PROCESS AND FORMULATION FOR THE PREPARATION OF LIGNIN FIBERS

专利摘要:
The invention relates to a formulation for the melted preparation of lignin-based fibers, precursors of carbon fibers. This formulation comprises lignin, a plasticizer and a crosslinking agent capable of crosslinking with lignin at a temperature at least 10 ° C higher than the glass transition temperature of the intimate mixture of lignin and plasticizer. A process for the preparation of lignin-based fibers from this formulation comprises hot extrusion spinning of an intimate mixture of the components of the formulation, under conditions suitable for causing crosslinking of the crosslinking agent and the lignin in the terminal zone of the extrusion device implemented.
公开号:FR3062399A1
申请号:FR1750688
申请日:2017-01-27
公开日:2018-08-03
发明作者:Teddy FOURNIER；Ludivine JUNCA；Maxence FACHE；Celia Mercader
申请人:Association Pour Le Developpement De Lenseignement Et Des Recherches Aupres Des Univ Des Centres De；Faurecia Services Group SAS；Institut de Recherche Technologique Jules Verne；
IPC主号:

专利说明:

(® Agent (s): IPSIDE.
FR 3 062 399 - A1 ® PROCESS AND FORMULATION FOR THE PREPARATION OF LIGNIN FIBERS.
@) The invention relates to a formulation for the preparation by the molten route of lignin-based fibers, precursors of carbon fibers. This formulation comprising lignin, a plasticizing agent and a crosslinking agent capable of crosslinking with lignin at a temperature at least 10 ° C. above the glass transition temperature of the intimate mixture of lignin and of the plasticizing agent. A process for the preparation of lignin-based fibers from this formulation comprises spinning by hot extrusion an intimate mixture of the components of the formulation, under conditions suitable for causing crosslinking of the crosslinking agent and the lignin in the terminal zone of the extrusion device used.
The present invention is in the field of manufacturing carbon fibers from bio-based materials.
More particularly, the present invention relates to a process for the preparation of lignin-based fibers, by the melt technique, as well as to a formulation for the implementation of this process. The invention also relates to lignin-based fibers capable of being obtained by such a process, as well as an extrudate, in particular in the form of granules, capable of being obtained as an intermediate product during the use of said process. process. The invention further relates to the use of a lignin-based fiber obtained by a process according to the invention for the manufacture of carbon fibers, as well as, more generally, that a process for the manufacture of a carbon fiber from such a lignin-based fiber.
Carbon fibers are used in many fields, taking advantage of their particularly advantageous mechanical, electrical and thermal properties and their low weight.
The manufacture of carbon fibers from renewable bio-based materials, in order to overcome the problem of the programmed depletion of fossil resources, has been the subject of much research in recent decades. It has in particular been proposed by the prior art to manufacture such fibers from lignin, a macromolecule of complex structure with high carbon content which constitutes one of the main components of wood, and which is present in large quantities in nature.
Lignin offers the particular advantage of being able to be obtained by means of processes which are not toxic to the environment and at low cost. It can also be shaped by spinning to form fibers, which can be used as precursors of carbon fibers.
The processes for manufacturing carbon fibers from lignins developed by the prior art generally use the following successive stages: the preparation of lignin-based fibers, by spinning a formulation containing lignin, stabilization / structuring of the lignin-based fibers thus obtained by an oxidative heat treatment, and the carbonization of the stabilized fibers, to form the targeted carbon fibers.
In particular, the stabilization of lignin-based fibers is necessary to prevent these fibers from melting during the rise in temperature to which they are subjected during the carbonization step. Conventionally, on a laboratory scale, this stabilization is carried out by crosslinking the lignin under an oxidizing atmosphere, by exposing the fibers to very slow temperature ramps, of about 0.02 ° C / min, for very long periods, typically of the order of several hours and up to several days, to reach temperatures as high as 300 to 400 ° C. This process cannot however be transposed industrially continuously, since it is too long and costly in energy to implement.
There are currently two main spinning techniques for the preparation of lignin-based fibers: the so-called solvent or wet technique, and the so-called melt technique.
The present inventors are more particularly interested in the technique of preparing fibers by the molten route, in which the fibers are formed by spinning in the molten state, typically by means of an extrusion device, this technique having the advantages. very simple and quick to implement. Schematically, the lignin is subjected to a temperature gradient high enough to cause its creep, which makes it possible to stretch it to form a wire.
In this particular field of the preparation of lignin-based fibers by the melt spinning technique, also called fusion spinning, it has been proposed by the prior art, in order to improve the properties of suitability for spinning and the quality of the lignin, to modify it chemically and / or to add different additives to it.
Document DE 102014004797 describes for example a process for preparing lignin-based fibers from a formulation containing chemically modified lignin, more particularly esterified or etherified, and additives of various functions, such as a plasticizing function and / or a crosslinking function. However, such a process makes it possible to obtain only fibers based on short lignin, of approximately 10 to 20 cm. In addition, these fibers must still be subjected to a high temperature stabilization heat treatment before the final carbonization step aimed at obtaining the carbon fibers. As explained above, carrying out this thermo-oxidative stabilization step is time consuming and energy consuming.
In order to stabilize the lignin-based fibers obtained by fusion spinning, to overcome the problems associated with the implementation of the thermo-oxidative stabilization step of the fibers, it has otherwise been proposed by the prior art, illustrated in particular by document EP 2 644 758, of incubating the lignin fibers, obtained by fusion spinning, with a crosslinking agent, at a temperature at which no crosslinking occurs, then subjecting the fibers to a step of heat treatment at a temperature allowing the crosslinking of the lignin of the fibers with the crosslinking agent. If this process can be carried out at lower temperatures and faster than the heat treatment processes for thermo-oxidative stabilization of the fibers of the prior art, it nevertheless requires significant heating of the fibers, and a certain implementation time. The step of dipping the fibers in a bath containing the crosslinking agent is in particular long, costly, technically complex and restrictive to implement.
The present invention aims to remedy the drawbacks of the processes for preparing lignin-based fibers proposed by the prior art, in particular the drawbacks set out above, by proposing a process for such preparation, and a formulation for its implementation. , which make it possible to form lignin-based fibers, including long continuous fibers, in particular several hundred meters long, which are sufficiently stable to be able to be subjected directly to a carbonization step, to form fibers of carbon, without an oxidative intermediate stabilization heat treatment, or with an intermediate heat treatment of much shorter duration.
An additional objective of the invention is that such lignin-based fibers can be obtained quickly, easily, in a few steps and at low cost.
The invention also relates to the fact that this process can be applied to all forms of lignin, whatever their process of production, and including to the forms of unmodified lignin.
To this end, according to a first aspect, there is proposed by the present invention a process for the preparation of lignin-based fibers, precursors of carbon fibers. This process includes the following steps:
a / where appropriate, the intimate mixing of the components of a formulation comprising:
- lignin,
a miscible plasticizing agent, in particular hot, with lignin,
- And a crosslinking agent capable of crosslinking with lignin, under conditions, in particular temperature and time conditions, in which there is no crosslinking of the crosslinking agent and of the lignin, b / the spinning of this intimate mixture in a hot extrusion device comprising an extrusion head at the end, to form continuous wires, by application in the extrusion device of conditions, in particular temperature profiles and residence time in the device, which are such as:
- the temperatures applied in the extrusion device are higher than the glass transition temperature of the intimate mixture,
- And the temperatures, the residence time of the intimate mixture in the extrusion device, and the residence time of the intimate mixture in the extrusion head are such that the crosslinking reaction of the crosslinking agent and of the lignin is initiated in the extrusion head, and only in the latter, c / where appropriate, the drawing, in particular continuous, of the lignin-based threads obtained, to form fibers of lignin-based length.
The crosslinking agent is chosen so that its crosslinking reaction with lignin is initiated in a time less than the residence time of the intimate mixture in the extrusion head from a temperature higher by at least 10 ° C. at the glass transition temperature of the intimate mixture of lignin and the plasticizer.
In the remainder of this description, for convenience, the expression “operating crosslinking temperature” means the lowest temperature at which a crosslinking reaction of the crosslinking agent and of the lignin is initiated in a shorter time. the residence time of the intimate mixture in the extrusion head, which constitutes the terminal part of the extrusion device. According to the invention, the crosslinking agent is chosen so that this operative crosslinking temperature is at least 10 ° C. higher than the glass transition temperature of the intimate mixture of lignin and of the plasticizing agent.
According to the invention, the choice of the crosslinking agent, and the conditions of temperature and residence time of the intimate mixture in the different parts of the extrusion device, is preferably carried out concomitantly, so as to allow softening to be carried out. intimate mixture which is sufficient for the spinning of the intimate mixture and the formation of lignin-based yarns, while initiating the crosslinking reaction of the crosslinking agent and of the lignin in the terminal part of the extrusion device, and only in the latter.
It is within the competence of a person skilled in the art to make such a joint choice, knowing that typically, the residence time of the material in the terminal part of an extrusion device is from a few tens of seconds to a few minutes , for example between 30 seconds and 5 minutes.
A person skilled in the art knows perfectly how to determine, according to the extrusion device which he implements, which part constitutes the extrusion head. Typically, this is the terminal part of the device, located downstream of the zones for supplying the device with material and for conveying this material, in the direction of flow of the material, and at the level of which it is produced. the shaping of the material. The extrusion head is notably terminated by the spinning die.
By the term lignin, according to the present invention is meant both a single lignin and a mixture of different lignins.
Likewise, by the expression "plasticizing agent" is included, in addition to a single plasticizing agent, any mixture of a plurality of plasticizing agents, and, by the expression "crosslinking agent", in addition to a single crosslinking agent, any mixture of a plurality of crosslinking agents.
