EP2688928A1

EP2688928A1 - Impact modifier and uses thereof in thermoset materials

Info

Publication number: EP2688928A1
Application number: EP12717369.8A
Authority: EP
Inventors: Thomas Fine; Jean-Loup Lacombe; Laurent Breysse
Original assignee: Arkema France SA
Current assignee: Arkema France SA
Priority date: 2011-03-25
Filing date: 2012-03-23
Publication date: 2014-01-29
Also published as: US20140018504A1; JP2014508845A; CN103562244A; FR2973033A1; KR20140019408A; WO2012131242A1

Abstract

The invention relates to an impact modifier and a device and a method for the production thereof, as well as to a method for preparing a thermoset material, or a thermoset material precursor, from the impact modifier. The impact modifier comprises at least one copolymer selected from among A-B-A, A-B and A-B-C type block copolymers, in which: each block is linked to the other by means of a covalent bond or an intermediate molecule that is connected to one of the blocks by a covalent bond and to the other block by another covalent bond; A is a PMMA homopolymer or a copolymer of methyl methacrylate, A preferably being compatible with the resin; C is either (i) a PMMA homopolymer or a copolymer of methyl methacrylate or (ii) a polymer based on monomers or a mixture of vinyl monomers, and blocks A and C can be identical; and B is incompatible or partially compatible with the thermoset resin and incompatible with block A and optional block C. The impact modifier is characterised in that it takes the form of microgranules having a diameter of less than 1500 μm, advantageously less than 1000 μm, preferably between 400 and 1000 μm. The ratio of the standard deviation/mean size of the particles is less than 10%, preferably less than 5%.

Description

MODIFYING SHOCK AND USES THEREOF

The present invention relates to a shock modifier, a device and a method for manufacturing said impact modifier, and to a method for preparing a thermoset material, or a precursor of thermoset material, from said modifier. shock. The invention will advantageously find application in the field of the preparation of thermoset materials and in particular thermoset materials with improved impact strength. These materials can be used in various fields such as aeronautics, electronics, automotive or industry, including as structural adhesives, matrices for composite materials or as protection elements for electronic components . BACKGROUND OF THE INVENTION

By "impact modifier" is meant in the present application, a compound which, mixed with a thermosetting material improves the mechanical properties of the polymerized thermosetting material. This can be reflected, for example, in improving elongation at break, impact resistance or fatigue resistance.

By "thermoset material" is meant in the present application, a material formed of polymeric chains of variable lengths interconnected by covalent bonds so as to form a three-dimensional network. By way of nonlimiting example, mention may be made of the following families of thermosets: epoxy, (metha) crylic, cyanoacrylate, bismaleimide, unsaturated polyesters, vinyl ester, phenolic and polyurethane.

The thermosets can be obtained by mixing a first so-called resin part with a second so-called hardener part. Shock modifiers can be in one or both parts or in both parts.

Among the various types of impact modifiers used in thermosetting resins, there may be mentioned, for example, impact modifiers that are solubilized in the precursor of thermosetting agents before polymerization. These shock modifiers are distinguished from shock modifiers type heart-bark particles that are dispersed in the precursor before polymerization. The first range of impact modifiers has the great advantage of not requiring expensive dispersing tools and is not subject to effects of segregation or destabilization of the dispersion.

More particularly, one is interested in block copolymers that can be found in the form of granules or powder such as those described in patents EP 1 866 369 and EP 1 290 088.

In practice, the dissolution of the impact modifier in the form of granules is not desirable for industrial constraints. Indeed, for a simple reason of exchange surface area on volume, one is automatically in a case of very unfavorable figure. Also, in order to dissolve the impact modifier more rapidly, the use of a shock modifier in the form of a powder is preferred. This powder can be dissolved in the precursor liquid solution (thermosetting material or hardener); however, the handling of the powder remains delicate and the dissolution difficult.

