of this residue.

Due to the use of a viscosity agent generally exclusively inorganic, mineral, without organic viscosity agent, the organic matter content of the pulp according to the invention is generally less than 4% by mass, preferably less than 2% in mass, which constitutes an advantage of the dough according to the invention.

These solid, mineral, inorganic clay particles act as viscosants to obtain the desired pasty consistency. Advantageously, the inorganic viscosity agent can be chosen from smectites, kaolinites, perlites, vermiculites, and their mixtures.

The nature of the mineral, inorganic viscosifying agent unexpectedly influences the drying of the paste according to the invention and the particle size of the residue obtained.

The decontamination paste according to the invention contains a compound in the form of fibers.

Advantageously, the fibers can be chosen from fibers of organic compounds such as cellulose fibers, and fibers of mineral compounds such as rock wool and glass wool.

The fibers can have a diameter of 2 µm to 10 µm.

The fibers can have a length of 50 µm to 10 mm.

The paste according to the invention may contain an active decontamination agent.

This active decontamination agent can be any active decontamination agent making it possible to eliminate a contaminating species whatever the nature of this contaminating species: whether this contaminating species is chemical, biological or even nuclear, radioactive - in other words, this decontamination agent can be any “NRBC” (Nuclear, Biological, Radiological, Chemical) decontamination agent, or whether this contaminating species is organic or mineral, liquid or solid.

The paste according to the invention can thus contain an active agent for biological, chemical or nuclear, radioactive decontamination.

The active decontamination agent can also be a degreasing agent, pickling in order to eliminate any contaminating species found on the surface and possibly below the surface and into the depth of the substrate.

Certain active decontamination agents can simultaneously play several decontamination functions.

By biological decontamination agent which can also be described as a biocidal agent, or a disinfecting agent, is meant any agent which, when brought into contact with a biological species and in particular a toxic biological species, is capable of inactivate or destroy it. By biological species is meant any type of microorganism such as bacteria, fungi, yeasts, viruses, toxins, spores, in particular spores of Bacillus anthracis, prions, and protozoa.

The biological species which are eliminated, destroyed, inactivated by the paste according to the invention are essentially biotoxic species such as pathogenic spores, for example spores of Bacillus anthracis, toxins such as, for example, botulinum toxin or ricin, bacteria such as Yersinia pestis bacteria and viruses such as vaccinia virus or haemorrhagic fever viruses, for example of the Ebola type.

By chemical decontamination agent is meant any agent which, when it is brought into contact with a chemical species and in particular a toxic chemical species, is capable of destroying or inactivating it.

The chemical species which are eliminated by the paste according to the invention are in particular toxic chemical species such as toxic gases, in particular neurotoxic or vesicants.

These toxic gases are in particular organophosphorus compounds, among which mention may be made of Sarin or GB agent, VX, Tabun or GA agent, Soman, Cyclosarin, diisopropyl fluoro phosphonate (DFP), Amiton or VG agent, the Parathion. Other toxic gases are mustard gas or agent H or agent HD, Lewisite or agent L, agent T.

The nuclear, radioactive species which can be eliminated by the paste according to the invention can be chosen, for example, from metal oxides and hydroxides, in particular in the form of solid precipitates.

It should be noted that in the case of radioactive species, there is no talk of destruction or inactivation but only of elimination of the contamination by dissolution of the irradiating deposits or corrosion of the materials supporting the contamination. There is therefore a real transfer of nuclear contamination to the solid waste obtained after drying of the pulp.

The active decontamination agent, for example the active biological or chemical decontamination agent can be chosen from bases such as sodium hydroxide, potassium hydroxide, and mixtures thereof; acids such as nitric acid, acid phosphoric, hydrochloric acid, sulfuric acid, hydrogen oxalates such as sodium hydrogen oxalate, and mixtures thereof; oxidizing agents such as peroxides, permanganates, persulfates, ozone, hypochlorites such as sodium hypochlorite, IV cerium salts, and mixtures thereof; quaternary ammonium salts such as hexadecylpyridinium (cetylpyridinium) salts, such as hexadecylpyridinium chloride (cetylpyridinium); reducing agents; and their mixtures.

For example, the active decontamination agent can be a disinfecting agent such as bleach, which provides the dough with decontamination, biological and / or chemical depollution properties.

Certain active decontamination agents can be classified among several of the categories defined above.

Nitric acid is therefore an acid, but also an oxidizing agent.

The active decontamination agent, such as a biocidal agent, is generally used at a concentration of 0.1 to 10 mol / L of pulp, preferably of 0.5 to 10 mol / L of pulp, more preferably of 1 to 10 mol / L, and better still 3 to 6 mol / L of dough in order to guarantee a decontamination power, for example a power of inhibition of biological species, in particular biotoxic, compatible with the drying time of the dough, and to ensure, for example, a drying of the dough at a temperature between 20 ° C and 50 ° C and at a relative humidity between 20% and 60% on average in 30 minutes to 5 hours.

In order to achieve total efficiency, including under the most unfavorable temperature and humidity conditions with respect to drying time, the formulation of the paste supports different concentrations of active agent. It can be noted, in fact, that the increase in the concentration of decontamination agent more particularly in acid or basic decontamination agent considerably increases the drying time of the paste and therefore the efficiency of the process.

The active decontamination agent can be an acid or a mixture of acids. These acids are generally chosen from mineral acids such as hydrochloric acid, nitric acid, sulfuric acid and phosphoric acid.

A decontaminating agent, in particular a particularly preferred biological decontaminating agent is nitric acid. Indeed, it turned out in a completely surprising way that nitric acid destroyed, inactivated, biological species, in particular biotoxic ones.

In particular, it has been surprisingly demonstrated that nitric acid destroys and inactivates spores such as the spores of Bacillus thuringiensis which are particularly resistant species.

The acid or acids is (are) preferably present at a concentration of 0.5 to 10 mol / L, more preferably from 1 to 10 mol / L, better still from 3 to 6 mol / L to ensure drying of the dough generally at a temperature between 20 ° C and 50 ° C and at a relative humidity between 20% and 60% on average in 30 minutes to 5 hours.