Furthermore, also fall within the scope of the invention the processes according to which the plasticizing agent and the crosslinking agent are formed by a single and same compound, which alone combines the plasticizing function and the crosslinking function, and the characteristics to be miscible with lignin and to be able to initiate a crosslinking reaction with the latter in a time less than the residence time of the intimate mixture in the extrusion head of the extrusion device, from a temperature at least 10 ° C above the glass transition temperature of the intimate mixture it forms with lignin.
The term “intimate mixture of lignin and of the plasticizing agent” means, conventionally in itself, a mixture obtained by mixing these components at a temperature greater than or equal to the glass transition temperature of the lignin and to the melting point of the plasticizer. Typically, the glass transition temperature of the intimate mixture of lignin and the plasticizer is lower than that of lignin alone.
The glass transition temperature, designated by the abbreviation Tg, of the intimate mixture of lignin and of the plasticizing agent depends on the particular characteristics of the lignin and of the plasticizing agent used, in particular of the molar mass of the plasticizer, as well as their respective proportions in the mixture. It is within the skill of those skilled in the art to determine, for each given lignin - plasticizer mixture, what is the associated glass transition temperature. To this end, a person skilled in the art can in particular prepare an intimate mixture of these constituents, in the proportions of the formulation according to the invention, according to any conventional method in itself, then measure the glass transition temperature thereof. The skilled person will be able to implement any conventional process in itself, such as differential thermal analysis (DSC) or dynamic mechanical analysis (DMA).
According to the invention, the crosslinking of the crosslinking agent and of the lignin is advantageously carried out, at least partially, in the extrusion device itself. The crosslinking agent reacts there with lignin, to create a three-dimensional network which stabilizes the fibers, and which extends over the entirety of the yarns obtained, including the core of the fibers. This stabilization is advantageously sufficient to allow direct carbonization of the lignin-based fibers thus obtained, without it being particularly necessary to subject them beforehand to a thermo-oxidative stabilization treatment, or at least to nothing other than a very short-term heat treatment. An example of such a subsequent heat treatment may for example consist of heating the fibers in an oven, under oxygen or under nitrogen for example, for a period of a few tens of minutes, for example around 30 minutes, so as to complete quickly. the crosslinking of the crosslinking agent and of the lignin started in the extrusion device.
The crosslinking is also advantageously initiated only in the terminal zone of the extrusion device, at the level of the extrusion head itself, so that this crosslinking does not slow down or in any way block the spinning step of the method according to the invention.
The introduction, into the formulation according to the invention, of the crosslinking agent, and its intimate mixture with the lignin, before proceeding to melt spinning, makes it possible to form, at the end of the spinning step, a fiber containing lignin and the plasticizing agent, which has sufficient mechanical strength to withstand, without breaking, the rise in temperature necessary for the subsequent carbonization step.
Compared to the methods proposed by the prior art for achieving the stabilization of lignin fibers, in particular by crosslinking the lignin under an oxidizing atmosphere with very slow temperature ramps, the method according to the invention thus makes it much easier and more quickly to obtain fibers ready to be subjected to the carbonization step, and this at a lower cost.
The process according to the invention advantageously makes it possible to obtain continuous fibers of great length, in particular of several hundred, even several thousand meters.
In addition, it can be applied, with the same success, to lignins of any origin and of any kind and whatever the process which allowed them to be obtained. It also applies, with the same efficacy, to any form of lignin, including non-chemically modified lignins. It applies in particular to lignins having a low ability to thermo-oxidize.
It is easy and quick to set up, and it involves only a few steps. The lignin-based fiber obtained at the outlet of the extrusion device can also advantageously be put into a reel directly, or after if necessary a simple drawing step.
This process makes it possible to obtain, at low cost, lignin-based fibers capable of being subjected to a carbonization step to form carbon fibers.
The process for the preparation by the melted route of lignin-based fibers according to the invention can meet one or more of the characteristics described below, implemented in isolation or in each of their technically operative combinations.
In particular embodiments of the invention, the crosslinking agent is chosen to be capable of crosslinking with lignin in less than 10 minutes, preferably in less than 5 minutes, at a temperature between 30 and 190Ό, preferably between 80 and 170Ό.
Preferably, it is also chosen to be capable of crosslinking with lignin at room temperature, that is to say at a temperature of around 20 Ό, and more generally between 15 and 25 Ό, crosslinking at this temperature then being slow.
In particular embodiments of the invention, in the formulation, the plasticizing agent conventionally makes it possible to make the lignin more spinnable, at a lower temperature.
In the formulation according to the invention, the lignin and the plasticizing agent are preferably such, and in such proportions, that the glass transition temperature of the intimate mixture of said lignin and said plasticizing agent is between 0 and 180 Ό, included between 20 and 1800, preferably between 20 and 100 O, in particular between 20 and 80 O, and for example approximately equal to 60 O. Such a characteristic advantageously makes it possible to operate, for the implementation of the steps of the preparation process of lignin-based fibers according to the invention, at relatively low temperatures, which do not cause degradation of the various components of the formulation, and which can be achieved with low energy consumption.
The lignin used in the composition of the formulation according to the invention can be of any type.
By lignin is meant in particular in the present description both essentially pure, unmodified lignin and its derivatives. The term derivatives according to the present invention encompasses the partial fractionation of lignin, as well as the chemical derivatives of lignin, in particular esterified or etherified lignins.
Lignin can in particular be introduced into the formulation in the form of a salt, or else of a partially purified extract, containing it in mixture with other components. Such an extract can be obtained according to any conventional method in itself for the skilled person. For example, lignin can be introduced into the formulation in partially purified form, such as Kraft lignin or Soda lignin, or also in the form of Organosolv lignin, or of any mixture of such lignins.
The lignin used in the composition of the formulation according to the invention preferably has a high molecular weight, in particular a molecular weight of between 1,000 and 100,000 g / mol, preferably between 3,000 and 10,000 g / mol, and in particular between 5,000 and 10,000 g / mol.
A lignin which is particularly preferred in the context of the invention is the lignin marketed under the name Protobind 2400 by the company GreenValue. It is a sulfur-free lignin soda, obtained from wheat straw, having a glass transition temperature between 100 and 120 ° C and a molar mass between 5,000 and 7,000 g / mol. This lignin also has in particular a carbon content of between 55 and 65% of atoms, a rate of aliphatic -OH functions of between 1 and mmol / g, a level of aromatic -OH functions of between 2.5 and mmol / g , and a level of -COOH functions between 0.5 and 1 mmol / g.
Another lignin which can be used in the context of the invention is in particular Kraft-type lignin sold under the name BioChoice® by the company UPM. This lignin has in particular: a glass transition temperature of between 130 and 160 ° C; a molar mass of between 8,000 and 10,000 g / mol; a carbon content of between 60 and 70% of the atoms; a level of aliphatic -OH functions of between 1.5 and 2 mmol / g; a level of aromatic -OH functions of between 3.5 and 4 mmol / g; and a level of -COOH functions between 0 and 0.5 mmol / g.
The plasticizing agent used in the composition of the formulation according to the invention is preferably of the polymer type. The term “polymers” also includes copolymers here. The plasticizing agent is preferably chosen from polyethers, polycarboxylates and polyesters, such as for example poly (ethylene oxide) (PEO), polyethylene terephthalate or polycaprolactone, or any mixture of such polymers. The plasticizing agent according to the invention can otherwise be chosen from all the copolymers of which at least one of the segments belongs to one of the families of polymers above, for example the poly (ethylene oxide) -co-poly (oxide of propylene) (PEO-co-PPO) and more generally all the copolymers comprising a polyether block.
The plasticizing agent used preferably has a molecular weight greater than 100 g / mol. Such a characteristic gives the formulation according to the invention a sufficiently high hot viscosity to allow it to be easily handled during the carrying out of the steps of the method according to the invention, and to ensure good mechanical strength of the fiber based of lignin obtained at the end of this process.
More particularly, when the plasticizing agent belongs to the family of polyethers, its molecular weight is preferably between 500 and 10,000,000 g / mol, preferably between 100,000 and 1,000,000 g / mol and preferably between 300,000 and 500,000 g / mol.
When the plasticizing agent belongs to the family of polycarboxylates, its molecular weight is preferably between 100 and 100,000 g / mol, preferably between 500 and 50,000 g / mol and preferably between 500 and 30,000 g / mol.
The plasticizing agent used in the composition of the formulation according to the invention also preferably has a glass transition temperature of between -100 and 100 ° C, preferably between -60 and 60 ° C, especially between -40 and -70 ° C. Such a characteristic advantageously makes it possible to obtain a relatively low softening temperature for the intimate mixture of lignin and of the plasticizing agent, so that it is possible to transform this mixture at a relatively low temperature, at which it does not does not degrade its constituents.
Examples of plasticizing agents which can be used in the formulation according to the invention are in particular:
- poly (ethylene oxide) sold under the name Alkox® E30 by the company Meisei Chemical Works LTD. This product has a glass transition temperature between -50 and -60 ° C, a melting temperature between 55 and 60 ° C and a molar mass between 300,000 and 400,000 g / mol;
- the ether polycarboxylate sold under the name Ethacryl® HF by the company Coatex. This product has a glass transition temperature between -45 and -60 ° C and a melting temperature between 35 and 45 ° C.
The crosslinking agent used in the composition of the formulation according to the invention is preferably of molecular type. Any conventional crosslinking agent in itself for the crosslinking of phenolic resins can be used according to the invention.
The crosslinking agent is preferably chosen from:
- benzoxazines, epoxies, oxazolines, polyoxymethylenes, such as paraformaldehyde, aldehydes, such as glutaraldehyde, formaldehyde, furfural, etc., hexamethylenetetramine and hexamethylenemethoxymelamine;
- the compounds having a functionality greater than or equal to two, the chemical functions of which are chosen from the group consisting of functions: benzoxazine, epoxy, in particular glycidyl ether, isocyanate, anhydride, carboxylic acid, methylol and ester, these chemical functions possibly being identical or different, or any mixture of such compounds.