Indeed, the grains, when poured into the liquid precursor solution, tend to agglomerate with each other on the surface of the liquid creating agglomerates very difficult to lubricate. To limit this phenomenon, it is necessary to pour very slowly the grains to ensure optimal dispersion in the liquid solution. However, a slow payment does not always prevent the formation of agglomerates because the powder, even before payment, may tend to form in the form of lumps given the high percentage of the order of 30 to 60% of soft phase of the impact modifier in powder form and the presence of fine particles.

Furthermore, these fine particles generally complicate the handling of the impact modifier and in particular its weighing and dosing, and furthermore requires compliance with the European regulation on Atmospheres Explosibles (ATEX).

Finally, these particles in powder form are characterized by a ratio between the standard deviation and the median particle size high, greater than 15%. This very wide particle size distribution makes the process of solubilization of these impact modifiers in the form of a powder in the thermosetting precursor random. Given the aforementioned drawbacks it is understood that the step of dissolving the impact modifier, as currently practiced, is perfectible both in terms of convenience and speed or result in the mixture obtained. OBJECT OF THE INVENTION

The object of the present invention is to provide a shock modifier whose structure limits the risk of agglomeration both during its storage and during the mixing step in the precursor liquid solution.

The present invention also aims to provide a shock modifier whose structure facilitates the preparation of a thermoset material and more precisely its precursors.

The present invention also aims to provide a device and a reliable manufacturing process of this impact modifier. SUMMARY OF THE INVENTION

For this purpose, the invention relates to an impact modifier for a thermosetting resin comprising at least one copolymer chosen from block copolymers of type A-B-A, A-B and A-B-C, in which:

each block is connected to the other by means of a covalent bond or an intermediate molecule connected to one of the blocks by a covalent bond and to the other block by another covalent bond,

A is a PMMA homopolymer or a copolymer of methyl methacrylate, C is either (i) a homopolymeric PMMA or a methyl methacrylate copolymer (MMA) or (ii) a polymer based on monomers or a mixture of vinyl monomers; blocks A and C may be identical;

B is incompatible or partially compatible with said resin and incompatible with the block A and the eventual block C, and its glass transition temperature Tg is lower than that of the blocks A and C.

Typically, said shock modifier is in the form of microgranules of diameter between 400 and 1500 μιη, preferably between 400 and 1000 μιη, and advantageously between 500 and 800 μιη. This characteristic is particularly advantageous since the impact modifier in this form does not concentrate in clumps, either during storage in the dry phase or during its dispersion in the precursor liquid. In addition, surprisingly, the dissolution rate of the impact modifier in the form of microgranules is greater than or equal to that of the impact modifier in powder form conventionally used. The handling of these microgranules is also facilitated by the absence of fines generated by the associated manufacturing process. Advantageously, the ratio of the standard deviation / average particle size is less than 10%, preferably less than 5%, and advantageously less than 3%. This very narrow particle size distribution for the impact modifier according to the invention enables it to provide better control of the solubilization process in the precursor during the preparation of thermoset materials.

The present invention also relates to a method for manufacturing an impact modifier as mentioned above, by a solvent route, said process comprising an extrusion step, an underwater cutting step and a drying step. According to the invention, the extrusion step is carried out through a die having at least one orifice having a diameter of between 0.3 and 0.5 mm at a die temperature depending on the nature of the impact modifier and, the step of cutting under water is carried out in a granulator at a cutting water temperature to obtain a shock modifier in the form of microgranules of diameter between 400 and 1500 μιη, and preferably between 400 and 1000 μπι.

The term "extrusion" means in the cradle of the invention the extrusion bi-screw, single screw, BUSS, LIST or any other method for melting the impact modifier and pass through a die.

The invention also relates to a device for manufacturing an impact modifier, as mentioned above, in which the extruder comprises a die with at least one orifice of between 0.3 and 0.5 mm and preferably between 0.35 and 0.37 mm.

