Classifications

• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
  • D01F9/00—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments
  • D01F9/08—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments of inorganic material
  • D01F9/12—Carbon filaments; Apparatus specially adapted for the manufacture thereof
  • D01F9/14—Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments
  • D01F9/20—Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from polyaddition, polycondensation or polymerisation products
  • D01F9/21—Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from polyaddition, polycondensation or polymerisation products from macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
  • D01F9/22—Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from polyaddition, polycondensation or polymerisation products from macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyacrylonitriles
• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
  • D01F9/00—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments
  • D01F9/08—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments of inorganic material
  • D01F9/12—Carbon filaments; Apparatus specially adapted for the manufacture thereof

Definitions

• the invention relates to the high temperature heat treatment of carbon products containing sodium, and more particularly the treatment of gaseous effluents produced during the heat treatment.
• a particular field of application of the invention is the production of carbon fiber textures or preforms intended to constitute fibrous reinforcements for parts made of composite material such as carbon / resin composite, for example C / epoxy or C / phenolic, or thermostructural composite, for example carbon / carbon composite (C / C) or ceramic matrix composite and carbon reinforcement.
• Such fibrous textures are usually obtained from carbon precursor fibers which are more apt to undergo the textile operations required for the shaping of these textures.
• carbon precursor fibers are preoxidized polyacrylonitrile (PAN) fibers, pitch fibers, phenolic fibers and rayon fibers.
• a first carbonization step proper by chemical transformation of the precursor into carbon this first step being carried out on an industrial scale in an oven by gradually raising the heating temperature of the oven to around 900 ° C.
• a second step of high temperature heat treatment aiming in particular to remove by sublimation the sodium coming from the precursor, this second step also being carried out in an oven by gradually raising the temperature to approximately 1600 ° C., or even up to approximately 2000 ° C to 2200 ° C, or even 2500 ° C to remove other metallic impurities or carry out a very high temperature heat treatment of carbon fibers.
• the second step is generally carried out under reduced pressure and under sweeping of neutral gas such as nitrogen.
• the second step is usually carried out before densification of the fibrous texture by the resin, carbon or ceramic matrix of the composite material.
• the densification can be carried out by the liquid route, that is to say impregnation with a liquid compound, such as a resin, precursor of the material of the matrix, and transformation of this precursor by heat treatment. Densification can also be carried out by gas, that is to say by chemical vapor infiltration, the two processes, liquid and gas being well known and can possibly be combined.
• the object of the invention is to propose a method which avoids the aforementioned drawback by preventing the formation on walls of gaseous effluent extraction pipes of potentially dangerous deposits at the stage of cleaning these pipes.
• This object is achieved by a process of the type in which the carbon products are heated in an oven, under neutral gas sweeping and under reduced pressure, with continuous extraction from the effluent oven.
• gaseous containing in particular sodium in sublimated form by an effluent evacuation pipe, process in which, in accordance with the invention, at least one sodium neutralization product is injected into the effluent evacuation pipe, immediately downstream of the gaseous effluent outlet from the furnace.
• sodium neutralization product is meant a product making it possible to obtain a stable sodium compound which is fairly easily eliminated.
• a fairly easy handling product is chosen, for example water vapor or preferably carbon dioxide possibly mixed with water vapor.
• the neutralization product can be injected at or downstream of an elbow formed by the evacuation pipe for gaseous effluent out of the oven.
• the injected neutralization product can also be diluted in a neutral gas such as nitrogen.
• the neutralization product can be continuously injected into the gaseous effluent stream extracted from the oven during the heat treatment, so as to form a stable and easily removable sodium compound and avoid the deposition of sodium on the wall of the evacuation.
• the neutralization product is injected into the evacuation pipe after the end of the heat treatment in order to neutralize the sodium deposited on the wall of the evacuation pipe, before cleaning of the latter.