The crosslinking agent used according to the invention preferably has a crosslinking temperature operating with the lignin of between 30 and 190 ° C and preferably between 80 and 170 Ό.
Examples of crosslinking agents which can be used in the formulation according to the invention are in particular:
- bisphenolazine bisbenzoxazine F sold under the name Araldite® MT 35700 by the company Huntsman. This product has a glass transition temperature of 73.6 ° C, and a crosslinking temperature operating with lignin of 190 ° C;
- bisphenol A diglycidyl ether sold under the name Epolam® 8056R by the company Axson. This product has a glass transition temperature of approximately -20 ° Q, a crosslinking temperature operating with lignin of 120 ° C and a molar mass of less than 700 g / mol;
- 1,3-phenylene-bis-oxazoline sold under the name Nexamite® PBO by the company Nexamite. This product has a melting temperature of 149 ° C, a molar mass of approximately 216 g / mol, and is capable of crosslinking with lignin in less than 10 minutes at a temperature greater than or equal to 100 ° C.
In particular embodiments of the invention, in which the plasticizing agent and the crosslinking agent consist of one and the same compound, this compound is in particular a polymer with plasticizing function, functionalized so as to also have a crosslinking function. Mention may in particular be made, as such compound, of polyethers functionalized with epoxy functions.
The formulation according to the invention may contain the following weight percentages, relative to the total weight of the formulation:
- 50 to 98%, preferably 60 to 90%, and preferably 65 to 80%, of lignin,
- and / or 1 to 49%, preferably 5 to 30%, and preferably 10 to 25%, of plasticizing agent,
- And / or 1 to 25%, preferably 2 to 10%, and preferably 2.5 to%, of crosslinking agent.
Such proportions advantageously provide optimal properties, in particular in terms of mechanical strength and ease of preparation, of lignin-based fibers formed in accordance with the invention.
The formulation according to the invention may also include one or more other additives, aimed at better structuring the material, improving the mechanical properties of the fibers formed, etc.
Each of these additives may in particular be present in the formulation at a content of between 1 ppm and 10% by weight, relative to the total weight of the formulation, preferably between 1 ppm and 5% by weight, for example between 100 ppm and 1% by weight, relative to the total weight of the formulation.
Examples of additives which may enter into the composition of the formulation according to the invention are compatibilizing agents, such as grafted maleic anhydride polymers or co-polymers. By way of example, mention may be made in particular of the Lotader® 3300 marketed by the company Arkema, or even the Beiwa® 901 from DzBh.
The formulation according to the invention may for example comprise one or more additives chosen from carbon fillers of nanometric size, in particular from carbon nanotubes and graphene, alone or as a mixture.
The term “carbon nanocharge” is understood here to mean a filler comprising an element from the group formed by carbon nanotubes, carbon nanofibers, graphene, fullerenes and carbon black, or any mixture of such elements. Preferably, the carbon nanofillers integrated into the formulation according to the invention are carbon nanotubes, alone or in admixture with graphene. Carbon nanotubes are for example marketed by the company ARKEMA under the name Graphistrength®.
The carbon nanofillers according to the present invention may have a smaller dimension of between 0.1 to 200 nm, preferably between 0.1 and 160 nm, and preferably between 0.1 and 50 nm. This dimension can for example be measured by light scattering.
“Graphene” is understood to mean, according to the present invention, a planar graphite sheet, isolated and individualized, but also, by extension, an assembly comprising between one and a few tens of sheets and having a planar structure or more or less wavy. This definition thus includes FLG (for English Few Layer Graphene, that is to say weakly stacked graphene), NGP (for English Nanosized Graphene Plates, that is to say graphene plates nanometric dimension), CNS (for English Carbon NanoSheets, i.e. graphene nano-sheets), GNR (for English Graphene NanoRibbons, i.e. nano- graphene ribbons). On the other hand, it excludes carbon nanotubes and nanofibers, which consist respectively of the winding of one or more graphene sheets coaxially and of the turbostratic stack of these sheets.
It is within the competence of a person skilled in the art to determine, depending on the particular characteristics of the compounds used, which conditions, in particular temperature and time, must be applied for carrying out step a / of intimate mixing. components of the formulation, so as to achieve this intimate mixing without causing the crosslinking of the crosslinking agent and of the lignin.
In particular embodiments of the invention, step a / of intimate mixing of the components of the formulation comprises the following substeps, these substeps being able to be implemented successively or simultaneously, at least partially:
a1 / the preparation of the formulation, by mixing its components, in particular lignin, the plasticizing agent and the crosslinking agent, a2 / and the mixing by melting of said components of the formulation, at a temperature higher than the glass transition temperature of the lignin and the melting temperature of the plasticizing agent, to form an extrudate in which the lignin, the plasticizing agent and the crosslinking agent are in intimate mixture.
In particular, for the sub-step a1 / of mixing the components of the formulation, the components in the solid state can first of all be mixed by mechanical action, for example by means of a concrete mixer, preferably at room temperature. , so as to form a dry mixture.
The possible liquid components can, for their part, be incorporated at this time into this dry mixture, or subsequently during step a2 / of melting mixture of the components of the formulation, in the apparatus used for carrying out this step. Thus, the formulation according to the invention can be formed either upstream of this device, or in this device itself, extemporaneously, during the preparation of the intimate mixture of the components of the formulation according to the invention.
It is in particular entirely advantageous in the context of the present invention to integrate the crosslinking agent into the formulation in the apparatus making it possible to form, by fusion, the intimate mixture of the constituents of the formulation, so as to minimize exposing this crosslinking agent to high temperatures, and thereby avoiding the risk of triggering its crosslinking reaction with lignin.
The apparatus used for carrying out this sub-step a2 /, of mixing by fusion of the components of the formulation according to the invention, can be of any conventional type in itself for such an operation, commonly designated by the compounding term. It may in particular be a conventional extrusion mixing device in itself, for example an extrusion device of the twin-screw type, a co-kneader, an internal mixer, etc.
The extrudate obtained at the end of sub-step a2 /, which is formed from a material consisting of an intimate mixture of the components of the formulation, can then be subjected to step b / of spinning the process according to the invention, preferably after having been previously cooled, for example with air or any other effluent which would not degrade the material, then shaped into granules.
In particular embodiments of the method according to the invention, in step a /, the intimate mixing of the components of the formulation is preferably carried out at the lowest possible temperature, so as to avoid as much as possible any degradation of the materials used, it being understood that it must be produced at a temperature greater than or equal to the glass transition temperature of the lignin, which is generally between 100 and 160 ° C., and at the melting temperature cfe plasticizer, which is generally between 30 and 60 ° C.
In particular, the sub-step a2 / of melting by mixing is preferably carried out at a temperature between the glass transition temperature of the intimate mixture of lignin and of the plasticizing agent, and 100 ° C. above this temperature. .
For example, when the material used for carrying out this step is an extrusion device comprising a feed hopper, a mixing tank, a conveying means and an extrusion die, the temperatures at these different zones can be chosen as follows:
- temperature of the feeding zone between 0 and 100 ° C, preferably 20 and 80 ° C, and preferably 40 and 60 ° C;
- temperature of the mixing zone between 60 and 180 ° C, preferably 90 and 160 ° C, and preferably 100 and 130 ° C;
- temperature of the conveying zone between 60 and 180 ° C, preferably 90 and 160 ° C, and preferably 100 and 130 ° C;
- temperature of the extrusion die between 60 and 180 ° C, preferably 90 and 160 ° C, and preferably 110 and 140 ° C.
The advantage of such low temperature profiles is, on the one hand, to avoid the degradation of the main material which is lignin; on the other hand, in connection with a very short residence time of the material in the device, for example less than 5 minutes, it makes it possible to avoid crosslinking of the components of the intimate mixture in order to be able to envisage a new extrusion of the granules obtained. , for step b / of spinning.
The residence time of the material in the extrusion device, for carrying out step a / of intimate mixing of the components, is variable and chosen according to the particular characteristics of the compounds used. For example, it can be about 1 minute. At the end of this step a /, rods a few millimeters in diameter are recovered, which are subjected to the next step of the process.
In particular embodiments of the invention, the method comprises a prior step of steaming the components of the formulation, preferably at 80 ° C. and for at least four hours.
In particular embodiments of the invention, in step b / of spinning the intimate mixture of the components of the formulation, a temperature is applied in the extrusion head which is higher than the glass transition temperature. said intimate mixture, with a value between 10 and 150 ° C, preferably between 30 ° C and 100Ό, and preferably between 60 ° C and 90 ° C.
In this step b / of spinning the intimate mixture of the components of the formulation, a temperature is greater than or equal to the operating crosslinking temperature of the crosslinking agent with the lignin in the extrusion head.
The temperature of the extrusion head is preferably chosen, in relation to the residence time of the mixture inside, so that the crosslinking reaction of the crosslinking agent and of the lignin begins and takes place partially in the head of extrusion, but not complete.
Any conventional device in itself for a person skilled in the art can be used to carry out this step.
For example, when the material used for carrying out this step b / is an extrusion device comprising a feed hopper, a conveying means and an extrusion die, the temperatures at these different zones can be chosen as follows:
- temperature of the feeding zone between 50 and 180 ° C, preferably 80 and 150 ° C, and preferably 1æ and 130 ° C;
- temperature of the conveying zone between 60 and 180 ° C, preferably 90 and 160 ° C, and preferably 110 and 140 ° C;
- And temperature of the extrusion head between 100 and 250 ° C, preferably 150 and 200 ° C.
The operating parameters are also chosen in a conventional manner in itself for the skilled person.
The speed of rotation of the extrusion screw is in particular between 10 and 300 revolutions / minute.
The residence time of the material in the extrusion device is variable. It is preferably greater than 5 minutes.
During this step, the molten mixture is preferably directly extruded through the extrusion head at the outlet of the screw. It is then stretched in the molten phase during its cooling, for example in ambient air or in a water bath.