The invention finally relates to a method for preparing a thermoset material from said impact modifier. BRIEF DESCRIPTION OF THE DRAWINGS

The present invention will be better understood on reading a detailed example of embodiment with reference to the accompanying drawings, provided by way of non-limiting example, among which:

FIG. 1 represents an exemplary embodiment, in front view, of a die made according to the invention,

FIG. 2 represents an embodiment detail referenced I in FIG. 1 according to the sectional view A-A,

FIG. 3 is a front view of an exemplary embodiment of a separation grid made according to the invention,

FIG. 4 represents a 4a) image of the conventional granules of copolymer 1, for example, lifted in Example 1, whereas FIG. 4b) represents the microgranules according to the invention obtained at the end of the manufacturing process of the Example No. 1,

FIG. 5 is a diagram illustrating the continuous measurement over time of the viscosity of two resin mixtures obtained by mixing a precursor and a powder or microgranules.

DETAILED DESCRIPTION OF THE INVENTION

According to a first aspect, the present invention relates to an impact modifier for thermosetting resin comprising at least one copolymer chosen from block copolymers of type A-B-A, A-B and A-B-C, in which:

A is a PMMA homopolymer or a copolymer of methyl methacrylate;

A is preferably compatible with said resin,

It is either (i) a PMMA homopolymer or a copolymer of methyl methacrylate or (ii) a polymer based on monomers or a mixture of vinyl monomers; blocks A and C may be identical,

- B is incompatible or partially compatible with said resin and incompatible with the block A and the eventual block C. These AB, ABA or ABC block copolymers may be manufactured by any means of polymerization. Preferably, the controlled radical polymerization or anionic polymerization processes implemented using the solvent, emulsion, suspension or other method are used.

With regard to diblock A-B or triblock ABA, A is a PMMA homopolymer or a copolymer of methyl methacrylate. In the case where A is a copolymer, the comonomers used are preferably those based on alkyl methacrylate for forming a block A compatible with the thermoset resin. By way of example, mention may be made of alkyl methacrylates in which the alkyl group contains from 1 to 18 carbons: methyl methacrylate, ethyl methacrylate, propyl methacrylate, n-butyl methacrylate, t-butyl methacrylate and methacrylate. n-hexyl, cyclohexyl methacrylate, ethyl hexyl methacrylate, n-octyl methacrylate, lauryl methacrylate, tridecyl methacrylate stearyl methacrylate, isobornyl methacrylate. Mention may also be made, by way of example, of all comonomers which are soluble in water, such as acrylic or methacrylic acid, amides derived from these acids, such as, for example, dimethyl acrylamide, 2-methoxyethyl acrylate or methacrylate, and acrylates. or optionally quaternized 2-aminoethyl methacrylates, (meth) acrylates of polyethylene glycol (PEG), water-soluble vinyl monomers such as N-vinyl pyrrolidone or any other monomer soluble in water. By way of example, mention may also be made of all the reactive comonomers copolymerizable with methyl methacrylate. By reactive monomer is meant a chemical group capable of reacting with the functions of thermosetting resins. Block A can be formed of only one of these (meth) acrylic monomers or of several. By way of example, mention may be made of hydroxyethyl methacrylate, glycidyl methacrylate, maleic anhydride, acrylic or methacrylic acid.

Block A may be manufactured by any means of polymerization and in particular by controlled or anionic radical polymerization.

As regards block B, advantageously the Tg of B is less than 0 ° C. and preferably less than -40 ° C. By "Tg" is meant the glass transition temperature of a polymer measured by DSC according to the ASTM standard. E1356. The monomer used to synthesize the elastomeric B block may be a diene chosen from butadiene, isoprene, 2,3-dimethyl-1,3-butadiene, 1,3-pentadiene and 2-phenyl-1,3 butadiene. B is advantageously chosen from poly (dienes), especially poly (butadiene), poly (isoprene) and their random copolymers, or else from partially or completely hydrogenated poly (dienes). Of the polybutadienes, those with the lowest Tg are advantageously used, for example 1,4-polybutadiene of Tg (around -90 ° C.) which is lower than that of 1,2-polybutadiene. (around 0 ° C). Blocks B can also be hydrogenated.

The monomer used to synthesize block B may also be an alkyl (meth) acrylate, in which case the following Tg values are given in parentheses, following the name of the acrylate: ethyl acrylate ( -24 ° C), butyl acrylate (-54 ° C), 2-ethylhexyl acrylate (-85 ° C), hydroxyethyl acrylate (-15 ° C) and methacrylate 2 - ethylhexyl (-10 ° C). Butyl acrylate is advantageously used. Block B may also consist of a mixture of monomers. The acrylates are different from those of the block A to respect the condition of incompatibility of the blocks A and B.