Another preferred contaminant is a mixture of nitric acid and phosphoric acid. The paste according to the invention can then be constituted by a clay, such as kaolinite, and by an acidic aqueous solution of nitric acid, for example IM, and phosphoric acid for example IM, the clay representing for example 40% to 60% by mass of the mass of the dough, and the acidic aqueous solution representing for example from 60% to 40% by mass of the mass of the dough.

Alternatively, the active decontamination agent, for example the active biological decontamination agent, may be a base, preferably an inorganic base, preferably chosen from soda, potash, and mixtures thereof.

In the case of such a basic paste formulation, the paste according to the invention has, in addition to the decontamination action, a degreasing action which also makes it possible to eliminate any contaminating species on the surface of the substrate.

As already mentioned above, in order to achieve total efficiency, including under the most unfavorable climatic conditions with respect to the drying time of the dough, the dough according to the invention can have a large concentration range of basic decontamination agent (s).

Indeed, increasing the concentration of basic decontamination agent such as NaOH or KOH, generally playing the role of biocidal agent, makes it possible to considerably increase the inhibition rates of biological species, as has been demonstrated for spores of Bacillus thuringiensis. The base is advantageously present at a concentration of less than 10 mol / L, preferably between 0.5 and 7 mol / L, more preferably between 1 and 5 mol / L, better still between 3 and 6 mol / L, to ensure a drying of the dough at a temperature between 20 ° C and 50 ° C and at a relative humidity between 20% and 60% on average in 30 minutes to 5 hours.

The decontamination agent, in particular when it is a biological decontamination agent, is preferably sodium hydroxide or potassium hydroxide.

With regard, for example, to the kinetics of inhibition of spores and the durations of drying of the pastes as a function of the temperature, the active decontamination agent, in particular when it is a biocidal agent, will preferably be hydroxide. sodium at a concentration between 1 and 5 mol / L.

The paste according to the invention may optionally also contain a surfactant or a mixture of surfactants, preferably chosen from the family of nonionic surfactants such as block copolymers, block copolymers such as block copolymers of 'ethylene oxide and propylene oxide, and ethoxylated fatty acids; and their mixtures.

For this type of paste, the surfactants are preferably block copolymers marketed by BASF under the name PLURONIC ^®.

Pluronics ^® are block copolymers of ethylene oxide and propylene oxide.

These surfactants influence the rheological properties of the dough, in particular the thixotropic nature of the product and its recovery time and avoid the appearance of sagging.

Advantageously, the agent extracting contaminating species is chosen from inorganic adsorbents such as zeolites, clays, phosphates such as apatites, titanates such as sodium titanates, and ferrocyanides and ferricyanides.

This optional extracting agent such as a zeolite or a clay can be used in the case where the contaminating species is a radionuclide, but this optional extracting agent can also be used in the case of contaminating species other than radionuclides, such as for example metals, such as toxic metals or heavy metals.

Advantageously, the chelating agent of the contaminating species is chosen from n-octylphenyl-N oxide, N-diisobutylcarbamoyl methylphosphine (CMPO), tributyl phosphate (TBP), l-hydroxyethane-1,1 diphosphonic acid ( HEDPA), di-2-ethylhexylphosphoric acid (DHEPA), trioctylphosphine oxide (TOPO), diethylenetriamine pentaacetate (DTPA), primary, secondary and tertiary organic amines, cobalt dicarbollide, calixarenes, niobates , ammonium molybdophosphate (AMP), (trimethylpentyl) phosphinic acid (TPPA), and mixtures thereof.

The extracting agent can sometimes act as a chelating agent and vice versa.

Advantageously, the coloring agent is chosen from dyes, preferably organic dyes, and pigments, preferably mineral dyes.

Advantageously, the pigment is a mineral pigment. In this regard, reference may be made to document WO-A1-2014 / 154817 [7].

There is no limitation as to the mineral pigment which is incorporated into the paste according to the invention.

Generally, the mineral pigment is chosen from mineral pigments which are stable in the paste.

The term “stable pigment” is generally understood to mean that the pigment does not exhibit a stable change in color over time, when the paste is stored for a minimum of 6 months.

There is no limitation as to the color of this pigment, which is usually the color it will impart to the paste. This pigment can be black, red, blue, green, yellow, orange, purple, brown, etc., and even white.

Generally, the paste therefore has a color identical to the color of the pigment it contains. It is however possible that the paste has a color which differs from the color of the pigment it contains, but this is not sought.

The pigment, especially when it is white, is generally different from the inorganic viscosity agent. Advantageously, the mineral pigment is chosen so that it gives the paste after drying a color different from the color of the surface on which the paste is deposited.

Advantageously, the mineral pigment is a micronized pigment, and the average particle size of the mineral pigment can be from 0.05 to 5 μm, preferably from 0.1 to 1 μm.

Advantageously, the mineral pigment is chosen from oxides of metal (metals) and / or metalloid (s), hydroxides of metal (metals) and / or metalloid (s), oxyhydroxides of metal (metals) and / or of metalloid (s), ferrocyanides and ferricyanides of metal (metals), metal aluminates (metals), and mixtures thereof.

Preferably, the mineral pigment is chosen from iron oxides, preferably micronized, and their mixtures.

The iron oxides can have different colors, they can be for example yellow, red, purple, orange, brown, or black.

In fact, iron oxide pigments are known to have good hiding power and great resistance to acids and bases.

For incorporation into a decontamination paste, iron oxides have the best performance in terms of stability and coloring power. Thus, an iron oxide content of 0.1%, or even 0.01% by mass is sufficient to strongly color the dough without modifying its properties.

Micronized iron oxides are available from the company Rockwood ^® under the Ferroxide ^® trade name.

There may be mentioned inter alia the Ferroxide ^® 212M which is a micronised red iron oxide with an average particle size of 0.1 pm and Ferroxide ^® M 228 which is a micronised red iron oxide with an average particle size of 0.5 pm.