It should be noted that during this step, the crosslinking agent can not only react with lignin, but also with the plasticizing agent, depending on the characteristics of these compounds and the operating conditions used.
The lignin-based yarns thus obtained have physicochemical properties making it possible to form, by drawing these yarns, fibers of very great length, of several hundred, even several thousand, meters.
Step c / drawing of the wires can be carried out according to any method and using any apparatus known to a person skilled in the art for carrying out such an operation. It can in particular be carried out at a temperature causing a softening of the material constituting the wires. For this purpose, the wires pass successively through a bank of so-called supply rollers, through an oven brought to said temperature, then through a bank of so-called stretch rollers. They undergo a stretch between the two banks of rollers, according to the ratio of the rotational speeds of the feed rollers and the stretch rollers. They can otherwise be stretched on heating rollers rotating at different speeds.
Such stretching advantageously makes it possible to align the polymer chains along the axis of the fibers.
The fibers can optionally be treated at the end of spinning, by radiation treatments, such as gamma rays, beta rays, electron beams, UV rays.
As a last step, the lignin-based fiber obtained, which may have a considerable length, can be reeled, for example on a cardboard tube.
All of these steps of the process according to the invention for preparing lignin-based fibers were easy and quick to implement, with low energy consumption.
The process for the preparation of a lignin-based fiber according to the invention may comprise a final step of storing the lignin-based fiber at room temperature, that is to say at a temperature of about 20 ° C. , and more generally between 15 and 25 ° C. This sbckage is preferably for a duration greater than 1 day.
Such a step proves to be particularly advantageous in the embodiments in which the crosslinking agent is capable of crosslinking with the lignin at room temperature. It then allows the crosslinking reaction of the crosslinking agent and of the lignin, which was initiated in the extrusion device during step b / spinning of the process according to the invention, to continue, or even to end. A storage period at room temperature of a few days is particularly particularly preferred for this purpose in the context of the invention.
The invention does not however exclude storage of the lignin-based fiber at a lower temperature, for example at a temperature between 5 and 15 ° C.
The process for preparing a lignin-based fiber according to the invention can also comprise, as a replacement for this final storage step, or in addition to the latter, just before or after it, a heat treatment step short lignin-based fiber, for example of a few tens of minutes, in particular between 10 and 60 minutes, for example around 30 minutes, intended to allow the completion of the crosslinking reaction of the agent crosslinking agent and lignin started in the extrusion device during step b / spinning according to the invention. This heat treatment can be carried out under an oxidative atmosphere or not. It is preferably carried out at a temperature below 350 ° C. In particular embodiments of the invention, it is carried out at a temperature between 180 and 280 ° C.
According to a second aspect, the present invention relates to a formulation for the implementation of a process for the preparation, by the melt technique, of fibers based on lignin, precursors of carbon fibers, according to the present invention. This formulation includes:
- lignin,
- a miscible plasticizer, generally hot, with lignin,
- And a crosslinking agent capable of initiating a crosslinking reaction with lignin and having an operating crosslinking temperature at least 10 ° C above the glass transition temperature of the intimate mixture of said lignin and said plasticizer.
In particular embodiments of the invention, the formulation comprises a crosslinking agent capable of initiating a crosslinking reaction with lignin in less than 10 minutes, preferably in less than minutes, from a temperature higher than at least minus 10 ° C at the glass transition temperature of the intimate mixture of lignin and the plasticizer.
The formulation according to the invention, and its various components, can also meet one or more of the characteristics described above with reference to the process for preparing lignin-based fibers according to the invention.
According to a third aspect, the present invention relates to a lignin-based extrudate which can be obtained at the end of step a / of intimate mixing of the components of the formulation, and more particularly of the sub-step a2 /, of a process for the preparation of lignin-based fibers according to the invention. This extrudate is in particular in the form of granules.
Another aspect of the invention relates to a lignin-based fiber capable of being obtained by a process according to the invention, meeting one or more of the above characteristics.
This fiber can be either of the single-filament type or of the multi-filament type.
It is continuous, and can have a diameter between 1 and 1000 μm, preferably between 15 and 30 μm, and a length between one meter and several kilometers.
The lignin which constitutes it is there, at least in part, in a crosslinked form with the crosslinking agent, and this as much in the core of the fiber as on its surface, so that it exhibits mechanical strength under particularly good temperature rise.
According to another aspect, the present invention relates to the use of such a fiber according to the invention for the manufacture of carbon fibers.
More generally, the invention also relates to a process for manufacturing a carbon fiber, according to which a lignin-based fiber according to the invention is subjected, in particular obtained by a preparation process as described above, to a carbonization treatment, then graphitization if necessary.
The carbonization treatment can in particular be carried out on the fiber obtained at the end of step b / or of step c / of the process for preparing a lignin-based fiber according to the invention, without having previously submitted this fiber to an interlayer thermo-oxidative treatment.
The lignin-based fiber obtained at the end of step b / or of step c / of the process for preparing a lignin-based fiber according to the invention can in particular be subjected, prior to step carbonization treatment, UV, Gamma, Beta, electronic radiation treatment.
The process for manufacturing a carbon fiber according to the invention can also comprise, prior to the step of treatment by carbonization, a step of heat treatment of the fiber based on lignin of short duration, for example a few tens minutes, in particular between 10 and 60 minutes, for example around 30 minutes, intended to allow the completion of the crosslinking reaction of the crosslinking agent and of the lignin started in the extrusion device during the step b / of spinning according to the invention. This heat treatment, which can advantageously be carried out in the oven used for the carbonization treatment, can be carried out under an oxidative atmosphere or not. It is preferably carried out at a temperature below 350 ° C. In particular embodiments of the invention, it is carried out at a temperature between 180 and 280 ° C. The pressure applied in the oven is preferably between atmospheric pressure and 10 bars above atmospheric pressure.
In particular embodiments of the invention, the process for manufacturing a carbon fiber comprises, before carrying out the carbonization treatment step, a step of storing the lignin-based fiber, by example in the form of a coil, at ambient temperature, that is to say at a temperature of approximately 20 ° C., or more generally between 15 and 25 ° C. If the crosslinking agent used allows it, this storage step is preferably carried out for a sufficient time to allow the crosslinking reaction of the crosslinking agent and of the lignin, which has been initiated in the extrusion head of the extrusion device, to continue. The stability of lignin-based fibers is then advantageously all the more important.
The carbonization treatment of the lignin-based fiber can be implemented according to any conventional method in itself for the skilled person.
It can be carried out continuously, the fiber passing through the carbonization furnace, or batchwise, that is to say in static mode, the fiber preferably being kept under tension in the furnace.
Prior to carbonization, the fiber can be impregnated with an agent which aids in carbonization, such as a siloxane.
In particular embodiments of the invention, the carbonization oven is hermetically closed and put under vacuum until a value lower than 1.10 ⁴ Pa (0.1 bar). It is then filled with an inert gas, such as nitrogen, argon, etc., and a gas leak is created so that the gas flow is between 50 and 500 volume replenishments per hour. The pressure in the oven is preferably between 1.10 ³ Pa and 5.10 ⁴ Pa above atmospheric pressure. The temperature applied in the carbonization oven is preferably between 800 ° C and 1500 ° C.
At the end of this carbonization treatment, a carbon fiber is obtained.
This carbon fiber can then be subjected, if necessary, to a graphitization treatment, by heating to a temperature of 2500 ° C. under inert gas, so as to obtain a better structuring of the carbon, and therefore of the properties more advantageous mechanical.
The lignin-based fiber according to the invention can otherwise be carbonized continuously, by passing it successively through various ovens, including a carbonization oven under an inert atmosphere at a temperature between 800 ° C and 1500 ° C, then an oven gr ^ hitization at a temperature up to 2500 ° C. The speed of travel of the fiber in these ovens is then preferably between 1 and 100 m / h.
The characteristics and advantages of the invention will appear more clearly in the light of the examples of implementation below, provided for illustrative purposes only and in no way limit the invention, with the support of FIGS. 1 to 9, in which:
- Figure 1 illustrates schematically, in the form of a block diagram, the different steps of a process for manufacturing a carbon fiber according to the invention;
- Figure 2 shows a bar graph illustrating the hot melt index (MFI) measured at different temperatures, for granules obtained in the first step of a process according to the invention ("with crosslinker") and for granules obtained by a similar process, but not using a crosslinking agent (“without crosslinker”);
- Figure 3 shows a graph representing, as a function of temperature, the loss factor (tan delta) and the conservation modulus (E ') measured by dynamic mechanical analysis for a sample of granules obtained in the first step of a process for preparing lignin-based fibers according to the invention: without additional heat treatment (E0), with a heat treatment of 130 ° C for 5 min (E1) or a heat treatment of 130 ° C for 5 min, then 20 ° C up to 220 ° C for 100 min (E2);
- Figure 4 shows graphs illustrating the evolution of the hot melt index (MFI) measured respectively at a / 160 ° C, b / 130 ° C, depending on the sampling time, for granules obtained first step of a method according to the invention; on each of these graphs the reference area for calculating the MFI is indicated by a box;
- Figure 5 shows a graph representing, as a function of temperature, the loss factor (tan delta) and the conservation modulus (E ') measured by dynamic mechanical analysis for a sample of granules obtained in the first step of a process according to the invention: without additional heat treatment (E0 '), with a heat treatment of 130 ° C for 5 min (E1') or a heat treatment of 130 ° C for 5 min then from 20 ° C to 220 ° C for 100 min (E2 ');
- Figure 6 shows a scanning electron microscopy image of a lignin-based fiber obtained by a method according to the invention;
- Figure 7 shows an optical microscopy image of a carbon fiber obtained by direct carbonization of the lignin-based fiber of Figure 5, by a process for manufacturing carbon fibers according to the invention;
