EP3245319A1 - Réacteur de carbonisation pour la production combinée de materiaux de construction et d'électricité à l'aide de la lumière solaire - Google Patents

Réacteur de carbonisation pour la production combinée de materiaux de construction et d'électricité à l'aide de la lumière solaire

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Publication number
EP3245319A1
EP3245319A1 EP16702656.6A EP16702656A EP3245319A1 EP 3245319 A1 EP3245319 A1 EP 3245319A1 EP 16702656 A EP16702656 A EP 16702656A EP 3245319 A1 EP3245319 A1 EP 3245319A1
Authority
EP
European Patent Office
Prior art keywords
tube
pyrolysis
phase
arrangement according
carbon
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP16702656.6A
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German (de)
English (en)
Inventor
Kolja Kuse
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Individual
Original Assignee
Individual
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Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of EP3245319A1 publication Critical patent/EP3245319A1/fr
Withdrawn legal-status Critical Current

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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
    • D01F9/32—Apparatus therefor
    • 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
    • D01F9/32—Apparatus therefor
    • D01F9/328—Apparatus therefor for manufacturing filaments from polyaddition, polycondensation, or polymerisation products
    • 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24S—SOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S23/00—Arrangements for concentrating solar-rays for solar heat collectors
    • F24S23/12—Light guides
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00—Energy generation through renewable energy sources
    • Y02E10/40—Solar thermal energy, e.g. solar towers
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
    • Y02P70/62—Manufacturing or production processes characterised by the final manufactured product related technologies for production or treatment of textile or flexible materials or products thereof, including footwear

