• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Mobile and autothermal pyrolyzer. The invention relates to a mobile and autothermal pyrolyzer comprising a vertical pyrolysis chamber where the reaction of the material to be pyrolyzed is carried out, characterized in that it comprises a shell of refractory material arranged concentrically and separated from the vertical pyrolysis chamber, defining between both a combustión chamber that provides heat to carry out pyrolysis without external input of thermal energy. (Machine-translation by Google Translate, not legally binding)
    公开号:ES2557492A1
    申请号:ES201431105
    申请日:2014-07-23
    公开日:2016-01-26
    发明作者:Antonio Morán Palao；José Guillermo ROSAS MAYORAL；Marta Elena SÁNCHEZ MORÁN；Jorge CARA JIMÉNEZ；Arturo MARTÍNEZ MARTÍNEZ；Óscar LÓPEZ VARELA
    申请人:Mecanotaf Sa；Mecanotaf S A；Universidad de Leon；
    IPC主号:
    专利说明:

    MOBILE AND SELF-THERMAL PELLIZER
    D E S C R I P C I O N
    5 OBJECT OF THE INVENTION
    The invention relates to a mobile and autothermal pyrolizer that allows pyrolization of biomass, mainly of lignocellulosic origin, without external input of thermal energy to carry out pyrolysis, which significantly reduces its operating costs
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    The object of the invention is a mobile and autothermal pyrolizer that does not require auxiliary installations for its operation and can work outdoors, in addition to being easily transported to different locations without the need to build structures or provide auxiliary facilities in the new Location.
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    The flexibility of the system to be repositioned allows the reactor to be taken to areas close to the location of the raw material, thus reducing the transport costs that are significant when it comes to low density materials.
    20 Another advantage of the invention is the ease of access to parts of the equipment that require cleaning to maintain optimal operation.
    BACKGROUND OF THE INVENTION
    25 Pyrolysis is a thermal process for the decomposition of the raw material to be treated, which can be biomass, which is heated in the absence of air, oxygen or any reducing agent. However, there are systems that allow the combustion of a small fraction of the biomass to give thermal energy to the system. The products obtained by thermal decomposition of biomass are gases, liquids and solids.
    The production of biochar or charcoal (depending on its application) as carbonized material from pyrolysis, has been present throughout the history of mankind.
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    Traditional processes, using wells, mounds or furnaces, usually involve the direct combustion of a fraction of the biomass as a source of heat in the oven. Gases and liquids are often not collected with the resulting environmental and health problems to the people there! Work or live nearby.
    As for industrial processes, for example in furnaces, they use combustion of part of the material to be charred for heating. These ovens work in batches and are built on-site. Charging, charring and cooling cycles last from a few hours to 20 days in the case of Missouri type furnaces of around 165 m3 capacity.
    There is a wide variety of systems for pyrolysis with helical screws for transporting the material inside the reactor and especially in a horizontal position, such as those included in EP1405895A1. These systems can present jams especially if the particle size is not of the ideal dimensions. The pretreatment of the raw material to reduce its size, especially if small and homogeneous particles are sought, can increase operating costs. The particle size is also relevant when it comes to fluidized bed systems, such as that described in US7943014B2 since the fluidizing current must be able to move the material to be treated.
    The previous system has energy dependence to maintain pyrolysis conditions, requiring fossil fuels.
    In US6048374 a self-thermal system for the pyrolysis of biomass is described. Said system is a vertical position reactor with several clearly differentiated sections. The material enters through the upper part and is led to a narrowing of the reactor by means of a conical helical screw. In the narrow part of the reactor the pyrolysis or gasification is carried out. Said narrowing zone is heated by direct contact with the combustion chamber that surrounds it. The carbonized material is evacuated from the reaction zone and burned in the combustion chamber to energize the system.
    In EP1970424 an autothermal apparatus and a method for the pyrolysis of biomass are described, in which the combustion of the gases is carried out in a chamber of
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    External combustion and combustion gases are used for indirect heating of the material inside the reactor.