- Figure 8 shows graphs illustrating the evolution of the hot melt index (MFI) measured respectively at a / 130 ° C, b / 170 ° C, depending on the sampling time, for granules obtained first step of a process similar to the process according to the invention not using a crosslinking agent; on each of these graphs the reference area for calculating the MFI is indicated by a box;
- and Figure 9 shows a graph representing, as a function of temperature, the loss factor (tan delta) and the conservation modulus (E ') measured by dynamic mechanical analysis for a sample of granules obtained in the first step of a process similar to the process according to the invention not using a crosslinking agent, without additional heat treatment.
The different stages of a process for manufacturing a carbon fiber according to an embodiment of the invention are illustrated schematically in FIG. 1, in the form of a block diagram.
This process firstly comprises the manufacture of a lignin-based fiber, in accordance with the present invention.
In the first step a1 /, illustrated in 11 in the figure, it comprises the mixture of lignin, a plasticizer which is miscible with heat with lignin and a crosslinking agent capable of crosslinking with lignin, more precisely to initiate a reaction. crosslinking with lignin, in a few minutes at a temperature which is at least 10 ° C. above the glass transition temperature of the intimate mixture of lignin and of the plasticizing agent.
The next step a2 / of the process, illustrated at 12 in the figure, consists in carrying out the intimate mixing of the above components, by the so-called compounding technique, at a temperature higher than the glass transition temperature of the lignin and at the melting point of the plasticizer. At the end of this stage, an extrudate is obtained, in particular in the form of granules, in which the lignin, the plasticizing agent and the crosslinking agent are in intimate mixture. No crosslinking reaction has yet started at this stage of the process.
Step a1 / and step a2 / can be carried out successively or simultaneously, at least for some of the operations that they require.
The next step in the process for preparing a lignin-based fiber according to a particular embodiment of the invention, illustrated at 13 in the figure, consists of a spinning step b / of the extrudate obtained, in an extrusion device comprising an extrusion head at the end, to form continuous wires. To this end, operating conditions of temperature and residence time in the device are applied, which are such that the temperature applied in the extrusion device is higher than the glass transition temperature of the intimate mixture formed in the step. a2 /, so that this mixture is in fluid form; and the crosslinking of the crosslinking agent and of the lignin is caused in the end part of the extrusion device, in the extrusion head, and only in this end part.
A lignin-based fiber is obtained at the output of the extrusion device, which is subjected, where appropriate, to a step c / drawing, illustrated in 14 in the figure, conventional in itself.
The lignin-based fiber obtained is then subjected to a winding step, illustrated at 15 in the figure.
The process for manufacturing a carbon fiber according to the invention then comprises a step of carbonizing the lignin-based fiber, illustrated at 16 in the figure, and conventional in itself.
Optionally, it may include an intermediate step, illustrated at 17 in FIG. 1, of heat treatment of the lignin-based fiber in a reel, aimed at increasing its stability by progressing the crosslinking reaction of the crosslinking agent and of the lignin, at a temperature below 350 ° C and for a period not exceeding a few dozen minutes.
Example 1
1 / Formulation
The formulation in accordance with the invention implemented in this example contains the following constituent contents, expressed as a percentage by weight, relative to the total weight of the formulation:
- 76% of Protobind 2400 lignin sold by the company GreenValue,
- 20% of polyethylene oxide polymer sold under the name Alkox® E30 by the company Meisei Chemical Works, with a molar mass of between 300,000 and 400,000 g / mol (plasticizing agent),
- and 4% diglycidyl ether of bisphenol A, an epoxy compound marketed under the name Epolam 8056 R by the company Axson (crosslinking agent).
The properties of the plasticizing agent are as follows: glass transition temperature Tg = -50 / -60 ° C, melting temperature Tf = 55 - 60 ° C, crystallization temperature Te = 30 - 40 ° C.
The properties of the crosslinking agent are as follows: glass transition temperature Tg = -20 ° C., molar mass less than 700 g / mol.
The glass transition temperature of this formulation is approximately 30 ° C. Its operating crosslinking temperature is greater than 120 ° C.
2 / Process for preparing lignin fibers
From these ingredients, the process for manufacturing lignin fibers according to the following invention is implemented.
Compounding
The lignin and the plasticizing agent are mixed in the prior step by mechanical action. A worm feeder is used to pour this mixture into the feed hopper of an unheated extruder.
The extruder used is a Eurolab twin screw extruder from Thermo Scientific. The operating parameters are as follows:
- Screw diameter = 16 mm
- L / D ratio: 40
- Screw speed = 250 rpm
No degassing is carried out during the extrusion.
The temperatures of the different areas of the extruder are as follows:
- Temperature of the feeding area: 60 ° C
- Temperature of the mixing zones: 100 ° C and 120Ό
- Temperature of the conveying zones: 120 ° C and 135Ό
- Die temperature: 130 ° C
The extrusion die temperature is 30 ° C. below the operating crosslinking temperature of the crosslinking agent with lignin.
The crosslinking agent, which is in liquid form, is injected using a syringe pump into the penultimate heating zone (that is to say at the zone at 135 ° C. ). It therefore spends only a short time in the extruder, which avoids activating the crosslinking reaction with lignin.
A flexible and stretchable rod is obtained at the outlet of the die. The total lignin residence time in the extruder was less than 5 min.
This rod is air-cooled before being granulated.
Analysis of the granules obtained
The granules thus obtained are analyzed to determine their hot melt index (MFI, for the English Melt Flow Index) at different temperatures. This analysis consists of measuring the mass of material passing through a given die under the action of a fixed pressure, for a given time and at a fixed temperature. The more fluid the material, the greater the quantity of material leaving the die during this given time.
The analysis conditions are as follows. The temperatures tested are 130, 140, 150, 160 and 170 ° C. Once the drier is at the desired temperature, 5 g of material is inserted into the hopper of the MFI measuring device. So that this quantity is really at the desired temperature, it undergoes a preheating time of 5 min under a weight of 2.16 Kg, then a sample is taken every 10 seconds.
By way of comparison, the same measurement protocol is used, for granules obtained as indicated above, but without the addition of crosslinking agent.
The results obtained are shown in Figure 2.
For comparative granules without crosslinker (hatched bars on the graph), it can be seen that the higher the temperature, the higher the MFI index.
For the granules obtained in accordance with the invention (white bars on the graph): at 130 ° C., the MFI is weak, but higher than for the granules obtained without crosslinker. At 130 ° C, the unreacted thinner acts as a plasticizer and thins the mixture. After 6 minutes of flow under heating, a solidification is observed due to the crosslinking (the crosslinker has played its role well and has fully crosslinked the formulation: no more flow occurs). At 140 ° C, the MFI is slightly higher. The viscosity of the unreacted mixture is lower because the temperature is higher. Curing takes place more quickly, after 3 minutes of flow under heating. The kinetics of the reaction are accelerated because the temperature is higher. At 150 ° C., it can be seen that the MFI has been transported, and solidification takes place after only 2 minutes of flow under heating. This indicates that crosslinking has started during the warm-up time. Finally, at 160 ° C, there is no flow after 5 minutes, so solidification took place during the preheating time.
Thus, this demonstrates that the crosslinking agent reacts after a certain time and crosslinks the mixture, causing the viscosity to increase and the MFI to drop; furthermore, the time required for the reaction decreases as the temperature increases.
The granules are further analyzed by dynamic mechanical analysis (DMA) to measure their viscoelastic and mechanical properties as a function of temperature. To this end, at the end of the compounding step, they are subjected to additional heat treatments making it possible to simulate the behavior of the material during the subsequent steps of the process (spinning, then optional additional heat treatment): heat treatment at 130 ° C for 5 min; heat treatment at 130 ° C for 5 min then second pass from 20 to 220 ° C for 100 min. For comparison, a sample obtained directly after compounding is also analyzed.
A DMA 1 device from Mettler Toledo is used. The operating parameters are as follows:
- Type of stress: voltage
- Sample requested: parallelepiped; L = 5mm; l = 2mm; e = 0.8mm
- Temperature ramp: 2 ° C / min
- Frequency: 1 Hz
- Displacement: 2pm
The displacement is chosen so as to obtain a signal while remaining in the linear viscoelastic domain.
The results obtained are shown in Figure 3.
It is observed that the sample as obtained after compounding (E0) flows after the glass transition, so that it is suitable for subsequent spinning. The sample heated at 130 ° C for 5 min (E1) has a slightly offset glass transition, and the material does not flow after it; after the glass transition, the conservation modulus E ’is 5 to 10 times greater than that of the sample E0. The material has started to crosslink. Crosslinking is not complete, since a rise in E 'is observed between 130 ° C and 220 ° C. This result confirms that it will be possible to carry out the next stage of the process according to the invention at a temperature greater than or equal to 130 ° C. to start the crosslinking stage. For the sample having undergone the first temperature scan and a subsequent temperature scan between 20 and 220 ° C (E2), the glass transition is strongly shifted towards high temperatures and after this transition, E 'remains 10 times higher than that from E0. The material is completely crosslinked and does not flow. E ’reached by E1 at 220 ° C is very close to E’ reached by E2. This result shows the importance of the die temperature in the next step: a die that is too hot leads to complete crosslinking and obstruction of the extrusion head by the material.
Spinning
The granules obtained at the end of the compounding step are subjected to a spinning step by hot extrusion and then drawing of the fibers, as follows.
A horizontal single-table Scamex extruder of the Rheoscam type is used with an L / D ratio = 11, with 3 heating zones. The third heating zone controls the temperature of the extrusion head, and is adjusted to initiate crosslinking.
The temperatures used are more precisely the following:
- Temperature of the feeding area: 120 ° C
- Temperature of the conveyor zone: 140 ° C
- Extrusion head temperature: 180 ° C
The granules are introduced into the extruder, and the molten mixture is directly extruded through the extrusion head at the outlet of the screw, to form a wire, which is drawn while being cooled in the ambient air.
The wire then joins a bank of feeding rollers, speed 20 m / min, passes through an oven at a temperature of 160 ° C, then on a bench of drawing rollers, speed 40 m / min. It undergoes a stretch between the two banks of rollers, according to the ratio of the rotational speeds of the feed rollers and the stretch rollers. As a last step, the lignin fiber obtained is wound on a cardboard tube.
This fiber is in the form of a monofilament. It has a diameter of about 20 µm. Its length is around 1,000 meters.
This lignin fiber can be directly subjected to a carbonization step, to form a carbon fiber, without undergoing any intermediate oxidative heat treatment step.