• Another object of the invention is to provide an installation making it possible to implement the method. This object is achieved by an installation for heat treatment of carbon products containing sodium, of the type comprising an oven, means for supplying the oven with neutral purging gas, and a pipe for extracting gaseous effluent from the oven, installation which further comprises, in accordance with the invention means for injecting a sodium neutralization product into the extraction pipe immediately after removal from the oven.
• FIG. 1 is a very schematic general view of an installation according to one embodiment of the invention.
• FIG. 2 is a detail view showing part of a device for extracting gaseous effluent from the furnace of the installation of Figure 1;
• FIG. 3 is a detail view showing a part of a device for extracting gaseous effluent from the furnace of the installation of Figure 1, according to another embodiment of the invention.
• heat treatment at high temperature is meant a treatment at a temperature usually higher than that encountered by the textures during carbonization, that is to say a temperature above 1000 ° C., typically between 1400 ° C. and 2000 ° C to 2200 ° C, even 2500 ° C.
• the heat treatment is carried out under reduced pressure, less than atmospheric pressure, preferably less than 50 kPa, typically between 0.1 kPa and 50 kPa, preferably less than 5 kPa, and with a sweep of neutral gas such as nitrogen or argon.
• the method according to the invention is applicable to the elimination of sodium present at low content in fibers, for example less than 80 ppm, or at much higher content, greater than 3500 ppm.
• FIG 1 very schematically shows an oven 10 comprising a susceptor 12 of cylindrical shape and vertical axis which laterally delimits a volume or enclosure 11 for loading carbon products (not shown).
• the susceptor 12 for example made of graphite, is surmounted by a cover 14, is heated by inductive coupling with an inductor 16 which surrounds the susceptor with the interposition of a thermal insulator 18.
• the inductor is supplied by a circuit 20 which delivers a current depending on the heating requirement of the oven.
• the inductor can be divided into several sections over the height of the oven. Each section is supplied separately with electric current in order to define different heating zones in the oven in which the temperature can be regulated independently.
• the bottom of the oven is formed by a thermal insulator 22 covered with an oven bottom 24, for example made of graphite, on which the susceptor 12 rests.
• the assembly is housed in an envelope 26, for example metallic, closed in leaktight manner by a removable cover 28.
• a pipe 30 provided with a valve 31 is connected to a source (not shown) of inert gas, for example nitrogen N 2 .
• Line 30 supplies the furnace 10 with inert sweeping gas at the upper part thereof, possibly by several inlets 32 opening in different places around the casing 26 of the furnace.
• An extraction device 40 is connected to an outlet duct 42 of the oven passing through the bottom of the latter, in order to extract the gaseous effluent produced during the thermal treatment of the carbon products, in order in particular to remove residual sodium therefrom.
• the device 40 is connected to the outlet conduit 42 by an evacuation pipe 44 provided with an inlet 46 for injecting carbon dioxide CO 2 .
• the pipe 44 forms an elbow 44a at its end connected by a flange 45 to the outlet duct 42 of the oven.
• the injection inlet 46 is connected to a pipe 48 connected to a source (not shown) of CO 2 gas and provided with a valve 49.
• the pipe 48 is extended by a nozzle 50 which enters the pipe 44 in order to inject the CO 2 gas into this pipe towards the downstream end of the elbow 44a and avoid accidental injection of the CO 2 gas inside the oven through the outlet duct 42.
• a nozzle 50 which enters the pipe 44 in order to inject the CO 2 gas into this pipe towards the downstream end of the elbow 44a and avoid accidental injection of the CO 2 gas inside the oven through the outlet duct 42.
• the CO 2 injection is carried out as close as possible to the outlet of the furnace, at a level where the sodium contained in the effluent is always in sublimated form.
• the injection at a bend in the pipe 44 promotes mixing by turbulence between the gaseous effluent and CO2.
• Two columns 52, 54 provided with plates 53, 55 imposing a tortuous path to the gases are connected in series between the line 44 and a line 56 provided with a valve 57.
• a pump 58 is mounted on the pipe 56, between the valve 57 and a valve 59 in order to be able to switch on or isolate the pump 58.