    Among autothermal and portable systems, US7943014B2 discloses a mobile pyrolysis system for agricultural biological waste. This system seeks the maximization of liquids and works with a fluidized bed. The thermal energy of the process is provided by the combustion of non-condensable gases that are produced during pyrolysis.
    Being a fluidized bed system, it is necessary to carry out a strict control of the fed particle size, the residence time of the material, the cleaning of the gas-steam current to separate the desired liquid from the gas and the suspended fines .
    The mobile and autothermal pyrolizer of the present invention solves all the above drawbacks by means of a simple, robust and thermally self-sufficient design. The design and simplicity of the system allow the reduction of operating costs by accepting materials almost without pretreatment, and it is easy to transfer it to different locations without the need for auxiliary facilities for its operation.
    DESCRIPTION OF THE INVENTION
    The present invention relates to a mobile and autothermal pyrolizer comprising a vertical pyrolysis chamber where the reaction of the material to be pyrolized occurs and a casing of refractory material arranged concentrically and separated from the vertical pyrolysis chamber, defining between them a combustion chamber that provides the heat to carry out the pyrolysis due to the heat transmitted by the walls of the vertical pyrolysis chamber to the material to be pyrolyzed disposed therein.
    The vertical pyrolysis chamber has no air inlet so that gasification or combustion does not occur. In the pyrolizer, the material already carbonized at the exit of the vertical pyrolysis chamber is not used for the contribution of energy but rather the energy is obtained from the burning of condensable gases and vapors in the combustion chamber, thus conserving! the residue already carbonized for other uses.
    The pyrolizer comprises means for feeding the material to be pyrolyzed for introduction into the vertical pyrolysis chamber and airtight means for discharging the
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    Carbonized or already pyrolized material that is transferred to a closed air-free container where the already carbonized material is arranged for cooling, avoiding its self-ignition.
    The vertical pyrolysis chamber comprises exit holes of the pyrolysis gases, preferably two diametrically opposed holes arranged in its upper part and tubes fixed to an external wall of the vertical pyrolysis chamber communicated with the exit holes of the exhaust gases. pyrolysis, where the tubes are open at its lower end to direct the pyrolysis gases to the lower part of the combustion chamber where they are mixed with air from an air inlet and are burned providing heat to the system.
    The pyrolizer comprises a gas burner that allows the initial heating of the vertical pyrolysis chamber to be carried out in addition to producing the first pyrolysis gases and achieving combustion. Once this point is reached, the process operates autothermally, that is, external gas is no longer necessary.
    The pyrolizer comprises a centrifugal fan that allows to extract the hot gases from the combustion of the combustion chamber and direct them to an outlet chimney.
    The combustion gases on their way to the exit chimney are used to preheat the material to be pyrolyzed before being fed to the pyrolysis vertical chamber through a conduit that surrounds the feeding tube.
    The pyrolizer comprises temperature probes that allow temperature monitoring in different parts thereof, in addition to an automatic control system to vary the feed times of material to be pyrolyzed and extraction of already carbonized material.
    BRIEF DESCRIPTION OF THE DRAWINGS
    Figure 1 shows an elevational view of the mobile and autothermal pyrolizer of the present invention.
    Figure 2 shows a plan view of the vertical pyrolysis chamber of the mobile and autothermal pyrolizer of the present invention.
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    PREFERRED EMBODIMENT OF THE INVENTION
    The mobile and autothermal pyrolizer of the present invention is described in detail below.
    The pyrolizer comprises a vertical chamber (1) of pyrolysis of variable internal section, preferably a truncated cone to prevent jams, where the reaction is produced, which is fed by its upper part by means of feeding means (12, 13, 2, 21).
    These feeding means (12, 13, 2, 21) comprise a bucket elevator (12) that receives the material to be pyrolyzed, preferably biomass, from a conveyor belt (13) that also functions as a deposit of material to be pyrolized. , and a feeding tube (2) comprising a first screw screw (21) that feeds the vertical chamber (1) of pyrolysis. The material to be pyrolyzed moves along the vertical chamber (1) of pyrolysis due to gravity.