For example, it can for this purpose be subjected to static carbonization under nitrogen and under tension with a temperature ramp from 20 to 1200 ° C at 3 ° C / min, cassically in itself. The carbon fiber then obtained is in the form of a monofilament, and has a diameter of approximately 10 μm.
Example 2
1 / Formulation
The formulation in accordance with the invention implemented in this example contains the following constituent contents, expressed as a percentage by weight, relative to the total weight of the formulation:
- 75% Protobind 2400 lignin,
- 20% of polyethylene oxide polymer sold under the name Alkox® E30 (plasticizer),
- and 5% bisphenol F bisbenzoxazine sold under the name Araldite® MT 35700 by the company Huntsman (crosslinking agent).
The properties of the plasticizing agent are as follows: glass transition temperature Tg = -50 / -60 ° C, melting temperature Tf = 55 - 60 ° C, crystallization temperature Te = 30 - 40 ° C.
The properties of the crosslinking agent are as follows: glass transition temperature Tg = 73.6 ° C., melting temperature Tf = 240 ° C.
The glass transition temperature of this formulation is approximately 30 ° C. Its operative crosslinking temperature is higher than 180 ° C.
2 / Process for preparing lignin fibers
From these ingredients, the process for manufacturing lignin fibers according to the invention is implemented as described above in Example 1, with the exception of the following operating parameters.
Compounding
The temperatures of the different areas of the extruder are as follows:
- Temperature of the feeding area: 60 ° C
- Temperature of the mixing zones: 100 ° C and 130Ό
- Temperature of the conveying zones: 130 ° C and 130Ό
- Die temperature: 130 ° C
The screw speed is 150 rpm.
The crosslinking agent used begins to crosslink with lignin at around 200 ° C. Extrusion temperatures being lower than its activation temperature, it plays the role of filler in the formulation. The rod at the outlet of the die is flexible and stretchable. It is air-cooled before being granulated.
Analysis of the granules obtained
The granules thus obtained are analyzed to determine their melt flow index MFI at different temperatures. The protocol used is the same as that set out in Example 1 above.
The temperatures tested are 160 and 190 ° C.
The results obtained are shown in Figure 4.
We calculate, for the sample treated at 160 ° C (graph a /), for the reference zone indicated by a box in the figure, a hot melt index MFI = 0.94 ± 0.41 g / 10min. For the sample treated at 130 ° C (graph b /), for the reference zone indicated by a box in the figure, a hot melt index MFI = 0.82 ± 0.29 g / 10min.
These results obtained at 160 and 190 ° C are self-explanatory: the MFI decreases over time for each temperature. This means that the crosslinking agent begins to act. In the next spinning step, crosslinking in the last zone of the extruder can be carried out, in order to obtain a lignin-based fiber that does not require a subsequent thermo-oxidation step.
The granules are also analyzed by dynamic mechanical analysis (DMA), according to the protocol indicated in example 1 above.
The results obtained are shown in Figure 5.
It is observed there that (sample as obtained after compounding (EO ') flows after the glass transition, and is therefore suitable for the next step of the process according to the invention. The sample treated at 130 ° C. for 5 min ( ET) has exactly the same behavior: crosslinking has not taken place. In both cases, there is a rise in E 'around 190 ° C., showing the start of crosslinking. The result obtained for the sample having undergone additional heat treatment from 20 ° C to 220 ° C (E2 ') conihne that the crosslinking has taken place: the glass transition takes place at higher temperature, and E' after this transition is 10 times higher than in the previous cases, there is still a signal: the material has not crept.
This confirms that crosslinking begins around 190 ° C
Spinning
The granules obtained at the end of the compounding step are subjected to a spinning step by hot extrusion then drawing of the fibers, according to the protocol described in Example 1 above.
The temperatures of the different areas of the extruder are as follows:
- Temperature of the feeding area: 130 ° C
- Temperature of the conveyor zone: 180 ° C
- Extrusion head temperature: 200 ° C
A lignin fiber of about 500 m in length and about 100 µm in diameter is obtained. A scanning electron microscopy image of this lignin-based fiber is shown in Figure 6.
3 / Preceded for the preparation of carbene fibers
This lignin fiber is directly subjected to a carbonization step, to form a carbon fiber, without first undergoing any step of oxidative heat treatment.
This step is carried out by static carbonization under nitrogen and under tension, with a temperature ramp from 20 to 1200 ° C at 3 ° C / min, in a conventional manner in itself. The carbon fiber obtained is in the form of a continuous monofilament with a length of approximately 20 cm, and has a diameter of approximately 50 μm.
An optical microscopy image of this carbon fiber is shown in Figure 7.
Example 3
1 / Formulation
The formulation in accordance with the invention implemented in this example contains the following constituent contents, expressed as a percentage by weight, relative to the total weight of the formulation:
- 72% of Protobind 2400 lignin sold by the company GreenValue,
- 18% of ether polycarboxylate polymer sold under the name Ethacryl® HF by the company Coatex, with a molar mass of between 100,000 and 150,000 g / mol (plasticizing agent),
- and 10% diglycidyl ether of bisphenol A, an epoxy compound marketed under the name Epolam 8056 R by the company Axson (crosslinking agent).
The properties of the plasticizer are as follows: glass transition temperature Tg = -45 / -60 ° C, melting temperature Tf = 35 - 45 ° C, crystallization temperature Tc = 0-15 ° C.
The glass transition temperature of this formulation is approximately 105 ° C. The operating crosslinking temperature of the crosslinking agent with lignin is greater than 130 ° C.
2 / Process for preparing lignin fibers
From these ingredients, the process for manufacturing lignin fibers according to the following invention is implemented.
Compoundaoe
A worm feeder is used to pour the lignin into the feed hopper of an unheated extruder. Ethacryl® HF is injected into this same feed hopper using a peristaltic pump, while the crosslinking agent is only injected into the penultimate heating zone before the die, using a pump syringe. It therefore spends only a short time in the extruder, which avoids activating the crosslinking reaction with lignin.
The extruder used is a LTE 26-40 twin screw coexisting extruder from Labtech Engineering Company LTD. The operating parameters are as follows:
- Screw diameter = 26 mm
- L / D ratio: 40
- Screw speed = 190 rpm
3 degassing openings are used during the extrusion.
The temperatures of the different areas of the extruder are as follows:
- Temperature of the feeding area: 80 ° C
- Temperature of the mixing zones: 120 ° C
- Temperature of the conveyor zones: 120 ° C
- Die temperature: 120 ° C
The extrusion die temperature is 10 ° C. below the operating crosslinking temperature of the crosslinking agent with lignin.
A flexible and stretchable rod is obtained at the outlet of the die. Total lignin residence time in the extruder was less than 1 min.
This rod is air-cooled before being granulated.
Spinning
The granules obtained at the end of the compounding step are subjected to a spinning step by hot extrusion and then drawing of the fibers, as follows. The operating protocol is as described in Example 1, with the exception of the temperatures of the extruder, which are as follows:
- Temperature of the feeding area: 130 ° C
- Temperature of the conveyor zone: 130 ° C
- Extrusion head temperature: 140 ° C
The wire obtained at the end of the extrusion step then joins a bank of feed rollers, at a speed of 27 m / min, passes through an oven at a temperature of 100 ° C., then onto a bank of rollers. drawing, speed 81 m / min.
As a last step, the lignin fiber obtained is wound on a cardboard tube.
This fiber is in the form of a monofilament. It has a diameter of about 30 µm. Its length is around 500 meters.
This lignin fiber can be directly subjected to a carbonization step, to form a carbon fiber, without undergoing any intermediate oxidative heat treatment step.
For example, it can for this purpose be subjected to static carbonization under nitrogen and under tension with a temperature ramp from 20 to 1200 ° C at 3 ° C / min, cassically in itself. The carbon fiber then obtained is in the form of a monofilament, and has a diameter of approximately 15 μm.
Example 4 - comparative example
By way of comparison, a process for the preparation of lignin-based fibers is used similar to the process according to the invention, which however does not use a crosslinking agent.
1 / Formulation
The formulation used in this example contains the following constituent contents, expressed as a percentage by weight, relative to the total weight of the formulation:
- 80% Protobind 2400 lignin,
- 20% of polyethylene oxide polymer sold under the name Alkox® E30 (plasticizer),
The glass transition temperature of this formulation is approximately 50 ° C.
2 / Process for preparing lignin fibers
From these ingredients, a process for manufacturing lignin fibers is implemented according to the operating conditions described above in Example 1, with the exception of the following operating parameters.
Compounding
The temperatures of the different areas of the extruder are as follows:
- Temperature of the feeding area: 60 ° C
- Temperature of the mixing zones: 100 ° C and 120Ό
- Temperature of the conveyor zones: 120 ° C and 130Ό
- Die temperature: 130 ° C
The screw speed is 250 rpm.
Analysis of the granules obtained
The granules thus obtained are analyzed to determine their melt flow index MFI at different temperatures. The protocol implemented is the same as that exposed in Example 1 above.
The temperatures tested are 130 and 170 ° C. The results obtained are shown in Figure 8, respectively in a / and in b /.
We calculate: for the sample treated at 130 ° C (graph a /), for the reference area indicated by a box in the figure, a hot melt index MFI = 0.42 ± 0.22 g / 10 min; for the sample treated at 170 ° C (graph b /), for the reference zone indicated by a box in the figure, a hot melt index MFI = 4.40 ± 1.07 g / 10min.
These results obtained at 130 and 170 ° C are self-explanatory: the MFI is constant over time for a given temperature and the MFI is higher and higher as the temperature increases. This means that the higher the temperature, the more fluid the lignin / plasticizer mixture.
The granules are also analyzed by dynamic mechanical analysis (DMA) according to the protocol indicated in example 1 above, for
The results obtained for the analysis of the sample from the compounding, without additional heat treatment, are shown in Figure 9.
It is observed there that the sample as obtained after compounding flows after the glass transition (loss of signal), and is therefore suitable for the next step of the process.
The sample treated at 120 ° C for 5 min has exactly the same behavior: crosslinking did not take place. A second pass at 220 ° C cannot be carried out, the sample having flowed into the device.
Spinning
The granules obtained at the end of the compounding step are subjected to a spinning step by hot extrusion then drawing of the fibers, according to the protocol described in example 1 above, with the operating parameters:
- Temperature of the feeding area: 160 ° C
- Temperature of the conveyor zone: 170 ° C
- Extrusion head temperature: 180 ° C
A lignin-based fiber is obtained which is about 500 m in length and about 100 µm in diameter.
3 / Process for preparing carbon fibers
This lignin-based fiber is directly subjected to a carbonization step, without first undergoing any step of oxidative heat treatment.
This step is carried out by static carbonization under nitrogen and under tension, with a temperature ramp from 20 to 1200 ° C. at 3 ° C./min, in a conventional manner in itself. During this step, we observe that the fiber melts and creeps at a temperature below 250 ° C, and that it breaks in the oven.
This demonstrates that it is not possible to directly carbonize the lignin-based fiber obtained in the absence of crosslinking agent.

