Process for treating asbestos waste using a horizontal rotary crusher

Abstract

The present invention relates to a method for treating a solid material containing asbestos, comprising contacting the solid material with an aqueous acid solution in a rotary horizontal mill, to decompose the mineral filler included in the asbestos-containing solid material, followed by a heating step to decompose the asbestos. The invention also relates to the use of a rotary horizontal mill for decomposing, using an acid solution, a solid material containing: (a) asbestos and (b) a mineral binder.

Description

Title of the invention: Method for treating asbestos waste using a horizontal rotary crusher SUBJECT OF THE INVENTION

[0001] The present invention relates to a method for treating a solid material containing asbestos, comprising bringing the solid material into contact with an aqueous acid solution in a rotary horizontal mill, to decompose the mineral filler included in the asbestos-containing solid material, followed by a heating step in order to decompose the asbestos. The invention also relates to the use of a rotary horizontal mill for decomposing, using an acid solution, a solid material containing: (a) asbestos and (b) a mineral binder. BACKGROUND OF THE INVENTION

[0002] Asbestos is a material formed from silicate fibers, essentially chrysotile, a magnesium silicate with the formula Mg3[Si2O5(OH)4], which was widely used in the 1970s both as reinforcement in composites and as insulation in the construction industry. Its involvement in respiratory tract cancers led to its ban in a number of countries and the implementation of specific measures on building renovation sites to protect personnel and ensure the treatment of asbestos waste. Currently, almost all waste from asbestos removal operations is buried.

[0003] Research has therefore been carried out in order to have a process for treating asbestos waste (or MPCA, for Materials and Products Containing Asbestos) which is more respectful of the environment, by allowing their treatment and resulting in non-hazardous residues which can potentially be recovered.

[0004] In this context, it has already been proposed to treat asbestos waste, in particular based on fiber cement, using hydrochloric acid in order to decompose it and to isolate in particular metal cation salts and silica (EP 2 285 455). To do this, the asbestos waste is crushed before being treated using hydrochloric acid at room temperature in order to separate the asbestos and any silicic solids present (from the clay constituting the hydraulic binder) from the non-asbestos and non-silicic constituents, then the asbestos solid obtained is separated by filtration before being resuspended, in a mixer-type reactor, in an aqueous solution of hydrochloric acid brought to reflux (at 70-110°C, typically 95°C) for several hours.

[0005] Patent application EP 4 124 397 describes an improvement of this method, making it possible to treat very different types of MPCA, in which the step of heating of the asbestos solid in the presence of hydrochloric acid is carried out according to a temperature ramp comprising a first stage at 50-60°C and a second stage at 70-100°C.

[0006] In the above processes, the preliminary grinding of the asbestos waste is carried out dry, in a hammer mill, or alternatively in a wet mill in order to limit the formation of dust, until aggregates of 1 to 10 mm are obtained which are then subjected to the first stage of cold acid attack then to the hot acid attack(s).

[0007] However, it became apparent to the inventors that these grinding methods were not satisfactory. Indeed, during the treatment of asbestos floor tiles, hammer mill clogging phenomena were observed when the grinding time was insufficient. The rate of insertion into the crusher must therefore be slowed down. Furthermore, although the improved process described above makes it possible to limit the formation of foam, the latter nevertheless constitutes a problem in the case of certain waste rich in carbonates, such as floor tiles (which comprise, for example, a combination of carbonated mineral filler, PVC and asbestos) or fiber cement-based waste. It has indeed appeared that bringing such an asbestos solid, having a high specific surface area after grinding, into contact with hydrochloric acid in a quantity necessary and sufficient for the reaction, promoted the formation of foam.To counter this phenomenon, an anti-foaming agent is added to the reactor before the asbestos solid material is introduced, and this is introduced gradually so that the foam can be suppressed before the asbestos solid can be added to the reaction medium. Otherwise, the foam forms a barrier between the acid solution and the solid material, making it difficult to suspend. In extreme cases, the foam can damage the reactor and its instrumentation. In all cases, during this contacting step, it is necessary to provide a large quantity of water and strong agitation in the reactor in order to suspend the ground asbestos solid. These disadvantages affect the efficiency and economy of the process.