    The pyrolizer also comprises airtight discharge means (3, 31) comprising a discharge tube (3) which in turn comprises a second screw screw (31), where the bottom of the pyrolysis vertical chamber (1) is It is connected to the second horizontal tube (3), where the second screw screw (31) removes the material already pyrolyzed or carbonized from inside the vertical chamber (1) of pyrolysis.
    Concentrically to the vertical pyrolysis chamber (1) and separated from it, the pyrolizer comprises a housing (5) of refractory material, preferably concrete, defining between the vertical pyrolysis chamber (1) and the material housing (5) a combustion chamber (6) that provides heat to carry out pyrolysis is refractory. The heat is transmitted through the walls of the vertical chamber (1) of pyrolysis to the material disposed inside. The combustion chamber (6) comprises an air inlet hole (22).
    The pyrolizer comprises a closed container (4) free of air where the already carbonized material is disposed at the outlet of the second screw screw (31) for cooling, while preventing its self-ignition. The closed container (4) comprises manual systems for the distribution of the already carbonized material inside, preferably internal blades operable by means of external cranks (not shown).
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    The vertical pyrolysis chamber (1) comprises pyrolysis gas outlet orifices, preferably two diametrically opposed holes arranged in its upper part and tubes (7) fixed to the external wall of the pyrolysis vertical chamber (1) communicated with the pyrolysis gas outlets, where the tubes are open at its lower end to direct the pyrolysis gases to the bottom of the combustion chamber (6) where they mix with the air and are burned giving heat to the system, as seen in Figure 2. These tubes (7) fixed to the outer wall of the pyrolysis vertical chamber (1) are kept at the same temperature as the combustion chamber (6) in order to Avoid condensation Enb the pyrolizer of the present invention, only the condensable gases and vapors are burned in the combustion chamber (6).
    The pyrolizer comprises a gas burner (8) that allows the initial heating of the vertical pyrolysis chamber (1) to be carried out, in addition to producing the first pyrolysis gases and achieving combustion. Once this point is reached, the process operates in an auto-thermal manner, that is, the external gas is no longer necessary, the gas burner (8) being deactivated.
    The pyrolizer comprises a centrifugal fan (9) that allows to extract hot gases from the combustion of the combustion chamber (6) and direct them to an outlet chimney (10).
    The combustion gases on their way to the outlet chimney (10) are used to preheat the material to be pyrolyzed before being fed to the pyrolysis vertical chamber (1) through a duct (23) arranged in the fan aspiration centrifuge (9) that previously surrounds the feeding tube (2).
    The pyrolizer comprises temperature probes (11) that allow temperature monitoring in different parts thereof, in addition to an automatic control system to vary the feed times of material to be pyrolyzed and extraction of already carbonized material.
    The pyrolizer also includes an integrated diesel electric generator. Alternatively, the pyrolizer comprises heat exchangers in the area of the vertical chamber (1) of pyrolysis and in the conduction of the already carbonized material through the discharge tube (3) to the closed container (4) where it is cooled.
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    The pyrolizer comprises a secondary burner (English term used to describe it afterburner) arranged at the exit of the outlet chimney (10) to control the pyrolysis gases in case they exceed the energy needs and maintain control over the air emissions.
    Said secondary burner (not shown) comprises a heat exchanger to take advantage of the combustion heat of the pyrolysis gases.
    EXAMPLE
    The data presented below are experimental results using as material to pyrolize residual biomass from the start of old or diseased vine plants with low grape production.
    One of the advantages of the mobile and autothermal pyrolizer of the present invention is that it can treat the material practically as it has been torn from the ground. The material does not require complicated pretreatments being heterogeneous in particle size, ranging from fine material to pieces of approximately 15 cm in length and up to 5 cm in diameter. The bulk density of the material was 256 kg / m3.
    As described, the equipment uses propane gas to reach the working temperature. To reach 790 ° C in the combustion chamber, starting the heating from a temperature of 17 ° C, 19.65 kg of propane gas and approximately 4 hours are required.
    The feed of the material to be pyrolyzed is started before reaching the target temperature in the combustion chamber. In this way the material starts thermal decomposition releasing gases that are burned in the combustion chamber. About 10 minutes after starting the material feed, the propane gas supply stops and from that moment the pyrolizer is working in autothermal mode.