In addition and / or instead of iron oxides, other oxides or hydroxides of colored metals or metalloids can be incorporated into the paste according to the invention, depending on the pH of the paste, mention may in particular be made of the vanadium oxide (V2O5) which is orange, manganese oxide (Mn02) which is black, cobalt oxide which is blue or green, and rare earth oxides. However, iron oxides are preferred for the reasons stated above. Among the oxyhydroxides, there may be mentioned goethite, that is to say iron oxyhydroxide FeOOH, which is very colored.

By way of example of metal ferrocyanide, mention may be made of Prussian blue, that is to say ferric ferrocyanide, and by way of example of aluminate, mention may be made of cobalt blue, it that is, cobalt aluminate.

The solvent for the paste according to the invention is generally chosen from water, organic solvents, and their mixtures.

A preferred solvent is water, and in this case, the solvent therefore consists of water, comprises 100% water.

The paste according to the invention can in certain cases be defined as a paste called “reabsorbing” paste, in which case the paste is then specifically formulated to be supersaturated in solution, in solvent. Such a “reabsorbing”, “supersaturated” paste makes it possible in particular to decontaminate porous materials that are deeply contaminated. When such a paste is deposited on a porous surface, part of the solvent of the paste then spontaneously soaks the pores of the material and solubilizes the contaminating species (contaminants).

It should be noted that no theoretical relationship is defined here with the supersaturation of a dough. The supersaturation of a paste corresponds to its capacity to lose part of its solvent (such as water) water while remaining saturated. That is to say that the paste will contract in order to replace this “lost” part of solvent (for example of water) which represents the supersaturation in solvent, for example in water.

The supersaturation therefore essentially depends on the composition of the dough, namely the type of materials included in the dough and their concentrations.

The solution can be formulated so as to specifically react with the porous material to promote the solubilization of contaminating species, contaminants, for example by chemical attack, chelation of the contaminant etc.

The paste is first brought into contact with the surface of the porous solid substrate to be decontaminated. Once the equilibrium has been reached between saturation of the paste in solution and imbibition of the porous material, the paste begins to dry, because the solvent evaporates at the paste-air interface. The solution soaked in the material is then reabsorbed within the paste under the effect of capillary rebalancing, causing at the same time the contaminants solubilized by advection and thereby allowing the decontamination of the porous material.

The invention further relates to a method for decontaminating a substrate made of a solid material, said substrate being contaminated by at least one contaminating species called labile contaminating species and / or by at least one contaminating species known as surface contaminating species. on one of its surfaces, and / or by at least one contaminating species known as the subsurface contaminating species located just below said surface, and / or by at least one contaminating species located under said surface in the depth of the substrate, in which one carries out at least one cycle comprising the following successive steps:

a) applying the paste according to the invention as described above on said surface;

b) the dough is kept on the surface at least for a sufficient time for the dough to destroy and / or inactivate and / or absorb and / or dissolve the contaminating species, and for the dough to dry and forms a dry and solid residue containing said contaminating species;

c) the dry and solid residue containing said contaminating species is removed.

The decontamination process implements the paste according to the invention as described above and it therefore has all the advantageous effects inherent in this paste which have been described above in particular with regard to the thickness applied and the size of the residue. dry and solid obtained.

In particular, as already mentioned above, in the context of the description of the dough, the presence in the dough according to the invention, of a compound in the form of fibers, even in the small quantities mentioned more high, ensures better internal resistance of the dough without modifying the advantageous properties of decontamination and drying. Thus, the compound in the form of fibers ensures that an even greater thickness of dough, for example greater than or equal to 5 mm, preferably greater than or equal to equal to 6, 7, 8 or 9 mm, more preferably at least 10 mm -and up to for example up to 50 mm- hold on a vertical wall without sagging, and after drying a solid non-pulverulent waste is always obtained. This is demonstrated in Example 4.

The pulp decontamination mechanism involved in the process according to the invention differs according to the type of decontamination.

In the case of labile, surface or sub-surface contamination, the paste is deposited on the contaminated surface and the viscosifying agent allows prolonged contact between the decontaminating solution (solvent for the paste) and the contaminated substrate.

Depending on the decontamination active agent possibly added in the formulation, the paste can dissolve the labile and surface contamination but also corrode the substrate over several μm to dissolve the sub-surface contamination.

The paste finally dries to produce a dry and solid residue at least centimeter containing the contaminating species.

This mechanism is similar to that known with vacuum decontamination gels. However, the paste according to the invention, used in the process according to the invention, contains a specific inorganic viscosity agent chosen from clays and a compound in the form of fibers, and can be applied with a thickness much greater than that with which the gels are applied. The truly synergistic combination of these characteristics, namely inorganic viscosity agent chosen from clays, composed in the form of fibers, and high applied thickness, makes it possible, surprisingly, to obtain a dry and solid residue comprising, on the contrary aspirable gels, little or no fractures, and therefore made up of one or more pieces (s) of a much larger size than the glitter of aspirable gel.

In general, in the method according to the invention, it is sought to avoid fractures, unlike methods which use aspirable gels in which it is sought to produce fractures. The method according to the invention makes it possible to fix, immobilize the contaminating species securely within the dry paste, of the dry and solid residue, which makes it possible to avoid any release in the event of leaching of the dry and solid residue.

The process according to the invention is a reliable and reproducible process which can be described as a robust process and the efficiency of the process depends little on the way in which the dough is deposited. Thus, unlike aspirable gels which require fine control over their use by spraying, and thanks to their improved wall holding properties, the pastes according to the invention can be spread manually on contaminated surfaces with a float. for example, or preferably, using a spraying machine in the manner of a mortar or a plaster.

The substrate made of a solid material can be a porous substrate, preferably a porous mineral substrate.

However, the efficiency of the paste and of the process according to the invention is just as good in the presence of a dense, non-porous and / or non-mineral surface.