[0008] It would therefore be useful to have a process which overcomes the aforementioned drawbacks and thus makes it possible to further improve its environmental impact and its energy balance, with a view to its exploitation on an industrial scale. Summary of the invention

[0009] The invention thus relates to a method for treating a solid material containing asbestos, characterized in that it comprises the following successive steps:

[0010] (a) fragmentation of the solid matter to form fragments of which the most large dimension is between 1 and 20 cm,

[0011] (b) contacting the fragmented solid matter with an aqueous solution of acid, at a temperature between 5°C and less than 50°C, in a horizontal rotary mill, so as to obtain a suspension,

[0012] (c) optionally, separating the suspension from step (b) into a filtrate and a treated solid material, followed by suspending the treated solid material in an acid bath,

[0013] (dl) optionally, heating the suspension from step (b) or (c), to a temperature between 50°C and 70°C,

[0014] (d2) heating the suspension from step (c) or (dl) to a temperature between 80 and 110°C, preferably between 90 and 95°C, and

[0015] (e) cooling the suspension obtained in step (d2).

[0016] The above method has many advantages over the methods of the prior art: - the reaction kinetics of cold acid treatment are more stable and constant, - the generation of foam due to the contact of the asbestos solid with the acid is moderate and better controlled, because: (a) the solid / liquid interface is continuously renewed due to the simultaneous combination of attrition by the grinder and attack by the acid, and (b) although the reaction is exothermic, the rise in temperature of the reaction medium is gradual and more easily controlled, - the volume of the reaction medium during this acid attack is reduced since it is no longer necessary to dilute it strongly to avoid sedimentation of the MPCA, - waste pieces of the order of a few centimetres can be directly processed, or even entire pieces such as tiles or earthenware tiles, so that fine grinding is no longer necessary, which reduces the investment and operating costs of the process and dust emissions (particularly in comparison with dry grinding processes).

[0017] This method also makes it possible to achieve energy savings of approximately 50% compared to the prior art methods described above.

[0018] The invention also relates to the use of a horizontal rotary crusher for decomposing, using an acid solution, a solid material containing: (a) asbestos and (b) a mineral binder. BRIEF DESCRIPTION OF THE FIGURES

[0019] [Fig. 1] is a diagram illustrating the different stages of an embodiment of the process according to the invention, comprising a heating step including two temperature stages at at least 50°C and at least 80°C, respectively, and a calcium separation step.

[0020] [Fig.2] is a diagram illustrating the different stages of an embodiment of the method according to the invention, comprising a heating step including two temperature stages at at least 50°C and at least 80°C, respectively, without separation of the calcium.

[0021] [Fig.3] is a diagram illustrating the different stages of an embodiment of the process according to the invention, comprising a single step of heating to at least 80°C and a step of separating the calcium.

[0022] [Fig.4] is a diagram illustrating the different stages of an embodiment of the process according to the invention, comprising a single heating step to at least 80°C, without separation of the calcium. DETAILED DESCRIPTION

[0023] The method according to the invention aims to treat in a simple and economical manner, on an industrial scale, a solid material containing asbestos. By "solid material containing asbestos" is meant any solid material consisting of, or originating from, asbestos waste containing asbestos and a mineral binder, as well as possibly at least one organic binder. The mineral binder generally contains at least one compound chosen from: a carbonate, in particular calcium carbonate; a calcium salt, oxide and / or hydroxide, in particular limestone and / or gypsum; oxides and / or hydroxides of iron, aluminum and / or magnesium; silica; alumina; an aluminosilicate; and mixtures thereof, preferably the mineral binder comprises at least one carbonate, optionally in a mixture with one or more of the aforementioned compounds. The organic binder, for its part, comprises an organic resin (in particular PVC), optionally in the form of a composite.Asbestos is preferably chrysotile.

[0024] This asbestos waste can thus be chosen in particular from: asbestos flocking; asbestos adhesives and coatings; floor covering plates or slabs (in particular tiles or earthenware), walls or roofs (in particular fiber cement sheets); asbestos plaster; or pipes, in particular based on fiber cement, in particular ventilation pipes or water supply or drainage pipes; as well as furniture elements based on asbestos-cement plates covered with enamel (Glasal). In these products, asbestos can be combined with cement, plaster, cardboard, paint or resins.