• the pump 58 makes it possible to establish the desired reduced pressure level in the oven. Although only one pump is shown, the presence of two pumps can be considered for the sake of redundancy.
• the gaseous effluent extracted by the pump 58 is brought to a burner 60 which feeds a chimney 62.
• the oven 10 is equipped with temperature sensors connected to the control circuit 20 in order to adjust the heating temperature to the desired value.
• Two sensors 64a, 64b are used, for example, constituted by optical sight pyrometers, which are housed on the cover 28 with regard to windows 28a, 28b made therein and openings 14a, 14b made in the cover 14 of the susceptor. .
• the use of several pyrometric sensors is not a necessity, but makes it possible to carry out measurements at different levels and to eliminate by comparison possible aberrant measurements.
• bichromatic type pyrometers are used which produce a continuous signal which is constantly usable.
• the temperature measured by the sensors 64a, 64b is transmitted to the control circuit 20 in order to supply the inductor to change this temperature according to a pre-established temperature rise profile. From a temperature of around 1000 ° C, depending on the pressure prevailing in the enclosure, the sodium contained in the fibrous textures is released and is evacuated with the gaseous effluent in a sublimed form, in the elementary state and optionally in the combined state, for example in the state of sodium oxide NaO 2 . CO 2 is injected into line 44 with a flow rate controlled by opening the valve 49 in order to neutralize Na (or Na ⁇ 2) as soon as it leaves the oven and to avoid its deposition on the walls of line 44.
• the injection of CO 2 can be started at a temperature below 900 ° C. This injection is also preferably continued at least until the end of the process.
• the sodium carbonate produced is collected in particular in the tray columns 52, 54.
• the gaseous effluent purified from sodium is brought to the burner 60.
• the extraction device 40 or at least part of it comprising the tray columns 52, 54 and optionally the pipe 44 is cleaned periodically in order to eliminate in particular the deposited sodium carbonate.
• the cleaning can be carried out by rinsing with water in situ or by washing with water in a washing container after at least partial disassembly of the extraction device.
• the sodium is neutralized by hydration.
• the pipe 44 is provided with one or more injection devices 70 for example in the form of hollow rings 72 surrounding the pipe 44.
• the injection device 70 is placed immediately downstream of the elbow 44a, with interposition an isolation valve 71 between the outlet 42 of the furnace and the injection device 70.
• two rings are provided spaced apart from each other along the pipe 44.
• the rings d injection 72 are supplied in parallel by a line 74 connected on the one hand to a source of neutralizing agent, for example a source of water vapor via a line 76 provided with a valve 75 and, on the other hand, to a source of neutral gas such as nitrogen or argon, via a pipeline 78 provided with a valve 57.
• a source of neutralizing agent for example a source of water vapor via a line 76 provided with a valve 75 and, on the other hand, to a source of neutral gas such as nitrogen or argon, via a pipeline 78 provided with a valve 57.
• the pipe 44 Downstream of the injection device 70, in the direction of flow of gaseous effluent, the pipe 44 has a drain orifice connected to a drain pipe 80 provided with a valve 81. Downstream of the connection with the pipe of purge, the pipe 44 can be connected directly to the pump 58 via the valve 57, the use of column trays not being essential here. The rest of the installation is identical to what has been described above.
• Each injection ring 72 forms a toric duct surrounding the pipe 44 and communicating with the latter through holes 74 formed in the wall of the pipe.
• the holes 74 can be inclined relative to normal to the wall of the pipe 44 to direct the flow of neutralizing agent downstream.
• the injection of the H 2 O + N 2 mixture can be carried out during the heat treatment process, as described above with respect to the injection of CO 2 , or after the end of the heat treatment process to hydrate the sodium deposited on the wall of the pipe 44.
• the pipe 44 in order to avoid a deposit of sodium on the wall of the pipe 44 upstream of the injection device closest to the outlet of the oven, the pipe 44 can be insulated along its part connecting the pipe outlet 42 to this injection device.