Advantageously, the substrate is made of at least one solid material chosen from metals and metal alloys such as stainless steel, painted steels, aluminum, and lead; polymers such as plastics or rubbers such as poly (vinyl chloride or PVC, polypropylenes or PP, polyethylenes or PE, in particular high density polyethylenes or HDPE, poly (methyl methacrylate or PMMA, poly ( vinylidene fluoride or PVDF, polycarbonates or PC; glasses; cements and cement materials; mortars and concretes; plasters; bricks; natural or artificial stone; ceramics.

Advantageously, the contaminating species is chosen from the chemical, biological, nuclear or radioactive contaminating species already listed above and in particular from the toxic biological species already listed above.

Advantageously, the paste is applied to the surface to be decontaminated at the rate of 2000 g to 50,000 g of paste per m ² of surface, preferably from 5,000 g to 10,000 g of paste per m ² of surface, which corresponds approximately to a thickness of dough from 2 to 50 mm per m ² of surface, preferably from 5 to 10 mm of dough per m ² of surface. Advantageously, as we have already seen above, the paste can be applied to the surface manually, with a float for example, or using a spraying machine.

Advantageously (during step b)), the drying is carried out at a temperature of 1 ° C to 50 ° C, preferably from 15 ° C to 25 ° C, and under a relative humidity of 20% to 80%, preferably from 20% to 70%.

Advantageously, the dough is kept on the surface for a period of 2 to 72 hours, preferably from 2 to 48 hours.

Advantageously, the dry and solid residue is in the form of one or more pieces (x), each of said pieces having a size (defined by their largest dimension) greater than or equal to 1 cm, preferably greater than or equal to 2 cm, preferably still greater than or equal to 5 cm.

Advantageously, the dry and solid residue is removed from the solid surface by a mechanical process such as brushing.

Advantageously, the cycle described above can be repeated for example from 1 to 10 times using the same paste during all the cycles or by using different pastes during one or more cycle (s).

Advantageously, during step b), the dough, before total drying, is rewetted with a solution, for example with a solution of a decontamination agent, preferably with a solution of the active decontamination agent for the dough. applied during step a) in the solvent of this paste, which then generally avoids repeating the application of the paste on the surface and causes a saving in reagent and a limited amount of waste. This rewetting operation can be repeated for example from 1 to 10 times.

Advantageously, the paste applied during step a) may be a paste supersaturated with solvent (see above), in particular in the case where the substrate is made of a porous solid material.

The process according to the invention can be qualified as a “regenerative” process because it uses a paste giving a waste, residue, dry and solid which, advantageously, can be regenerated to form a new paste according to the invention, which, if if necessary, can be used again in the process according to the invention. The waste, residue, dry and solid, in order to be regenerated, can be brought into contact with a solution, comprising a solvent, and optionally one or more optional components mentioned above to thereby obtain a paste according to the invention as described above, for example, the waste, residue, dry and solid can be brought into contact with a solution of a decontamination agent.

The process for decontaminating a substrate made of a solid material according to the invention, in particular in the case where this substrate is made of a porous solid material does not require prior imbibition of the substrate, in particular thanks to effective control of the supersaturation ( see above) of the dough according to the invention.

In summary, the process and the paste according to the invention exhibit, among other things, in addition to the advantageous properties already mentioned above, the following other advantageous properties:

easy application of the paste,

adhesion to walls and ceilings,

obtaining the maximum decontamination efficiency at the end of the drying phase of the paste, including in a situation of penetrating contamination in particular in the case of porous surfaces.

In general, we make sure that the drying time is greater than or equal to the time necessary for inactivation. In the case of a deep inactivation, a rewetting can be used.

processing a very wide range of materials,

the absence of mechanical or physical alteration of the materials at the end of the treatment,

the implementation of the process under variable climatic conditions, the reduction of the volume of waste,

ease of recovery of dry waste.

In conclusion, the applications of the paste and of the surface, sub-surface and in-depth decontamination process, in particular of porous materials according to the invention are diverse and varied. A particularly targeted application concerns the nuclear decontamination of cementitious materials in order to minimize the waste generated by the clean-up and dismantling of nuclear installations at the end of their life.

The problem of decontamination of porous materials also comes into play in other areas of activity such as industries using toxic chemical compounds, post-accident NRBC decontamination (Nuclear, Radiological, Biological and Chemical), architectural conservation of monuments historical, even in the context of dismantling of domestic sites polluted, for example by toxic molecules, heavy metals, micro-organisms, asbestos, soot particles following a fire etc.

Other characteristics and advantages of the invention will appear better on reading the detailed description which follows, this description being given by way of nonlimiting illustration, in conjunction with the accompanying drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

Figure 1 is a photograph of Dough-1 prepared in Example 1, in a container.

Figure 2 is a photograph of Dough-2 prepared in Example 1, in a container.

Figures 3A, 3B, and 3C show photographs showing a layer, deposit, of Dough-3 (Figure 3A), a layer, deposit, of Dough-1 (Figure 3B), and a layer, deposit, of Dough-4 (Figure 3C) deposited on a surface of a vertical mortar wall. The thickness of the layers of pasta deposited is 10 mm.

DETAILED PRESENTATION OF PARTICULAR EMBODIMENTS

The dough according to the invention can be easily prepared at room temperature. For example, the dough according to the invention can be prepared by preferably adding gradually, (successively in any order, and / or simultaneously) the or inorganic viscosifying agent (s), and the compound in the form of fibers in solvent such as water, preferably deionized water, or in a mixture of the solvent and one or more several components chosen from the components already listed above, namely: a surfactant, an active decontamination agent, an agent extracting contaminant species, a chelating agent contaminant species, and a coloring agent.

This mixing can be carried out by mechanical stirring, for example by means of a mechanical stirrer equipped with a three-blade propeller. The rotation speed is for example 200 revolutions / minute, and the duration of the stirring is for example from 3 to 5 minutes.