[0025] One of the main advantages of the method according to the invention is its ability to adapt to the treatment of these different types of waste, whatever their composition. chemical position. Generally speaking, asbestos waste treated according to the invention contains 5 to 20% by weight and more generally 5 to 15% by weight of asbestos. In special cases (flocking in particular), they can contain up to 80% by weight of asbestos.

[0026] The different stages of the process for treating this asbestos waste will now be described in more detail.

[0027] In a first step, the asbestos solid material is subjected to a fragmentation step (a). This may typically involve coarse crushing or grinding using a shear or impact crusher or (in the case of a fibrous solid material) a shredder. This step consists of reducing the size of the asbestos solid so that its largest dimension is between 1 and 20 cm, for example between 2 and 15 cm, or even between 2 and 5 cm. It is possible to provide a series of crushers in order to achieve the desired size, although this is not desirable.

[0028] During or after step (a), it is possible to separate the metals present in the fragmented solid matter. To do this, different techniques can be envisaged, which are well known to those skilled in the art. Depending on whether the metals are ferrous or non-ferrous, it is thus possible to envisage the use of overband magnets (deep-field electromagnetic magnets), a magnetic drum or eddy current separation, for example. This step of separating the metals makes it possible to prevent them from damaging certain crushers, but also to avoid generating dihydrogen during subsequent contact of the solid matter with acid and thus creating explosion-risk zones.

[0029] The fragmented solid material is then brought into contact in step (b) with an aqueous acid solution, in a horizontal rotary mill, at a temperature between 5°C and less than 50°C, so as to obtain a suspension. The reaction being more or less exothermic, it is possible that after bringing the solid material into contact with the acid, preferably at a temperature between 20 and 30°C, the temperature of the medium approaches 50°C. Otherwise, it may be useful to heat the medium slightly.

[0030] By "rotary horizontal mill" is meant in this description a device comprising a grinding chamber arranged horizontally relative to the ground and rotated by a motor, for example by means of rollers forming a cradle for the grinding chamber. The chamber further comprises one or more bars or balls (serving as grinding media) and its internal surface may optionally be provided with protuberances serving as deflectors. Generally, this type of mill comprises an opening made in one of its side walls, intended for the introduction of the fragmented solid material and the acid solution. This wall preferably comprises a vent. The opposite side wall is in this case intended for emptying the contents of the mill, i.e. the suspension from step (b). The material constituting the internal walls of the mill is chosen so as to be resistant to abrasion and to the acid used. If necessary, the mill can also be equipped with pH, ​​temperature and / or conductivity sensors. In the method according to the invention, the horizontal mill can be rotated at a relatively low speed compared to mills of the prior art, without any sedimentation of the asbestos-containing solid material occurring, however dense it may be. The duration of contact in the horizontal mill of the acid solution with the fragmented solid material can vary depending, in particular, on the diameter of the mill and is generally between 30 minutes and 6 hours.

[0031] It is preferred that the acid solution used in step (b) consists of hydrochloric acid, although it may alternatively be possible to use sulfuric acid, or even organic acids. In this case, it advantageously contains at least 15% by weight, preferably at least 18% by weight, more preferably 20 to 30% by weight of hydrochloric acid. The amount of acid solution is in all cases adjusted to obtain a suspension containing, for example, 20 to 50% by weight, preferably 30 to 45% by weight, of solid matter.

[0032] It has been observed that the combination of mechanical attrition produced by the horizontal mill with the leaching / embrittlement of the solid matter by the acid allows the solid matter to be completely disintegrated, although it is only coarsely ground before step (b). Furthermore, the release of carbon dioxide in this step is relatively constant and does not require the addition of an anti-foaming agent. Indeed, a balance is naturally established between the production of foam and its reduction during this step of the process, which allows it to be controlled.

[0033] An acid attack is thus carried out on the non-silicic constituents of the binder present in the asbestos waste. This cold treatment stage allows the asbestos waste to be decomposed into an asbestos solid, silica (from the hydraulic binders possibly included in the asbestos waste) and metal chlorides. The carbonates possibly present in the asbestos waste are mainly decomposed at this stage, according to the following reactions:

[0034] [Chem 1]

[0035] CaCO3 + 2HC1 -> CaCl2 + CO2 + H2O

[0036] [Chem 2]

[0037] CaO + 2HC1 -> CaCl2 + H2O

[0038] During step (c), the suspension from step (b) is then optionally separated, usually by filtration, into a filtrate and a treated solid, before the treated solid is resuspended in an acid bath, possibly after washing with water.