In triblock A-B-C, C is either (i) a PMMA homopolymer or a methyl methacrylate copolymer as defined above (ii) a polymer based on monomers or a mixture of vinyl monomers.

The two blocks A and C of the triblock A-B-C may be identical or different. They can be different in their molar mass but consist of the same monomers. If block C contains a comonomer it may be the same or different from the comonomer of block A.

With regard to (ii) by way of example of blocks C, mention may be made of those derived from vinylaromatic compounds such as styrene, α-methyl styrene, vinyl toluene and those derived from alkyl esters of acrylic acids and / or methacrylic acid having 1 to 18 carbon atoms in the alkyl chain.

Block B consists of the same monomers and possibly comonomers as block B of diblock A-B or triblock ABA. The blocks B of the triblock A-B-C and diblock A-B may be identical or different.

Such shock modifiers are known for example from the WO document

2008/110564, which describes triblock copolymers of the SBM type, such as Nanostrength SBM Powder AFX E21, or MBM type, such as Nanostrength MAM M22, marketed by the Applicant. These impact modifiers differ from those according to the invention in the size of their particles (they are in the form of powders having a mean diameter of less than 240 μιη) as well as in the ratio of standard deviation / average size (which is greater than 16 %, as shown in Example No. 3 of the present application).

Shock modifiers according to the invention are in the form of microgranules of diameter between 400 and 1500 μιη, preferably between 400 and 1000 μιη, and advantageously between 500 and 800 μιη. Advantageously, the ratio of the standard deviation / average particle size is less than 10%, preferably less than 5%, and advantageously less than 3%.

According to a second aspect, the invention relates to a method of manufacturing the impact modifier described above in the form of microgranules with a diameter of between 400 and 1500 μιη, preferably between 400 and 1000 μιη, and advantageously between 500 and 800 μιη. Conventionally, the pellet production line of a few millimeters in diameter comprises a feed system, a granulator with an extruder and a die as well as underwater cutting means, the chain further comprises a conveying line, means for separating and drying the granules.

For the production of microgranules, tests have shown that the production line must be modified and that special adaptations were necessary both at the granulator and the dryer. The manufacturing process must also be modified to obtain microgranules of diameter between 400 and 1500 μιη, and preferably between 400 and 1000 μιη.

More precisely and with reference to FIG. 1, a die 1 is shown for the production of microgranules. This die 1 is intended to be fixed on the axis of the granulator, not shown in the accompanying figures.

According to the invention, the die 1 comprises at least one orifice 2 comprised between 0.3 and 0.5 mm and preferably between 0.35 and 0.37 mm.

In the example of FIG. 1, the die 1 has orifices 2 distributed in cluster 3. The die 1 comprises a set of clusters 3, each grouping one number of orifices 2 greater than ten. Other configurations are of course conceivable and the number of orifices 2 distributed over the entire die 1 can easily be modified depending on the characteristics desired for the granulator.

According to an advantageous characteristic of the invention, and as shown in FIG. 2, the orifices 2 of one and the same cluster 3 are distributed in a front hole 4. This arrangement is advantageous in that it limits the pressure drops. at the level of the sector 1.

In the example of Figures 1 and 2, the die 1 comprises 6 before hole 4, each grouping a cluster 3. Each cluster 3 has 15 orifices 2 of diameter 0.36 μιη. The thickness of the wall at the openings 2 is of the order of 4 mm, while the total thickness of the die being of the order of 55 to 60 mm. The diameter of each front hole 4 is of the order of 70 mm.

Referring now to FIG. 3, a separation grid 5 is shown, this separation grid 5 comprises circularly shaped openings 6 made in a plate 7. The openings 6 advantageously have a diameter of between 1.5 and 2 mm and preferably 1.7 mm. The separation grid 5 further comprises a square section mesh 8 disposed on the plate 7, the space between the meshes is between 180 and 220 μιη.