The addition of the inorganic viscous agent (s) and the compound in the form of fibers to the solvent or to the mixture of the solvent and of the component (s) mentioned above can be carried out. by simply pouring the viscosifying agent (s) and the compound in the form of fibers into the said mixture, successively in any order or simultaneously. When adding the inorganic viscosity agent (s) and / or the compound in the form of fibers, the mixture containing the solvent, this or these inorganic viscosity agent (s) ( s), and / or the compound in the form of fibers and optionally the or component (s) mentioned above is generally kept under mechanical stirring.

This stirring can be, for example, carried out by means of a mechanical stirrer equipped with a three-blade propeller.

The stirring speed is generally gradually increased as the viscosity of the solution increases, finally reaching a stirring speed of for example between 400 and 600 revolutions / minute when all of the agent (s) inorganic viscosant (s) and compound in the form of fibers was added, without any splashes.

After the end of the addition of the inorganic viscosant (s) (mineral (s)) and of the compound in the form of fibers, stirring is still maintained, for example for 2 to 5 minutes, so to obtain a perfectly homogeneous paste.

The dough thus prepared is then left to stand for at least one hour before using it

It is obvious that other dough preparation protocols according to the invention can be implemented with an addition of the dough components in an order different from that mentioned above and / or with the simultaneous addition of several components

It should be noted that the optional surface-active agent of the paste according to the invention favorably and notably influences the rheological properties of the paste according to the invention. This surfactant in particular avoids the risks of spreading or sagging during the treatment of vertical surfaces and ceilings.

The paste according to the invention thus prepared is then applied to the solid surface to be decontaminated from a substrate made of a solid material, in other words to the surface having been exposed to contamination, for example to biological contamination. This contamination has already been described above. In particular, biological contamination can consist of one or more of the biological species already defined above.

As already indicated above, the active decontamination agent, for example the active biological decontamination agent, is chosen according to the contaminating species, for example the biological species to be eliminated, destroyed, or inactivate.

Apart from possibly light metal alloys of aluminum type, in the case where basic or acidic pastes are used, there is no limitation as to the material which constitutes the substrate to be decontaminated, in fact the paste according to the invention allows to treat without any damage, all kinds of materials even fragile.

The paste according to the invention generally does not generate any alteration, erosion, attack, chemical, mechanical or physical of the treated substrate.

However, in the case of a sub-surface decontamination operation, there is controlled corrosion of the substrate over a few μm, as for the aspirable gels.

The paste according to the invention is therefore in no way detrimental to the integrity of the treated substrates and even allows their reuse. Thus, sensitive materials such as military equipment are preserved and can be reused after their decontamination, while the monuments treated with the paste according to the invention are absolutely not degraded and have their visual and structural integrity preserved.

This substrate material can therefore be chosen from, for example, metals and alloys such as stainless steel, aluminum, and lead; polymers such as plastics or rubbers among which mention may be made of PVC, PP, PE in particular HDPE, PMMA, PVDF, PC; the glasses ; cements and cementitious materials; mortars and concretes; plasters; the bricks ; natural or artificial stone; ceramics.

In all cases, whatever the material, the effectiveness of decontamination by the paste according to the invention is effective.

The treated surface can be painted or unpainted.

The effectiveness of the treatment with the paste according to the invention is generally effective, including on contaminated substrates over several millimeters in depth.

There is also no limitation as to the shape, the geometry and the size of the substrate and of the surface to be decontaminated, the paste according to the invention and the process implementing it allow the treatment of large surfaces, of geometries complex, for example with hollows, angles, recesses.

The paste according to the invention ensures the effective treatment not only of substrates with horizontal surfaces such as floors, but also of substrates with vertical surfaces such as walls, or inclined or overhanging surfaces such as ceilings.

Compared to decontamination processes, for example biological decontamination processes which use liquids such as solutions, the decontamination process according to the invention which uses a paste is particularly advantageous for the treatment of large surface materials , not transportable and installed outside. Indeed, the method according to the invention due to the implementation of a paste, allows in situ decontamination avoiding the spreading of chemical solutions in the environment and the dispersion of contaminating species.

The paste according to the invention can be applied, spread over the surface to be treated by all the application methods known to those skilled in the art.

Conventional methods are manual application, for example with a float, or application using a spraying machine in the manner of a mortar or a plaster.

The sufficiently short viscosity recovery time of the pastes according to the invention allows the applied pastes to adhere to all surfaces, for example to walls.

The quantity of paste deposited on the surface to be treated is generally from 2000 to 50,000 g / m ² , preferably from 5,000 to 10,000 g / m ² . The quantity of dough deposited per unit of surface and, consequently, the thickness of paste deposited influences the speed of drying.

Thus, when a layer of paste of a thickness of 2 mm to 10 mm is deposited or projected onto the surface of the substrate to be treated, the effective contact time between the paste and the materials is then equivalent to its drying time. , period during which the active ingredient contained in the paste will interact with the contamination.

In addition, it has been surprisingly shown that the quantity of paste deposited - this paste containing, in addition, a specific viscosifying agent chosen from clays - when it is within the ranges mentioned above and in particular when it is greater or equal to 2000 g / m ² and in particular in the range from 5000 to 10000 g / m ² , which corresponds to a minimum thickness of paste deposited, for example greater than or equal to 2000 pm (2 mm) for a quantity of paste deposited greater than or equal to 2000 g / m ² , allowed after drying of the dough to obtain a dry and solid residue in the form of one or more large piece (s) (the size being defined by the largest dimension or pieces), each of the pieces having a size greater than or equal to 1 cm, preferably greater than or equal to 2 cm, more preferably still greater than or equal to 5 cm.

The quantity of paste deposited, and therefore the thickness of paste deposited, preferably greater than or equal to 2000 g / m ^2, ie 2000 μm, is, with the specific nature of the viscosifying agent used in the paste according to the invention (see above), the fundamental parameter which influences the size of the dry residues formed after drying of the dough and which thus ensures a dry and solid residue in the form of one or more large pieces, each of the pieces having a size greater than or equal to 1 cm, and not dry residues of millimeter size or pulverulent residues are formed. The dry and solid residue in the form of one or more large pieces obtained is easily removed by a mechanical process.