Definitions

  • the present invention describes an arrangement for the simultaneous production of building material from carbon and electricity by means of sunlight.
  • the method is based on the basic idea of the European patent application with the application number 09796616.2, which describes how from the carbon in the atmosphere or the ocean in the form of CO 2 pressure and tensile construction and construction materials based on carbon fiber and hard rock (eg EP 106 20 92), whereby the carbon fiber is obtained from algae oil and the required production energy from concentrated sunlight.
  • the present invention describes how this can be technically and financially implemented.
  • the process proposed here uses a large part of the heat energy lost in conventional solar thermal power plants primarily for carbon fiber production and then heat for electricity production, and the electricity is thus produced as a "waste product" upstream of the material production process of power generation and all the heat, including the heat lost today in power generation, is previously used for the carbonization process of carbon fiber production, thereby increasing the efficiency of factor 3.
  • the invention deals with how this is technically implemented.
  • the biosphere In the method of decarbonating the atmosphere and the oceans described in 09796616.2 and at the same time binding the carbon in the carbon fiber building material to be produced, the biosphere is deprived of more carbon dioxide throughout the entire process chain, including the largely regenerative production of building materials, than during its production arises. Central to this is the provision of sufficient sea areas for algae production and if necessary. additional land for the production of suitable vegetable oils.
  • the consistent use of carbon fibers is proposed here as follows, since they can be used in an outstanding manner as building materials and at the same time bind carbon in this form in a climate-effective manner, especially if the starting materials required for carbon fiber production are vegetable oil getting produced.
  • Starting materials are, for example, polyacrylonitrile (PAN fiber) fibers, which today are produced in a relatively simple process from petroleum and a spinning solution. This starting solution will be produced with algae oil in the future, which makes no technical difference. The solution is pressed through a multitude of very fine nozzles in a spinning bath and crosslinks into thin threads during this process.
  • PAN fiber polyacrylonitrile
  • the invention proposes to carry out the energy-consuming part of the oxidation and carbonization with the aid of concentrated sunlight in a newly developed sunlight carbonation reactor (C-reactor).
  • C-reactor sunlight carbonation reactor
  • the fiber material is not heated in bulk or liquid form in large pots, bowls or basins as in steel, cement or aluminum, but is first produced in relatively cold surroundings to form thin, endless bundles of fibers that are already used in the heating processes fed solid and semi-zugstabiler form and thus easily introduced into the focal point, for example, a parabolic trough and moved in this.
  • Carbon fibers are also of interest because they are easy to handle in use and disposal, and above all remain inert for hundreds of millions of years due to a stable state of aggregation, because of the high production temperature is difficult to react when the material is kept or stored under normal environmental conditions becomes.
  • the bundling of the sunlight in order to achieve the necessary high pyrolysis temperatures takes place with the aid of Parabolic mirror technology or lenses, such as Fresnel glasses or other geometry of mirrors and / or glass or quartz glass, in which not the detour of generating electric power using solar thermal and conventional steam turbine generators or PV systems, the carbonization energy is generated, but the light directly on and through the fiber to be produced itself to pyrolysis energy.
  • Parabolic mirror technology or lenses such as Fresnel glasses or other geometry of mirrors and / or glass or quartz glass
  • the heating of the carbon strand by sunlight with simultaneous generation of electricity uses the solar energy with an up to 3 times higher efficiency, unlike a scenario in which the power is first produced in solar thermal power plants and then used in the carbon fiber ovens to heat the fibers Since both processes are subject to high heat losses and also the power transport with line losses.
  • the proposed arrangement uses at least 45% of the solar energy for the carbonization and the entire generated heat is as before the power generation available that works in the desert with an efficiency of about 30% and in cold plateaus with about 40%.
  • the available amount of sunlight is used in total to about 75%, compared to today with about 25%, since in the comparison scenario of carbon fiber production, the energy efficiency is 30% less 20% line loss and heat loss in the carbonization furnace. This results in an overall efficiency of up to 25% in the conventional process, in which sunlight would not be used directly, but via the indirect use of electricity generated by PV systems or conventional CSP systems for material production.