Tests have shown that the method of manufacturing granules of conventional size is not suitable for obtaining microgranules with a diameter of less than 1.5 mm.

Table 1 below makes it possible to compare different orders of quantities between the granules conventionally produced and the microgranules of the present invention.

Assumptions: microgranular granules p = 920 kg / m3; Q = 60 kg / h

Diameter granules (mm) 3 0.4

Ratio Surf ace / Volume (1 / mm) = 6 / D 2 15

Weight of 100 granules (gram) 1.3 0.025

Number of granules per gram (granules / g) 77 4000

Surface of the granules (cm / g of granules) 21.8 20.1

Table 1

Given the size of the microgranules and the holes of the die, the microgranules can quickly plug the orifices of the die 1. To avoid this phenomenon, it was found by the applicant, the need to increase the temperature of the die 1. For this purpose, the extrusion step is performed through a die 1 having at least one orifice 2 having a diameter of between 0.3 and 0.5 mm at a die temperature sufficiently high to maintain the microgranules in the liquid state.

Furthermore, given the important relationship between the surface and the volume of each microgranule, it was found that the microgranules cooled to their hearts during the cutting step under water. Therefore, it is necessary to set a high cutting water temperature to achieve the evaporation of water to the surface of the microgranule. To do this, the underwater cutting step is performed in a granulator at a cutting water temperature above 70 ° C.

The two manufacturing examples described below were obtained from the die 1 and the square grid 5 detailed above and made it possible to obtain each microgranular sample with a diameter of between 400 and 1500 μιη. and preferably between 400 and 1000 μιη. The equipment used in carrying out Examples 1 and 2 furthermore contained the following elements:

Feeding system

Volumetric doser

Corotative twin-screw extruder Φ 26, length 36D

Gear pump

No filtration

granulator

7 knives with angle of attack 45 '

maximum speed 5000 rpm

Line to separator

Length of about 3 m in DN 40

Flow rate 6 m ³ / h

Wringer and dryer water / granules

LPU model without agglomerates sensor

1500 rpm fixed speed rotor

Pulse air output pellet: blowing 3 seconds / pause 3 seconds

Example No. 1 Microgranulation of the Copolymer 1

The impact modifier "copolymer 1" corresponds to the triblock copolymer A-B-A in which A is a copolymer of methyl methacrylate (MMA) and dimethyl acrylamide (DMA) and the block B is a homopolymer of butyl acrylate.

Temperatures:

water: 75 ° C

die: 295 ° C

melt: 22 FC

microgranules: 45 ° C

Melt pressure at 137 bar obtained at approximately 30 kg / h of melt

granulator

7 knives with angle of attack 45 '

Maximum speed of knives 5000 rpm

Die: 90 holes diameter 0.36 mm Separator / dryer:

Air impulse every 3 seconds to evacuate the pellets from the descent dryer exit.

FIG. 4b represents a photograph of the microgranules obtained by this first example of microgranulation. It can be seen from this FIG. 4b that the method implemented in this example makes it possible to obtain good control of the section and homogeneous microgranules between them. Conventional granules obtained from the same copolymer 1 are presented for comparison in Figure 4a.

The particle size distribution by weight of the microgranules of the copolymer 1 is presented in Table 2. These results are obtained during a passage through the vibrating screen.

Table 2

Example n ° 2 of micro granulation of the copolymer 2

The impact modifier "copolymer 2" corresponds to the polystyrene-polybutadiene-polymethyl methacrylate copolymer.

Temperatures:

water: 65 ° C then change to 85 ° C

die: 350 ° C

melt: 225 ° C microgranules: 42 ° C

Pressure melt at 132 bar at 16 kg / h

granulator

7 knives with angle of attack 45 '

Maximum speed of knives 5000 rpm

Die with 90 holes Φ 0.36

This second example made it possible to obtain microgranules of sizes below one micrometer. The particle size distribution by weight of the microgranules of the copolymer 2 is shown in Table 3. These results are obtained during a passage through the vibrating screen.