However, it should also be noted that if the paste contains a surfactant at low concentration, generally from 0.1% to 2% of the total mass of the paste, then the drying of the paste is improved and leads to a increased ability of dry residue to detach from the support. The paste is then kept on the surface to be treated for the entire time necessary for its drying. During this drying step which can be considered to constitute the active phase of the process according to the invention, the solvent contained in the paste, namely generally the water contained in the paste evaporates until obtaining a dry and solid residue.

The drying time depends on the composition of the dough in the concentration ranges of its constituents given above, but also, as has already been specified, on the quantity of dough deposited per unit of area, that is to say say the thickness of the dough deposited.

The drying time also depends on climatic conditions, namely the temperature and the relative humidity of the atmosphere in which the surface of the substrate made of a solid material is found.

The process according to the invention can be implemented under extremely wide climatic conditions, namely at a temperature T of 1 ° C to 50 ° C and at a relative humidity RH of 20% to 80%.

The drying time of the dough according to the invention is therefore generally from 1 hour to 48 hours at a temperature T of 1 ° C to 50 ° C and at a relative humidity RH of 20% to 80%.

It should be noted that the formulation of the paste according to the invention in particular when it contains surfactants such as "Pluronics ^® " generally provides a drying time which is substantially equivalent to the contact time (between the decontamination, such as a biocidal agent, and contaminating species, for example biological species, in particular biotoxic to be eliminated) which is necessary, required to inactivate and / or absorb the contaminating species polluting the material of the substrate, and / or to achieve sufficient the surface erosion reactions of the material.

In other words, the formulation of the paste ensures a drying time which is none other than the inactivation time of the contaminating species, for example biological species, which is compatible with the kinetics of inhibition of the contamination, for example biological contamination. Or else the formulation of the paste ensures a drying time which is none other than the time necessary for the erosion reactions to remove a contaminated surface layer from the material.

In the case of radioactive contaminating species, the contamination is eliminated by dissolution of the irradiating deposits or by corrosion of the materials supporting the contamination. There is therefore a real transfer of nuclear contamination to the dry and solid residue.

The specific surface area of the generally used mineral filler which is generally from 50 m ² / g to 300 m ² / g, preferably from 100 m ² / g and the absorption capacity of the paste according to the invention make it possible to trap the labile (surface) and fixed contamination of the material constituting the surface to be treated.

If necessary, the contaminating species, for example the contaminating biological species are inactivated in the pasty phase. After the pulp has dried, the contamination, for example the inactivated biological contamination, is eliminated during the recovery of the dry pulp residue described below.

At the end of the drying of the dough, the dry dough forms a dry residue which fractures little or not unlike the dry residue of the aspirable gels. This dry residue comprises one or more large pieces. The dry residue may contain the inactivated contaminant species.

The dry residue obtained after drying the paste has poor adhesion to the surface of the decontaminated material. Therefore, the dry residue obtained after drying the dough can be easily recovered by simple mechanical processes such as brushing. However, dry residues can also be removed by gas jet, for example by compressed air jet.

Thus, no rinsing with a liquid is generally necessary, and the method according to the invention does not generate any secondary liquid effluent.

It is however possible, although this is not preferred, and if desired, to remove the dry residues by means of a jet of liquid.

The process according to the invention therefore therefore firstly achieves a significant saving in chemical reagents compared to a process of decontamination by washing with a solution. Then the fact that a waste in the form of a dry residue easily recoverable mechanically is obtained, a rinsing operation with water or with a liquid, generally necessary for the removal of traces of chemical agents from the part , is generally avoided. This obviously results in a reduction in the quantity of effluents produced but also a significant simplification in terms of waste treatment and outlet channel.

Due to the mainly mineral composition of the pulp according to the invention and the small amount of waste produced, the dry waste can be stored or directed to an evacuation system ("outlet") without prior treatment.

At the end of the process according to the invention, a solid waste is recovered in the form of one or more piece (s) of large dry paste, which can be packaged as it is, directly packaged, it results as a significant reduction in the quantity of effluents produced has already indicated above, as well as a significant simplification in terms of waste treatment and outlet channels.

In addition, in the nuclear field, the fact of not having to reprocess the solid dry residue before conditioning the waste constitutes a considerable advantage; this authorizes the use of effective active agents hitherto prohibited in decontamination liquids due to the operating constraints of liquid effluent treatment stations ("STEL").

The paste may therefore contain powerful oxidizing agents such as cerium IV which can very easily be regenerated from the electrolysis of cerium III.

For example, in the common case where 2000 grams of paste are applied per m ² of treated surface, the mass of dry waste produced is less than 1400 grams per m ² .

Examples:

Example 1.

In this example, we describe the preparation of two surface decontamination pastes, subsurface and in depth called "Paste-1", and "Paste-2" according to the invention.

Dough-1 is a dough whose composition is as follows: 0.8% by weight (based on the total weight of the paste) of cellulose BC 1000 (fiber size of about 700 pm) marketed by Arbocel ^®;

49.6% by mass (relative to the total mass of the pulp) of kaolinite marketed by Sigma-Aldrich ^® ; and

49.6% by mass (relative to the total mass of the dough) of deionized water.

Dough-2 is a dough whose composition is as follows:

8% by weight (based on the total weight of the paste) of cellulose BC 1000 (fiber size of about 700 pm) marketed by Arbocel ^®;

20% by mass (relative to the total mass of the pulp) of kaolinite marketed by Sigma-Aldrich ^® ; and

72% by mass (relative to the total mass of the dough) of deionized water.

The synthesis protocol is similar for the two pastes:

Deionized water is first weighed in a suitable container.

The kaolinite and the cellulose are then gradually added to the water with stirring using a mechanical stirrer with three blades, until a homogeneous mixture presenting no lumps is obtained.

The pastes thus formed are finally kept stirring for a few minutes.

Figure 1 is a photograph of the prepared Dough-1.

Figure 2 is a photograph of the prepared Dough-2.