[0039] The filtrate from step (c) may optionally be treated so as to isolate the metal cation salts it contains, as described in application EP 2 285 455. To this end, its pH is generally adjusted to a value ranging from 5 to 7, advantageously by means of calcium oxide or hydroxide, so as to neutralize the residual acid and separate the iron and aluminum salts (which precipitate in the form of hydroxides) from the calcium salts (which remain in solution). After filtration of the medium, these metal cation salts can themselves be recovered.

[0040] In a first embodiment, the suspension from step (b) or (c) is subjected to a hot acid treatment in stages, following two steps (d1) and (d2).

[0041] For this purpose, the suspension is first brought to a first temperature Tl of between 50°C and 70°C, preferably between 50 and 55°C, and can be maintained at this temperature for a period of time ranging from 20 minutes to 1 hour. This step makes it possible to significantly advance the decomposition of the carbonated materials into carbon dioxide. Care will be taken in this step not to reach or exceed the boiling temperature of the acid solution. To do this, the acid concentration is measured during step (dl) and an aqueous acid solution is optionally added to the suspension, in such a quantity that the acid concentration generally does not exceed 400 g / l, in the case of hydrochloric acid.

[0042] In this embodiment, the method according to the invention may comprise an additional step of recovering the carbon dioxide generated in step (b) and / or in step (dl).

[0043] The suspension from step (d1) is then subjected to a finishing heating step (d2). To do this, it can either be directly subjected to step (d2), or be first filtered, then the solid obtained can be resuspended in the acid for step (d2). In all cases, step (d2) consists of bringing the suspension to a second temperature T2 of between 80 and 110°C, preferably 90 to 95°C, and maintaining it at this temperature for a period generally ranging from 30 minutes to 1 hour. This finishing step makes it possible to convert (or finish converting) the asbestos into silica and to dissolve the non-silicic compounds of the asbestos in the form of iron and magnesium chlorides, in particular. It can be carried out at a temperature up to the boiling point of the acid solution. To do this, the acid concentration is measured during step (d2) and an aqueous acid solution is optionally added to the suspension.In the case where hydrochloric acid is used, the amount of acid solution added is preferably such that the hydrochloric acid concentration does not exceed 340 g / l, preferably 250 g / l. In practice, in the case where a hydrochloric acid solution having a concentration greater than 20% by mass is used, it is possible to heat the suspension to 70°C until the hydrochloric acid is consumed to the point of representing 20% ​​by mass of the suspension. then proceed to heating to 95°C or 100°C (the vapors in this case being essentially composed of water).

[0044] This embodiment is illustrated in Figures 1 and 2, using hydrochloric acid as a reagent, although the invention is not limited to this embodiment. It has several advantages:

[0045] - the temperature of the heating stage is reached more quickly,

[0046] - the energy required to reach this temperature is less,

[0047] - at 50°C CO2 carries less acid when it is released, so that the The vast majority of the acid remains in the liquid phase for the asbestos decomposition reaction which will then take place.

[0048] A second embodiment of the invention is illustrated in Figures 3 and 4, using hydrochloric acid as a reagent, although the invention is not limited to this embodiment. In this embodiment, step (d2) is carried out directly after step (c), i.e. the suspension from step (c) is heated to a temperature T2 of between 80 and 110°C, preferably between 90 and 95°C, for a period of time ranging, for example, from 30 minutes to 1 hour. Advantageously, a hydrochloric acid solution of 12-25% by weight, preferably 15-20% by weight, is used.

[0049] It will be noted that, in the case where step (c) is not implemented, steps (d1) and / or (d2) can optionally be implemented in the same horizontal mill as that used in step (b) when the materials which constitute it are suitable for withstanding these reaction conditions.

[0050] The acid not consumed in step (d2) can be recycled to step (b) or (d1).

[0051] At the end of step (d2), the suspension obtained is cooled, for example to a temperature temperature between 25 and 80°C, preferably 25 to 60°C, during step (e).