Table 3

The impact modifier in the form of microgranules obtained in Examples 1 and 2 can then be used for the preparation of a thermoset material. The impact modifier in the form of microgranules can thus be used in a process for preparing a thermosetting material or a hardener.

The process for preparing the thermosetting material comprises a step of dissolution in the precursor of a composition comprising a shock modifier comprising at least one copolymer chosen from AB, ABA, ABC block copolymers in the form of microgranules with a diameter of between 400 and 1500. Dm, preferably between 400 and 1000 μιη, and advantageously between 500 and 800 μιη. Preferably, the impact modifier is chosen from block copolymers A-B, ABA or ABC.

It has been found that the use of a shock modifier for the manufacture of the thermosetting material considerably improves the preparation of the thermosetting material.

On the one hand, the problems related to the agglomeration and the manipulation of the impact modifier in the form of powder are eliminated and, on the other hand, the dissolution of the impact modifier in the form of microgranules makes it possible surprisingly to dissolve faster than under the shape of a powder.

The mechanical properties of the thermosetting material obtained from an impact modifier in the form of microgranules are also very close to those of a material obtained from an impact modifier in the form of powder.

Comparative tests have made it possible to compare the characteristics of resins obtained by mixing a precursor and a powder or microgranules. Referring to the appended FIG. 5, it is also possible to measure the viscosity of the two mixtures continuously over time. The viscosity of the mixture having used the impact modifier in the form of microgranules is of the same order of magnitude as that with the powder, the viscosities of each mixture remaining stable over time.

These tests show the advantage of producing a precursor of a thermoset material from a shock modifier in the form of microgranules.

Indeed the manipulation of the impact modifier is facilitated and the dissolution time of the microgranules in the precursor liquid is reduced compared to the dissolution time of a powder. Other features of the invention could also have been envisaged without departing from the scope of the invention defined by the claims below.

Example No. 3 Comparative Granulometry of Shock Modifiers: Granules and Powders

Particle size measurements for impact modifiers according to the invention (in the form of microgranules) and for impact modifiers according to WO 2008/110564 (in the form of powders) were carried out on the same measuring apparatus (automatic 'ALPAGA 500 nano® developed by the company OCCHIO).

The evaluations of the study concern the determination of the mean particle size of the following Nanostrengths:

micro granule grades (MG)

- E21 10C028 B076 # 3

- M22N 11MG008

- M52N 11MG001

powder grades (NP) - E21 NP 10M1032

- M22N NP 10M1030

- M52N NP 9M1812

The results are shown in Table 4 below. Average% gap

Grade measurement size (μιη) Standard deviation

(μπι) type

1,284.99

2,174.87

E21 NP 10M1032 3 230.81 233.48 39.46 17

4,231.84

5,244.87

1,117.52

2,128.08

M22N NP 10M1030 3,241.1 178.11 53.32 30

4,208.8

5,194.04

1,118.41 26

2,156.52

M52N NP 9M1812 3,240.43 180.66 47.16

4,209.95

5,178

E21 10C028 B076 1 694.43 <1

691.94 3.52

# 3 2 689.45

1,755.1 <1

M22N 11MG008 751.54 5.03

2,747.98

1,658.06 2

M52N 11MG001 647.54 14.88

2,637.02

Table 4

The grades have an average particle size:

- E21 MG (microgranulate): 692 μιη against 233 μιη in NP (powder) grade

- M22N MG: 751.5 μιη

- E21 MG: 647.5 μιη against 233 μιη in NP grade.

The size distribution shows a polydispersity 5 to 6 times higher for NP powder grades than for MG microgranules.

Claims

An impact modifier for a thermosetting resin comprising at least one copolymer chosen from block copolymers of type A-B-A, A-B and A-B-C, in which:

- A is a PMMA homopolymer or a copolymer of methyl methacrylate

((MMA);

It is either (i) a PMMA homopolymer or a copolymer of methyl methacrylate or (ii) a polymer based on monomers or a mixture of vinyl monomers;

the blocks A and C being identical or different;

B is an elastomeric polymer incompatible or partially compatible with said resin and incompatible with the block A and the optional block C,

characterized in that said impact modifier is in the form of microgranules of diameter between 400 and 1500 μιη, and preferably between 400 and 1000 μιη, and in that the standard deviation / average particle size ratio is less than 10%, and preferably less than 5%.