  • a suitable for the carbon fiber production output fiber for example, polyacrylonitrile, short PAN fiber, linearly introduced from one end of the linear parabolic mirror in the focal line of the parabolic mirror and with adjusted speed along the focal line in an oxygen-containing gas continuum moved on and heated until The initially bright PAN fiber is oxidized and becomes darker and darker in this oxidation process until it reaches the start of the oxidation phase at approx. 300 ° C has become very dark. The fiber is then moved along with the exclusion of oxygen - for example in a gas of predominantly nitrogen - along the focal line and in the pyrolysis phase under oxygen exclusion initially up to 800 ° C and then depending on the quality further to 1800 ° C or 3000 ° C.
  • the oxidized PAN fiber becomes blacker and darker with increasing carbon content in the pyrolysis phase and, as a result of this self-reinforced effect, increases in itself from ever higher temperatures until the fiber begins to glow.
  • the resulting temperatures must be controlled from the outside by cooling in order not to destroy the required equipment by overheating.
  • the surrounding the fiber strand gases must be transparent, so as not to hinder the heating of the fiber strand.
  • translucent solid vessels in rectangular or cylindrical tube form are also used. These may consist of transparent or translucent glass or another temperature-resistant and transparent or translucent solid such as quartz glass or high-temperature resistant plastic. Due to the rising along the focal line gas temperatures, the glass vessel walls must be cooled in the pyrolysis phase from the outside, so they do not melt.
  • This cooling is done with gas or liquids flowing between the inner and another vessel wall, which is also a transparent, rectangular or cylindrical tube.
  • the cooling gas or the cooling liquid are also translucent or transparent to allow the light to pass unattenuated to the carbon fiber strand.
  • air, water or temperature-stable oil, such as silicone oils can be used.
  • the heat is transferred via heat exchangers to a water cycle that drives steam turbine generators for the production of electricity. So that the carbon fiber strand does not sag due to gravity and thus gets out of focus, it must be guided. In the oxidation phase, there are no material problems, it can be used for the guide stainless steels, corrosive material should be avoided.
  • the materials used to center the fibers at the focal point must be so temperature-resistant that they do not melt at the temperatures applied.
  • the melting point is higher than the maximum achievable in pyrolysis temperature, or other high temperature resistant materials.
  • the tungsten wire is not so hot that it reaches the melting point of about 3,400 ° C, since the fiber at max. 3,100 ° C is completely carbonated.
  • this temperature must be maintained between 1500 ° C and 3000 ° C, depending on the altitude set.
  • the holding phase lasts longer at lower temperatures than at short temperatures. Since the fiber itself begins to radiate at appropriate temperatures, the further heating can and should be interrupted by bundled sunlight or even completely stopped. So that the fiber does not cool again by the own radiation, it is continued in a guide tube, which is mirrored from the inside, so that the heat energy is not in the form of radiation is radiated again and lost, which would mean that the necessary holding phase was interrupted or canceled.
  • a cooling phase begins, since the temperature of the finished carbon fiber must be brought back to normal ambient temperature.
  • the guide tubes Since the guide tubes must be correspondingly long, they are composed of similar parts. With the method described here for the production of carbon fibers is formed in the carbonation a large amount of heat that is dissipated at a specific time or at certain times, on the one hand, the guide tube is not too hot and does not melt and on the other hand, the fiber at the end of the pyrolysis process again is cooled. This cooling may also be by radiation or by mixed cooling by radiation and convection of internal and / or external coolants. The heat transfer is ensured by another enveloping pipe and the amount of heat is used via heat exchangers to produce electrical energy and ggfls.
  • the residual heat is also used for heating, as the process is preferably implemented in cold plateaus, since it increases the efficiency of power generation and the availability of sunlight appears optimal, such as in the plateaus of Peru, Peru or China.
  • the heated pyrolysis gas introduced into the carbonation tubes through the above-described nozzles must be exhausted to some extent at the end of the tube where the carbon fiber terminates the pyrolysis process to remove the pyrolysis-released gases such as hydrogen and oxygen dissipate.
  • This heated gas is also cooled by heat exchangers, cleaned and fed back to the pipe system in the cooled state at the beginning of each process. Heat the heat exchangers also the water cycle that drives the steam turbines.
  • the cooled gas is then returned to the carbonation tube through the above-described nozzles, with the oxygen being supplied to the gas during the oxidation phase.
  • the high energy needed to produce carbon fibers is provided by purely renewable energy sources, in this case the sun. Since the energy is obtained by heating a maximum black body, and not by the detour of power generation or the heating of other, less black body, the energy is optimally used in relation to the technical and thus financial expenditure made available sunlight and maximum energy and thus cost-efficient.