[0052] The cooled suspension can then be filtered, during a step (f), so as to obtain a filtrate containing metal chlorides and a solid fraction containing in particular silica, generally with a high specific surface area (between 150 and 300 m2 / g) and which is therefore recoverable. The solid fraction can also contain plastic materials, such as PVC, in particular when the asbestos waste is a vinyl-asbestos floor tile.

[0053] The filtrate from step (f) may optionally be treated so as to isolate the metal cation salts it contains, as described in application EP 2 285 455. To this end, its pH is generally adjusted to a value ranging from 5 to 7, advantageously by means of magnesium or calcium oxide or hydroxide, preferably magnesium oxide or hydroxide, so as to neutralize the residual acid and separate any iron and aluminum salts present (which precipitate in the form of hydroxides) of magnesium salts and possibly calcium salts (which remain in solution).

[0054] Specifically, in the case where step (c) has been implemented, the silica and the magnesium salts are recovered in step (f), as illustrated in Figures 1 and 3. Failing this, not only the silica, but also the calcium, magnesium, iron and aluminum salts are recovered in step (f), as illustrated in Figures 2 and 4.

[0055] After filtration of the medium, these metal cation salts can themselves be recovered, for example as such or by means of electrolysis for magnesium salts, and in the field of water treatment, for iron salts. EXAMPLES

[0056] The invention will be better understood in light of the following examples, which are given purely for illustrative purposes and are not intended to limit the scope of the invention, defined by the appended claims.

[0057] Example 1: Asbestos treatment process using a horizontal rotating reactor

[0058] This process is illustrated schematically in [Fig.l].

[0059] 500g of asbestos cement was roughly crushed into 3 or 4 cm pieces which were then introduced into a horizontal rotary reactor containing a PVC bar serving as grinding media and 1250 ml of 23% hydrochloric acid. The grinder, arranged in a cradle on rollers connected to an electric motor, was set in rotation by operating this motor. Deflectors arranged inside the grinder allowed the PVC bar to be raised and rolled over the load as the grinder rotated. The foam height observed did not exceed 10% of the reaction medium, so it was not necessary to add an anti-foaming agent.

[0060] After 4 hours, the suspension obtained was transferred to a heated reactor equipped with mechanical stirring, in which the suspension was brought to a temperature close to the boiling point of the solution for one hour. The mixture was then filtered to remove the silica from the rest of the aqueous solution. The silica was then washed and dried, while the filtrate was treated to extract the salts it contained. To do this, 40g of calcium hydroxide (in the form of a 30% aqueous suspension) were introduced into the medium, to bring the pH back to 7 and convert the iron and aluminum chlorides into iron and aluminum hydroxides in the form of a precipitate. The mixture was then filtered to remove the hydroxides from the saline solution consisting mainly of calcium chloride from the decomposition of the hydraulic binder and magnesium chloride from the destructuring of the chrysotile.

[0061] Example 2: Asbestos treatment process with calcium recovery

[0062] This process is illustrated schematically in [Fig. 1].

[0063] 500g of asbestos cement was roughly crushed into 3 or 4 cm pieces which were then introduced into a horizontal rotating reactor containing a PVC bar serving as grinding media and 1250 ml of 23% hydrochloric acid. The mill, arranged in a cradle on rollers connected to an electric motor, was set in rotation by activating this motor. Deflectors arranged inside the mill allowed the PVC bar to be raised and rolled over the load as the mill rotated. The foam height observed did not exceed 10% of the reaction medium, so it was not necessary to add an anti-foaming agent.

[0064] After 4 hours, the suspension obtained was filtered.

[0065] The filtrate was neutralized by adding 30% mass milk of lime, resulting in a precipitation of iron and aluminum in the form of hydroxides which were washed and dried. After neutralization, the water in the filtrate was evaporated and the solid was analyzed: it included 370g of CaCl2 (expressed as anhydrous salt) which was 98% pure.