Each of the two pastes has a malleable structure which can be deposited on a surface, such as a wall of an installation for example, manually or using a projection machine, in the manner of a mortar or a coating.

Example 2.

In this example, the effectiveness of a paste according to the invention is demonstrated, namely the paste-1 prepared in example 1 for decontaminating a porous material at the surface, subsurface and in depth. More precisely, in this example, we study decontamination using a decontaminating paste according to the invention, of a porous material constituted by a stack of glass beads, which is contaminated in depth by ¹³³ Cs.

The decontaminating paste according to the invention used in this example is Paste-1 prepared in Example 1.

The porous material used is a stack of glass beads, of sizes between 45 μm and 90 μm, which is prepared in a round crystallizer with a diameter of 9.1 cm.

The stack of glass beads produced, which has a height of 2 cm, is soaked and saturated with 43.42 mL of an aqueous solution of CsNÜ3 with a CSNO3 concentration of 0.016 M. 93 mg of ¹³³ They are present in the stack of glass beads.

A 2 cm layer of Paste-1 is then placed on the stack of glass beads saturated with the solution. The whole is then left to dry under ambient conditions. After one week of drying, the residual solid waste resulting from the drying of Pulp-1 is separated from the stack of glass beads. The glass beads are then collected and washed using a 0.1 M NaOH solution. The washing solution is finally analyzed by atomic absorption spectroscopy in order to determine the amount of Cs remaining in the stack. glass beads, and thus study the effectiveness of the process. Analysis of the washing solution reveals the presence of 63.2 mg of Cs. The decontamination step thus made it possible to recover 68% of the contaminants - that is to say ¹³³ Cs - present in the stack of glass beads.

Paste-1 dried and absorbed the aqueous solution by capillary action. The contaminants - that is to say ¹³³ Cs - were thus absorbed from the porous material towards the Paste-1 by advection.

Thanks to this example, it is clearly demonstrated that the “re-absorbent” pastes according to the invention have the capacity to decontaminate porous materials contaminated both at the surface, subsurface and in depth.

Example 3.

In this example, the fixation of a contaminant in the final solid waste obtained after decontamination with a paste according to the invention is studied. We show here that clay is essential to play both the role of viscosant but also of contamination fixative.

More precisely, in this example, we demonstrate the ability of the doughs according to the invention to fix a contaminant within the dry dough obtained after a decontamination operation.

For this, 1 g of kaolinite marketed by Sigma-Aldrich ^® was soaked with 4 mL of a solution of Cs. Different samples were produced with different concentrations of Cs, namely: 10 ^-1 M, 10 ² M, 10 ³ M, and 10 ⁵ M. The samples are left to dry until evaporation and then they are suspended in 100 ml with stirring for 24 h. After these 24 hours, the solution is filtered, and the Cs content is analyzed by atomic absorption spectroscopy, then compared to the amount of Cs introduced into the gram of kaolinite. The content of Cs retained by the clays is finally calculated and expressed in%. The results are collated in Table 1 below.

Table 1: Retention of Cs by clay (kaolinite)

The percentage of Cs retained by the clay depends on the initial amount of Cs added, which can be explained by the saturation of the binding sites.

The test carried out with a Cs concentration of 10 ⁵ M can be considered as the most representative of nuclear contamination because of the small amount of contaminant present. It is then observed in this case that almost all of the contaminants (that is to say of Cs) can be fixed by the clay. To conclude, in the case of a paste used for a Cs decontamination operation, clay proves essential to play both the role of viscosant and fixative of contamination.

Example 4.

In this example, it is demonstrated that the pastes according to the invention can hold on a vertical wall even if they are applied with a significant thickness and this thanks to the presence of a compound in the form of fibers.

Two new pastes are then prepared (according to the same protocol as that described in Example 1):

a “Pulp-3”, not in accordance with the invention, the composition of which is as follows: 50% by mass of kaolinite sold by Sigma-Aldrich, and 50% by mass of deionized water.

a "paste-4" according to the invention, whose composition is: 2.4% by mass of cellulose Arbocel BC 1000 ^® sold by; 48.8% by mass of kaolinite sold by Sigma-Aldrich; and 48.8% by mass of deionized water.

Figures 3A, 3B, and 3C show a layer, deposition, of Paste-3 (Figure 3A), a layer, deposition, of Paste-1 (described in Example 1) (Figure 3B) and a layer, deposit, of Dough-4 (Figure 3C) deposited on a surface of a vertical mortar wall. The thickness of the layers of pasta deposited is 10 mm.

It is observed in Figures 3A, 3B, and 3C, that in the absence of cellulose fibers, the pulp (here Pulp-3, not in accordance with the invention) does not hold on a vertical surface with a significant thickness. The addition of cellulose fibers in small quantities (Pulp-1 and Pulp-4 according to the invention) allows the pulp to hold on a vertical wall, even when a significant thickness of pulp, in particular at least 10 mm , is filed.

In addition, at the end of drying of Pastes 1 and 4, according to the invention, a non-pulverulent solid waste of size similar to that which has been deposited is obtained and no fracture is observed in this solid waste. In other words, the solid non-pulverulent waste has the same centimeter size as the deposition of wet pulp, which demonstrates that the presence of fibers does not negatively influence the size of the final waste.

REFERENCES

[1] US-A1-2012 / 0121459

[2] WO-A2-2007 / 039598

[3] WO-A2-2004 / 008463

[4] EP-A2-0642846

[5] WO-A1-2010 / 037809

[6] US-B2-7,737,320

[7] FR-A1-2 967 422

Claims

1. Decontamination paste comprising, preferably consisting of:

at least one compound in the form of fibers;

at least one surfactant;

at least one active decontamination agent;

at least one agent extracting contaminating species;

at least one agent chelating contaminating species;

at least one coloring agent;

and the rest of the solvent.