  • this sunlight not only produces the highest quality construction material, but also uses the heat energy generated by this process to generate electricity with solar thermal power plants, for example with the help of conventional steam turbines, if the heat developed during the carbonation process is deliberately dissipated and transmitted through heat exchangers a steam turbine is converted into electricity.
  • Electricity is produced as a "waste product" in addition to the output of high-quality construction and construction material.
  • the remaining heat that can not be used for power generation can be used to heat buildings, as such power plants are preferably located in cold regions such as plateaus not only because of the higher temperature gradients, the power generation is more efficient than in warm desert areas, which also provide sun around the clock, but also because of possible desert storms with damage to the sensitive glass and mirror surfaces by fine rubbing sand is to be expected.
  • further processing into carbon fiber end products could usefully be located near the C reactors.
  • this type of combined material and power generation creates a material that has the potential to permanently extract so much carbon from the atmosphere that a CO 2 concentration at the preindustrial level of 280 ppm can be regained within reasonable times.
  • 380 gigatons of carbon can be extracted from the atmosphere and / or the oceans over a period of 380 years at a start-up time of 30 years, when a total of 1.1 gigatonne carbon fibers are produced annually for 350 years vegetable oils were produced.
  • the absorption potential of the resin which can also be produced on the basis of algae oil, not yet considered.
  • C0 emissions should continue to rise to a level of 1000 ppm at the rates observed today.
  • the alga will have to be regarded as a source of raw material for two reasons. The first reason is that the extraction of vegetable oil does not compete with food production as the world's population is growing. Secondly, the oceans remove from the oceans that C0 2 responsible for the increasing acidification of the oceans.
  • the carbon fiber produced by this invention can make a significant contribution to the long-term and harmless geoengineering of greenhouse gases, the economy now no longer by the use of carbon fibers as a substitute for C0 2 - intensive materials such as steel and aluminum and concrete It acts as an engine of sustainable carbon sequestration that is stored after use until one day it may eventually be reused by future generations.
  • Carbon fiber which is no longer needed and disposed of can thus be reactivated by future generations without much effort, if necessary serve as a valuable carbon reserve, if for For example, if solar activity decreases over the centuries or millennia, carbon must be re-activated to heat the atmosphere by burning it to C0 2 , leaving carbon fiber carbon in a long-term closed recycling process that is easy and safe to handle.
  • the invention described here offers a controlled and controllable handling of carbon and oxygen. All previous processes for building materials currently produce long-term uncontrollable amounts of C0 2 , consume expensive electricity produced and bind oxygen. With the help of the present invention, these ratios are reversed all together.
  • the proposed process produces fully regenerative building material and regenerative electricity and provides control over the CO 2 concentration by reducing it, releasing vital oxygen.
  • the PAN fiber is guided in a transparent tube of, for example, glass, quartz glass or glass ceramic (2), which in the oxidation phase and the carbonation phase with different, likewise transparent gases (2a) in the oxidation phase (FIG ) and (2b) in the pyrolysis phase ( Figure 4).
  • a transparent tube of, for example, glass, quartz glass or glass ceramic (2) which in the oxidation phase and the carbonation phase with different, likewise transparent gases (2a) in the oxidation phase (FIG ) and (2b) in the pyrolysis phase ( Figure 4).
  • the fiber bundle In the oxidation phase in Fig. 3, the fiber bundle is in an oxygen-containing gas mixture (2a) and is heated up to about 300 ° C during this phase.
  • the glass tube (2) surrounding the fiber bundle is not exposed to critical temperatures which would necessitate cooling of the tubes since the melting temperature of glass is not reached.
  • FIG. 3 shows how the PAN fiber strand is first guided in the oxidation phase.
  • the guide rings (5) are kept at regular intervals in the oxidation tube by wires (6) made of temperature-stable material such as stainless steel, tungsten or molybdenum in the center.
  • the continuum around the PAN fiber strand consists of oxygen-containing gas (2a).
  • the rings are preferably made of temperature-stable, non-corrosive metal, tungsten or molybdenum.
  • the wires are passed through tubes (7) which pierce the walls of the cylindrical tubes (2) and (4) and the length of the wires (6) is electronically controlled via winding rollers (9) to keep the fiber strand in the focal line and by which gas (2a) can be replenished at the same time to replenish oxygen consumed by the oxidation (8a).
  • the carbon fiber to be carbonized or forming is located in a carbon fiber (1b) Nitrogen (2b) filled space to further oxidation and the burning of the material by further heating to 800 ° C and then up to 1800 ° or even 3000 ° C during the pyrolysis process in which the carbon chains (carbonization) takes place, which is responsible for the later high tensile stability and stiffness of the carbon fiber to prevent.