权利要求:
Claims (19)
[1" id="c-fr-0001]
1. Process for the preparation of lignin-based fibers by the melt process, characterized in that it comprises:
a / the intimate mixture (11, 12) of the components of a formulation comprising:
- lignin,
a plasticizing agent miscible with said lignin,
- And a crosslinking agent capable of crosslinking with said lignin, under conditions in which there is no crosslinking of the crosslinking agent and of the lignin, b / the spinning (13) of the intimate mixture thus obtained in a device for hot extrusion comprising an extrusion head at the end, to form continuous wires, by application in said extrusion device of conditions such as:
- the temperatures applied in said extrusion device are higher than the glass transition temperature of said intimate mixture,
- And the temperatures, the residence time of said intimate mixture in said extrusion device and the residence time of said intimate mixture in said extrusion head are such that the crosslinking reaction of the crosslinking agent and of the lignin is initiated only in said extrusion head, c / if appropriate, the drawing (14) of the threads obtained to form fibers based on lignin of great length, the crosslinking agent being chosen so that its crosslinking reaction with said lignin is initiated in a time less than said residence time of said intimate mixture in said extrusion head from a temperature at least 10 ° C higher than the glass transition temperature of the intimate mixture of said lignin and said agent plasticizer.
[2" id="c-fr-0002]
2. Method according to claim 1, according to which step a / of intimate mixing of the components of said formulation comprises the following substeps:
a1 / the preparation (11) of said formulation, by mixing said lignin, said plasticizing agent and said crosslinking agent, a2 / the mixing by melting (12) of the components of said formulation, at a temperature above the glass transition temperature of lignin and at the melting point of the plasticizing agent, to form an extrudate in which the lignin, the plasticizing agent and the crosslinking agent are in intimate mixture.
[3" id="c-fr-0003]
3. Method according to any one of claims 1 to 2, according to which, in step b / of spinning (13) of the intimate mixture of the components of the formulation, it is applied in the extrusion head at a temperature higher than the glass transition temperature of said intimate mixture of a value between 10 and 150 ° C, preferably between 30 ° C and 100 ° C, and preferably between 60 ° C and 90 ° C.
[4" id="c-fr-0004]
4. Method according to any one of claims 1 to 3, according to which the lignin and the plasticizing agent are such, and in such proportions, that the glass transition temperature of the intimate mixture of said lignin and said plasticizing agent is between 0 and 180 ° C, preferably between 20 and 100 ° C.
[5" id="c-fr-0005]
5. Method according to any one of claims 1 to 4, according to which the lignin has a molecular weight of between 1,000 and 100,000 g / mol, preferably between 3,000 and 10,000 g / mol.
[6" id="c-fr-0006]
6. Method according to any one of claims 1 to 5, according to which the plasticizing agent is a polymer, preferably chosen from polyethers, polycarboxylates and polyesters, or any mixture of such polymers.
[7" id="c-fr-0007]
7. Method according to any one of claims 1 to 6, according to which the plasticizing agent has a glass transition temperature of between -100 and 100 ° C, preferably -60 and 60 ° C.
[8" id="c-fr-0008]
8. Method according to any one of claims 1 to 7, according to which the crosslinking agent is chosen from:
- benzoxazines, epoxies, oxazolines, polyoxymethylenes, aldehydes, hexamethylenetetramine and hexamethylenemethoxymelamine;
- the compounds having a functionality greater than or equal to two, the chemical functions of which are chosen from the group consisting of functions: benzoxazine, epoxy (glycidyl ether in particular), isocyanate, anhydride, carboxylic acid, methylol and ester, these chemical functions possibly being identical or different, or any mixture of such compounds.
[9" id="c-fr-0009]
9. Method according to any one of claims 1 to 8, according to which the crosslinking agent is capable of crosslinking with lignin in less than 10 minutes, preferably in less than 5 minutes, at a temperature between 30 and 190 ° C, preferably between 80 and 170 ° C.
[10" id="c-fr-0010]
10. Method according to any one of claims 1 to 9, according to which the crosslinking agent is capable of crosslinking with lignin at room temperature.
[11" id="c-fr-0011]
11. Method according to any one of claims 1 to 10, according to which said formulation comprises the following percentages by weight, relative to the total weight of the formulation:
- 50 to 98%, preferably 60 to 90%, and preferably 65 to 80%, of lignin,
- and / or 1 to 49%, preferably 5 to 30%, preferably 10 to 25%, of plasticizing agent,
- And / or 1 to 25%, preferably 2 to 10%, preferably 2.5 to 5%, of crosslinking agent.
[12" id="c-fr-0012]
12. Method according to any one of claims 1 to 11, according to which said formulation comprises one or more additives chosen from carbon fillers of nanometric size, in particular from carbon nanotubes and graphene, alone or as a mixture.
[13" id="c-fr-0013]
13. Method according to any one of claims 1 to 12, comprising a final step of storing said lignin-based fiber at room temperature, preferably for a period greater than 1 day.
[14" id="c-fr-0014]
14. Formulation for the implementation of a process for preparing lignin-based fibers by the molten route according to any one of claims 1 to 13, characterized in that it comprises:
- lignin,
a plasticizing agent miscible with said lignin,
- And a crosslinking agent capable of initiating a crosslinking reaction with said lignin in less than 10 minutes from a temperature at least 10 ° C above the glass transition temperature of the intimate mixture of said lignin and said plasticizing agent .
[15" id="c-fr-0015]
15. Lignin-based extrudate capable of being obtained at the end of step a / of intimate mixing (11, 12) of the components of the formulation of a process according to any one of claims 1 to 13, in particular in the form of granules.
[16" id="c-fr-0016]
16. Lignin-based fiber capable of being obtained by a process according to any one of claims 1 to 13.
[17" id="c-fr-0017]
17. Use of a lignin-based fiber according to claim 16 for the manufacture of carbon fibers.
[18" id="c-fr-0018]
18. A method of manufacturing a carbon fiber, according to which a lignin-based fiber according to claim 16 is subjected to a carbonization treatment (16).
[19" id="c-fr-0019]
19. A method of manufacturing a carbon fiber according to claim 18 comprising, prior to the treatment of said fiber
5 lignin by carbonization (16), a heat treatment step (17) of said lignin fiber for a period of between 10 and 60 minutes.
1/4
MFI (g / 10 min)