2. Decontamination paste according to claim 1, in which the said component (s) is (are) present in the following proportions:

0.1 to 8 or 10% by mass, preferably 0.1 to 5% by mass, more preferably 0.5 to 5% by mass, better 1 to 5% by mass, better still 1 to 3% by mass relative to the mass of the dough, of the at least one compound in the form of fibers;

optionally, 0.1% to 2% by mass, relative to the mass of the paste, of at least one surfactant;

optionally, 0.1 to 10 mol / L of dough, preferably 0.5 to 10 mol / L of dough, more preferably 1 to 10 mol / L of dough, and better still 3 to 6 mol / L of dough, at least one active decontamination agent; optionally, 0.1% to 5% by mass, relative to the mass of the paste, of the at least one agent extracting contaminating species;

and the rest of the solvent.

3. Decontamination paste according to any one of the preceding claims, in which the fibers are chosen from fibers of organic compounds such as cellulose fibers, and fibers of mineral compounds such as rock wool and glass wool.

4. A paste according to any one of the preceding claims, in which the active decontamination agent is chosen from bases such as sodium hydroxide, potassium hydroxide, and mixtures thereof; acids such as nitric acid, phosphoric acid, hydrochloric acid, sulfuric acid, hydrogen oxalates such as sodium hydrogen oxalate, and mixtures thereof; oxidizing agents such as peroxides, permanganates, persulfates, ozone, hypochlorites such as sodium hypochlorite, IV cerium salts, and mixtures thereof; quaternary ammonium salts such as hexadecylpyridinium (cetylpyridinium) salts, such as hexadecylpyridinium chloride (cetylpyridinium); reducing agents; and their mixtures.

5. A paste according to any one of the preceding claims, in which the surfactant is chosen from nonionic surfactants such as block copolymers, block like block copolymers of ethylene oxide and propylene oxide, and ethoxylated fatty acids; and their mixtures.

6. A paste according to any one of the preceding claims, in which the agent extracting contaminating species is chosen from inorganic adsorbents such as zeolites, clays, phosphates such as apatites, titanates such as sodium titanates, and ferrocyanides and ferricyanides.

7. A paste according to any one of the preceding claims, in which the chelating agent of the contaminating species is chosen from n-octylphenyl-N oxide, N-diisobutylcarbamoyl methylphosphine (CMPO), tributyl phosphate (TBP), 1- hydroxyethane-1,1 disphosphonic acid (HEDPA), di-2-ethylhexylphosphoric acid (DHEPA), trioctylphosphine oxide (TOPO), diethylenetriamine pentaacetate (DTPA), primary and secondary organic amines and tertiary, cobalt dicarbollide, calixarenes, niobates, ammonium molybdophosphate (AMP), (trimethylpentyl) phosphinic acid (TPPA), and mixtures thereof.

8. A paste according to any one of the preceding claims, in which the coloring agent is chosen from organic dyes and mineral pigments, preferably micronized, such as metal oxides (metals) and / or metalloid (s) , hydroxides of metal (metals) and / or metalloid (s), oxyhydroxides of metal (metals) and / or metalloid (s), ferrocyanides and ferricyanides of metal (metals), metal aluminates (metals) , and mixtures thereof.

9. A paste according to any one of the preceding claims, in which the solvent is chosen from water, organic solvents and their mixtures.

10. A paste according to any one of the preceding claims which is supersaturated with solvent.

11. A method for decontaminating a substrate made of a solid material, said substrate being contaminated with at least one contaminating species called a labile contaminating species and / or with at least one contaminating species called a surface contaminating species found on one of its surfaces, and / or by at least one contaminating species known as a subsurface contaminating species located just below said surface, and / or by at least one contaminating species found under said surface in the depth of the substrate, in which at least one cycle is carried out comprising the following successive steps:

a) applying the paste according to any one of claims 1 to 10 on said surface;

c) the dry and solid residue containing said contaminating species is removed.

12. The method of claim 11, wherein the substrate is a porous substrate, preferably a porous mineral substrate.

13. Method according to any one of claims 11 to 12, in which the solid material is chosen from metals and metal alloys such as stainless steel, painted steels, aluminum and lead; polymers such as plastics or rubbers such as poly (vinyl chloride) or PVC, polypropylenes or PP, polyethylenes or PE, in particular high density polyethylenes or HDPE, poly (methyl methacrylate) s or PMMA , poly (vinylidene fluoride) s or PVDF, polycarbonates or PC; the glasses ; cements and cementitious materials; mortars and concretes; plasters; the bricks ; natural or artificial stone; ceramics.

14. Method according to any one of claims 11 to 13, in which the contaminating species is chosen from chemical, biological, nuclear or radioactive contaminating species.

15. The method of claim 14, wherein the contaminating species is a biological species chosen, for example, from bacteria, fungi, yeasts, viruses, toxins, spores, prions, and protozoa.

16. Method according to any one of claims 11 to 15, in which the paste is applied to the surface at the rate of 2000 g to 50,000 g of paste per m ² of surface, preferably from 5,000 g to 10,000 g of paste per m ² of surface, which corresponds approximately to a thickness of dough from 2 to 50 mm per m ² of surface, preferably from 5 to 10 mm of dough per m ² of surface.

17. Method according to any one of claims 11 to 16, in which during step b), the drying is carried out at a temperature of 1 ° C to 50 ° C, preferably from 15 ° C to 25 ° C , and at a relative humidity of 20% to 80%, preferably from 20% to 70%.

18. Method according to any one of claims 11 to 17, in which the paste is maintained on the surface for a period of 2 to 72 hours, preferably from 2 to 48 hours.

19. Method according to any one of claims 11 to 18, in which the dry and solid residue is in the form of one or more piece (s), each of said pieces having a size greater than or equal to 1 cm, preferably greater than or equal to 2 cm, more preferably greater than or equal to 5 cm.

20. Method according to any one of claims 11 to 19, in which the dry and solid residue is removed from the solid surface by a mechanical process such as brushing.

21. Method according to any one of claims 11 to 20, in which the cycle described is repeated from 1 to 10 times using the same paste during all the cycles or using different pasta during one or more cycle (s).

22. Method according to any one of claims 11 to 21, in which the paste applied during step a) is a paste supersaturated with solvent.