2. Impact modifier according to claim 1 wherein the block A being a copolymer of MMA, the comonomer is chosen from:

alkyl methacrylates in which the alkyl group contains from 1 to 18 carbons, namely methyl methacrylate, ethyl methacrylate, propyl methacrylate, n-butyl methacrylate, t-butyl methacrylate, n-hexyl methacrylate, methacrylate, cyclohexyl, ethyl hexyl methacrylate, n-octyl methacrylate, lauryl methacrylate, tridecyl methacrylate stearyl methacrylate, isobornyl methacrylate; water-soluble comonomers such as acrylic or methacrylic acid, amides derived from these acids, such as, for example, dimethyl acrylamide, 2-methoxyethyl acrylate or methacrylate, and optionally quaternized 2-aminoethyl acrylates or methacrylates, polyethylene glycol (PEG) (meth) acrylates, water-soluble vinyl monomers such as N-vinyl pyrrolidone or any other water-soluble monomer.

3. impact modifier according to one of claims 1 and 2 wherein the block A is compatible with said resin.

4. Impact modifier according to any one of the preceding claims wherein the Tg of the block B is less than 0 ° C, preferably less than - 40 ° C.

Shock modifier according to any of the preceding claims wherein the monomer used to synthesize block B is selected from:

dienes such as butadiene, isoprene, 2,3-dimethyl-1,3-butadiene, 1,3-pentadiene, 2-phenyl-1,3-butadiene;

poly (dienes), especially poly (butadiene), poly (isoprene) and their random copolymers;

poly (dienes) partially or totally hydrogenated;

polybutadienes, for example polybutadiene-1,4;

alkyl (meth) acrylates such as ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, hydroxyethyl acrylate and 2-ethylhexyl methacrylate.

6. Impact modifier according to any one of the preceding claims wherein the monomer used to synthesize the block C is selected from vinylaromatic compounds such as styrene, α-methyl styrene, vinyl toluene, or alkyl esters. acrylic and / or methacrylic acids having from 1 to 18 carbon atoms in the alkyl chain.

7. A method of manufacturing an impact modifier according to any one of claims 1 to 6, said method comprising an extrusion step, an underwater cutting step and a drying step and wherein:

The extrusion step is carried out through a die having at least one orifice having a diameter of between 0.3 and 0.5 mm,

the underwater cutting step is carried out in a granulator at a cutting water temperature greater than 70 ° C., which makes it possible to obtain a shock modifier in the form of microgranules with a diameter of between 400 and 1500 μιη, preferably between 400 and 1500. and 1000 μιη, and advantageously between 500 and 800 μιη.

8. Device for manufacturing an impact modifier according to any one of claims 1 to 6, wherein the extruder comprises a die (1) with at least one orifice (2) between 0.3 and 0.5 mm and preferably between 0.35 and 0.37mm.

9. Device for manufacturing an impact modifier according to claim 8 wherein the die (1) comprises a set of clusters (3) each having a number of orifices (2) greater than ten.

10. Apparatus for producing an impact modifier according to claim 8 wherein the die (1) comprises 6 clusters (3) of 15 orifices (2) of diameter 0.36mm.

11. Device for manufacturing an impact modifier according to claim 8 wherein each cluster (3) is disposed in a pre-hole (4) to reduce the pressure drop at the die (1).

12. Device for manufacturing an impact modifier according to any one of claims 8 to 11 wherein the separator / dryer providing the drying step comprises a separation grid (5) with openings of diameter between 1.5 at 2 mm and a square mesh (6) whose space between the meshes (6) is between 180 and 220 μιη.

13. Process for the preparation of a thermoset material from a thermosetting material and a hardener, at least one of which is obtained by the dissolution, in a precursor, of a composition comprising an impact modifier according to any one of Claims 1 to 6.

14. A process for preparing a thermosetting material comprising a step of dissolving in a precursor of a composition comprising an impact modifier according to any one of claims 1 to 6.