• the thermal insulation 43 makes it possible to avoid premature sodium condensation on the wall of the pipe 44 by too rapid cooling of the gaseous effluent.
• the thermal insulation 43 can be replaced or supplemented by heating means, for example by electrical resistances.
• valves 75 and 81 are open, the valves 71, 57 and 77 being closed and water in liquid form is admitted into the pipe 76 and, from there, into the injection device 70.
• Several rinses of line 44 can be carried out to remove the soda produced by neutralizing the sodium. After rinsing, the line 44 can be dried by simply opening the valve 57 and starting the pump 58, the valves 75 and 81 being closed.
• the CO 2 injected can also be diluted by mixing with nitrogen.
• Other alternative embodiments are possible, in particular by modifying the embodiment of FIGS. 1 and 2 so as to continuously inject not CO 2 , but water vapor or a mixture of CO2 and vapor, with possibly dilution by neutral gas.
• the process and the installation which have just been described are particularly suitable for carbon products obtained from preoxidized PAN precursor, in particular for fibrous carbon textures intended for the manufacture of parts made of composite material of carbon / resin C / type.
• C or C / ceramic for example with a silicon carbide matrix (C / SiC) or a silicon-boron-carbon ternary matrix (C / Si-BC).
• the textures are made of fibers in a carbon precursor state which are more capable of undergoing textile operations than carbon fibers.
• textures can be one-dimensional such as threads or cables, or two-dimensional, such as fabrics or webs formed of parallel threads or cables, or even three-dimensional, such as preforms obtained by filament winding, or by stacking, winding or draping fabrics or tablecloths in superimposed strata and possibly linked together by needling or sewing, for example.
• fibrous preforms are neck or divergent nozzle preforms or brake disc preforms.
• the invention also applies to carbon products, obtained from carbon precursor materials other than the pre-oxidized PAN, also containing sodium and possibly one or more other metals or metallic impurities to be removed. Examples of such precursors are pitches, phenolic materials, or rayon.
• the process according to the invention is advantageous in that it makes it possible to remove sodium present at very low content in the fibers, for example less than 80 ppm, sodium which would be impossible to remove by another process such as rinsing with water. 'water. It also makes it possible to eliminate sodium present in higher amounts in the fibers, for example at more than 3500 ppm. Besides sodium, calcium and / or magnesium can be removed by sublimation.
• metals such as Fe, Ni and Cr may also have to be removed in addition to the sodium. It is then necessary to carry out the heat treatment up to a temperature sufficient to ensure the sublimation of these metals, for example a temperature reaching 2000 ° C or 2200 ° C, or even 2500 ° C.

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• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• General Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Textile Engineering (AREA)
• Treatment Of Fiber Materials (AREA)
• Treating Waste Gases (AREA)
• Carbon And Carbon Compounds (AREA)
• Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
• Muffle Furnaces And Rotary Kilns (AREA)
• Furnace Details (AREA)
• Inorganic Fibers (AREA)
• Physical Or Chemical Processes And Apparatus (AREA)
• Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

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• 2002
  • 2002-07-12 FR FR0208818A patent/FR2842191B1/fr not_active Expired - Fee Related
  • 2002-09-26 US US10/256,224 patent/US7351390B2/en not_active Expired - Lifetime
• 2003
  • 2003-07-11 MX MXPA05000569A patent/MXPA05000569A/es active IP Right Grant
  • 2003-07-11 DE DE60327321T patent/DE60327321D1/de not_active Expired - Lifetime
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  • 2003-07-11 CA CA2492218A patent/CA2492218C/en not_active Expired - Fee Related
  • 2003-07-11 WO PCT/FR2003/002204 patent/WO2004007819A2/fr not_active Ceased
  • 2003-07-11 JP JP2004520775A patent/JP4327086B2/ja not_active Expired - Fee Related
  • 2003-07-11 AU AU2003267517A patent/AU2003267517A1/en not_active Abandoned
  • 2003-07-11 AT AT03748208T patent/ATE429533T1/de active
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