  • the transparent glass tube (2) - carbonization or pyrolysis tube - would melt at the high temperatures required for pyrolysis because the gas (2b) also reaches temperatures which exceed the melting temperature of the tube (2) - on the other hand this tube is necessary, in order to form a closed continuum of nitrogen (2b) or another transparent oxygen-free gas around the fiber strand and at the same time to pass the concentrated light onto the fiber strand without much optical resistance through the wall of the glass tube to the fiber strand for its heating the tube is cooled from the outside by a transparent gas, for example air, or a suitable transparent liquid, for example, temperature-resistant silicone oil (3b).
  • a transparent gas for example air
  • a suitable transparent liquid for example, temperature-resistant silicone oil (3b).
  • the inner glass bulb is surrounded by a second enveloping glass bulb (3), so that this cooling gas or the cooling liquid (3b) selectively dissipates such a heat measure that kept the inner glass tube (2) always at a temperature below its melting point becomes.
  • this heated cooling gas or the heated cooling liquid (3b) in turn uses a heat exchanger to its or their cooling with a heat exchanger, electricity can be generated from the thus dissipated heat with conventional power plant technology with steam turbine-driven generators. The heat generated during the carbonization is thus used simultaneously to generate electricity.
  • the fiber strand is conducted in the pyrolysis phase.
  • the guide rings (5) are kept at regular intervals in the pyrolysis tube (2) by wires (6) also made of extremely temperature-stable material such as tungsten or molybdenum in the center.
  • the continuum around the PAN fiber strand in the pyrolysis phase consists of a gas which does not contain any oxygen, for example nitrogen (2b).
  • the rings are preferably also made of temperature-stable tungsten or molybdenum, which withstand temperatures which are above the pyrolysis temperature.
  • the wires are passed through tubes (7), which pierce the walls of the cylindrical tubes (2), (3) and (4) and the length of the wires (6) via winding rollers (9) adjusted electronically controlled.
  • nitrogen (8b) is blown through the tubes (7), which at the outlet of the carbon fiber strand is removed from the carbonation tubes and cleaned in order to be reused.
  • FIG. 7 shows a cross section through the carbonation tube in the region of the pyrolysis heating zone in Figure 8.
  • Fig. 8 shows a section through the entire carbonation route, starting with the oxidation phase (11), in which the required heat energy is supplied either by means of parabolic mirrors or via electric heating for the oxidation of the PAN fiber, via the pyrolysis Heating phase (12) by means of parabolic mirror heating and holding phase (13) with internally mirrored tube, up to the subsequent cooling phase (14), as well as the parabolic mirror in the zones (11) and (12).
  • the pyrolysis zone (12) is adjoined by a holding zone (13), by means of which the pyrolysis time is set in relation to each other by a variable length and depending on the pyrolysis temperature and feed rate of the fiber. Since the fiber itself emits radiation in the visible light range at the pyrolysis temperature, this reverberation is prevented by a full pre-reflection (9a) on the inner wall of the pyrolysis tube in the holding phase subsequent to the heating phase (FIG. 6), so that the radiation energy as possible experiences no losses and the pyrolysis temperature can be maintained over a further distance without reheating by the parabolic mirror.
  • the need for the parabolic mirror is omitted in this route, it is only the inner mirroring (9a) of the inner or alternatively the outer tube needed.
  • a vacuum (3a) also provides the necessary insulation against heat loss in the holding zone.
  • the cooling phase follows (14), in which you can work with a single-walled or double-walled tube.
  • the cooling takes place by convection of a cooling gas in the inner tube, via the additional convection of a liquid or a gas within a second tube layer, which does not necessarily have to be transparent, but can be light-absorbing, or by radiation through a transparent tube system onto a black body, which serves as a heater in a heat exchanger system, that is, for example, cooled by water, the heated water is also used for power generation.
  • the described arrangement first of all means a factor of 3 in the increase in efficiency compared to a method in which the power was first generated by conventional CSP parabolic mirror technology to serve for the carbonization of the fiber, since the efficiency of power generation by the associated heat loss can be a maximum of 35%.
  • the light is first converted to at least 45% in carburizing energy in the form of heat on the carbon fiber itself, the use of light is therefore almost twice as high as in the conventional method of primary power generation and there additional ca 30% of the total heat is converted into electricity energy, it can be assumed that the total efficiency of the light energy is 75%.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Textile Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Energy (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Sustainable Development (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Inorganic Fibers (AREA)