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同族专利:

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公开号 | 公开日

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US20190390374A1|2019-12-26|

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WO2018138450A1|2018-08-02|

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FR3062399B1|2020-11-27|

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EP3574135A1|2019-12-04|

引用文献:

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公开号 | 申请日 | 公开日 | 申请人 | 专利标题

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EP2644758A1|2012-03-29|2013-10-02|Honda R&D Europe GmbH|Stabilization of lignin carbon fibers with crosslinkers|

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DE102014004797A1|2013-05-24|2014-11-27|Deutsche Institute Für Textil- Und Faserforschung Denkendorf|Precursor fibers of lignin-based carbon fibers, their preparation and use|

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CA2763986A1|2009-06-01|2010-12-09|The University Of Guelph|Lignin based materials and methods of making those|EP3633005A1|2018-10-05|2020-04-08|Aarhus Universitet|An aqueous adhesive composition for lignocellulosic materials such as wood and a method of production|

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DE102019004219A1|2019-06-17|2020-12-17|Faserinstitut Bremen E.V.|Lignin precursor and process for the production of a lignin precursor for the production of carbon fibers|

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CN111549449A|2020-04-30|2020-08-18|西安工程大学|Preparation method of lignin-based flexible carbon nanofiber self-supporting electrode material|

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CN111472069B|2020-05-28|2021-06-25|中国科学院化学研究所|Porous activated carbon fiber and preparation method thereof|

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CN112250497A|2020-09-17|2021-01-22|长沙联美生物科技有限责任公司|Lignin-based modified coating material and preparation method and application thereof|

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CN113046864A|2021-03-18|2021-06-29|湖南蓝凯新材料科技有限公司|Phenolic resin improved lignin carbon fiber and preparation method thereof|

法律状态:
2018-01-30| PLFP| Fee payment|Year of fee payment: 2 |

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2018-08-03| PLSC| Publication of the preliminary search report|Effective date: 20180803 |

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2020-01-30| PLFP| Fee payment|Year of fee payment: 4 |

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2021-01-29| PLFP| Fee payment|Year of fee payment: 5 |

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2021-12-15| PLFP| Fee payment|Year of fee payment: 6 |

优先权:

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申请号 | 申请日 | 专利标题

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FR1750688A|FR3062399B1|2017-01-27|2017-01-27|METHOD AND FORMULATION FOR THE PREPARATION OF LIGNIN FIBERS|

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FR1750688|2017-01-27|FR1750688A| FR3062399B1|2017-01-27|2017-01-27|METHOD AND FORMULATION FOR THE PREPARATION OF LIGNIN FIBERS|

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US16/481,195| US20190390374A1|2017-01-27|2018-01-29|Method and formulation for preparing lignin fibres|

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PCT/FR2018/050191| WO2018138450A1|2017-01-27|2018-01-29|Method and formulation for preparing lignin fibres|

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EP18705429.1A| EP3574135A1|2017-01-27|2018-01-29|Method and formulation for preparing lignin fibres|