[0066] For its part, the solid from the grinder was rinsed with water before being transferred to a heated reactor equipped with mechanical stirring, in which the solid was suspended in a hydrochloric acid solution containing 30 g of HCl in 250 mL of water. The suspension was brought to a temperature close to the boiling point of the solution (95 °C) for one hour. The mixture was then filtered to separate the silica from the rest of the aqueous solution. The silica was then washed and dried, while the filtrate was brought back to a pH close to 7. To do this, 4.5 g of magnesium hydroxide (in the form of a 30% aqueous suspension) were introduced into the medium, then the water was evaporated and the solid obtained was analyzed: it contained 30 g of MgCl2 (expressed as anhydrous salt) pure to more than 95%.

Claims

Claims

1. A method of treating a solid material containing asbestos, characterized in that it comprises the following successive steps: (a) fragmenting the solid material to form fragments whose largest dimension is between 1 and 20 cm, (b) bringing the fragmented solid material into contact with an aqueous acid solution, at a temperature between 5°C and less than 50°C, in a horizontal rotary mill, so as to obtain a suspension, (c) optionally, separating the suspension from step (b) into a filtrate and a treated solid material, followed by suspending the treated solid material in an acid bath, (dl) optionally, heating the suspension from step (b) or (c), to a temperature between 50°C and 70°C, (d2) heating the suspension from step (c) or (dl) to a temperature between 80 and 110°C, preferably between 90 and 95°C,and (e) cooling the suspension obtained in step (d2).,

2. Method according to claim 1, characterized in that it further comprises, during or after step (a), a step of separating the metals present in the fragmented solid matter.

3. Process according to claim 1 or 2, characterized in that the filtrate from step (c) is treated so as to isolate the metal cation salts which it contains, by adjusting its pH to a value ranging from 5 to 7, advantageously by means of calcium oxide or hydroxide, so as to neutralize the residual acid and separate the iron and aluminum salts from the calcium salts.

4. Method according to any one of claims 1 to 3, characterized in that it comprises an additional step of recovering the carbon dioxide generated in step (b) and / or in step (dl).

5. Process according to any one of claims 1 to 4, characterized in that the acid not consumed in step (d2) is recycled to step (b) or (d1).

6. Method according to any one of claims 1 to 5, characterized in that it further comprises a step of filtration of the cooled suspension resulting from step (e), during a step (f), so as to obtain a filtrate containing metal chlorides and a solid fraction containing in particular silica.

7. Process according to claim 6, characterized in that the filtrate from step (f) is treated so as to isolate the metal cation salts which it contains, by adjusting its pH to a value ranging from 5 to 7, advantageously by means of magnesium oxide or hydroxide, so as to neutralize the residual acid and to separate the iron and aluminum salts possibly present from the magnesium and possibly calcium salts.

8. Method according to any one of claims 1 to 7, characterized in that the mineral binder contains at least one compound chosen from: a carbonate, in particular calcium carbonate; a calcium salt, oxide and / or hydroxide, in particular limestone and / or gypsum; oxides and / or hydroxides of iron, aluminum and / or magnesium; silica; alumina; an aluminosilicate; and mixtures thereof, preferably the mineral binder comprises at least one carbonate, optionally mixed with one or more of the aforementioned compounds.

9. Method according to claim 8, characterized in that said waste is chosen from: asbestos flocking; asbestos adhesives and coatings; floor covering plates or slabs (in particular tiles or earthenware), walls or roofs (in particular fiber cement sheets); asbestos plaster; pipes, in particular based on fiber cement, in particular ventilation pipes or water supply or drainage pipes; or furniture elements based on asbestos-cement plates covered with enamel.

10. A method according to any one of claims 1 to 3 and 5 to 9, characterized in that it comprises the following successive steps: (a) fragmenting the solid material to form fragments whose largest dimension is between 1 and 20 cm, (b) bringing the fragmented solid material into contact with an aqueous acid solution, at a temperature between 5°C and less than 50°C, in a horizontal rotary mill, so as to obtain a suspension, (c) separating the suspension from step (b) into a filtrate and a treated solid material, followed by suspending the treated solid material in an acid bath, (d2) heating the suspension from step (c) to a temperature between 80 and 110°C, preferably between 90 and 95°C, and (e) cooling the suspension obtained in step (d2).

11. Method according to any one of claims 1 to 10, characterized in

12. what acid is hydrochloric acid. Use of a horizontal rotary mill to decompose, using an acid solution, a solid material containing: (a) asbestos and (b) a mineral binder.

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