Abstract

L'invention concerne un procédé à haut rendement énergétique pour la production simultanée de fibres de carbone et d'électricité à l'aide de la lumière solaire concentrée pour produire de façon neutre en CO2 des matériaux stable en compression et en traction. Le rendement énergétique repose sur le principe consistant à chauffer la fibre de carbone à produire directement avec la lumière solaire concentrée, ce qui est rendu possible par le fait que la fibre de PAN d'origine fonce lors du processus d'oxydation et de pyrolyse et devient enfin un corps noir presque idéal. La chaleur ainsi générée est utilisée ensuite ou en même temps pour la production de matière de la fibre pour la production d'électricité, ce qui correspond au principe de couplage puissance-chaleur classique pour augmenter davantage le rendement, déjà majoré par ce processus, lors de la production de fibres de carbone et fournir de l'énergie sous la forme très valorisée d'électricité.
EP16702656.6A 2015-01-17 2016-01-18 Réacteur de carbonisation pour la production combinée de materiaux de construction et d'électricité à l'aide de la lumière solaire Withdrawn EP3245319A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE201520000375 DE202015000375U1 (de) 2015-01-17 2015-01-17 Carbonisierungsreaktor zur kombinierten Erzeugung von Konstruktionsmaterial und Strom mit Hilfe von Sonnenlicht
PCT/EP2016/000079 WO2016113140A1 (fr) 2015-01-17 2016-01-18 Réacteur de carbonisation pour la production combinée de materiaux de construction et d'électricité à l'aide de la lumière solaire

Publications (1)

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EP3245319A1 true EP3245319A1 (fr) 2017-11-22

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EP16702656.6A Withdrawn EP3245319A1 (fr) 2015-01-17 2016-01-18 Réacteur de carbonisation pour la production combinée de materiaux de construction et d'électricité à l'aide de la lumière solaire

Country Status (14)

Country Link
US (1) US20190100858A1 (fr)
EP (1) EP3245319A1 (fr)
KR (1) KR20170117082A (fr)
CN (1) CN107429435A (fr)
AU (1) AU2016208227A1 (fr)
CL (1) CL2017001845A1 (fr)
DE (1) DE202015000375U1 (fr)
IL (1) IL253534A0 (fr)
MA (1) MA40702B1 (fr)
MX (1) MX2017009301A (fr)
PE (1) PE20171262A1 (fr)
TN (1) TN2017000307A1 (fr)
WO (1) WO2016113140A1 (fr)
ZA (1) ZA201705502B (fr)

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Publication number Priority date Publication date Assignee Title
US9802862B2 (en) 2008-11-27 2017-10-31 Kolja Kuse CO2 emission-free construction material made of CO2
DE202016006700U1 (de) * 2016-11-01 2017-04-26 Kolja Kuse Carbonfaser
US20220307685A1 (en) * 2021-03-25 2022-09-29 Eric Jose Marruffo Soleric Process for Enhancing Steam and Super-heated Steam Production from Small Concentrated Solar Power and Renewable Energy.

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JPS54156821A (en) * 1978-05-25 1979-12-11 Toho Rayon Co Ltd Device for manufacturing graphite fiber
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DE202007015789U1 (de) 2007-11-13 2008-03-13 Kuse, Kolja Steinträger mit Vorspannung
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CN103591702A (zh) * 2013-10-28 2014-02-19 汪禹 碟式太阳炉

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CL2017001845A1 (es) 2018-05-11
WO2016113140A9 (fr) 2017-07-13
US20190100858A1 (en) 2019-04-04
AU2016208227A1 (en) 2017-09-07
ZA201705502B (en) 2019-11-27
WO2016113140A1 (fr) 2016-07-21
MX2017009301A (es) 2018-03-06
MA40702A1 (fr) 2017-10-31
CN107429435A (zh) 2017-12-01
MA40702B1 (fr) 2018-06-29
PE20171262A1 (es) 2017-08-31
TN2017000307A1 (en) 2019-01-16
IL253534A0 (en) 2017-09-28
KR20170117082A (ko) 2017-10-20
DE202015000375U1 (de) 2015-03-02

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