    The combustion of pyrolysis gases is maintained by the high temperature in the combustion chamber and by the continuity in the thermal degradation of the material in the pyrolysis chamber, providing a constant flow of pyrolysis gas.
    The average temperature of the combustion chamber and the pyrolysis chamber is 753 ° C and 709 ° C respectively.
    An average flow of fed material of 55 kg / h was reached. This material flow will change depending on the type of material to be treated and its physical characteristics such as particle size and apparent density among others.
    Under the described working conditions the yield of the carbonized or biochar material is 26.67%.
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    The average temperature of combustion gases at the exit of the chimney is 312 ° C.
    权利要求:
    Claims (11)
    [1]
    R E I V I N D I C A C I O N E S
    1. - Mobile and autothermal pyrolyser comprising a vertical pyrolysis chamber (1) where the reaction of the material to be pyrolyzed occurs characterized in that it comprises a
    5 housing (5) of refractory material arranged concentrically and separated from the vertical chamber (1) of pyrolysis, defining between them a combustion chamber (6) that provides the heat to carry out the pyrolysis.
    [2]
    2. - Mobile and autothermal pyrolyser according to claim 1 characterized in that it comprises 10 feeding means (12, 13, 2, 21) of the material to be pyrolyzed for introduction into the
    vertical chamber (1) of pyrolysis.
    [3]
    3. - Mobile and autothermal pyrolizer according to claim 2 characterized in that the feeding means (12, 13, 2, 21) comprise a bucket elevator (12) that receives the
    15 material to be pyrolyzed from a conveyor belt (13), and a feed tube (2) comprising a first screw screw (21) that feeds the vertical chamber (1) of pyrolysis.
    [4]
    4. - Mobile and autothermal pyrolizer according to any of the preceding claims characterized in that it comprises airtight means of discharge (3, 31) of the material
    20 carbonized or already pyrolyzed and a closed container (4) in a vacuum atmosphere where the already carbonized material is disposed for cooling from airtight discharge means (3, 31).
    [5]
    5. - Mobile and autothermal pyrolizer according to any of the preceding claims 25 characterized in that the vertical pyrolysis chamber (1) comprises exit holes of
    pyrolysis gases and tubes (7) fixed to an external wall of the vertical pyrolysis chamber (1) communicated with the pyrolysis gas outlet holes, where the tubes (7) are open at their lower end where an air inlet hole (22) is found in the combustion chamber (6).
    30
    [6]
    6. - Mobile and autothermal pyrolizer according to any of the preceding claims characterized in that the vertical pyrolysis chamber (1) comprises a gas burner (8).
    [7]
    7. Mobile and autothermal pyrolizer according to any of the preceding claims characterized in that it comprises a centrifugal fan (9) that extracts hot gases from the combustion of the combustion chamber (6) and directs them to an outlet chimney (10) .
    5 8.- Mobile and autothermal pyrolyser according to revindication 7 characterized in that
    It comprises a conduit (23) arranged in the aspiration of the centrifugal fan (9) that previously surrounds the feeding tube (2) of the feeding means (12, 13, 2, 21) to preheat the material to be pyrolyzed before being fed to the vertical chamber (1) of pyrolysis.
    10
    [9]
    9. - Mobile and autothermal pyrolizer according to any of the preceding claims characterized in that it also comprises an integrated diesel electric generator.
    [10]
    10. - Mobile and autothermal pyrolizer according to any of claims 1 to 8
    15 characterized in that it comprises heat exchangers in the chamber area
    vertical (1) of pyrolysis and in the discharge tube (3) to the closed container (4).
    [11]
    11. - Mobile and autothermal pyrolizer according to claim 7 characterized in that
    It comprises a secondary burner arranged at the exit of the outlet chimney (10).
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    [12]
    12. - Mobile and autothermal pyrolizer according to claim 10 characterized in that the secondary burner comprises a heat exchanger.
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    同族专利:
    公开号 | 公开日
    ES2557492B1|2016-11-03|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    WO1999009115A1|1997-08-18|1999-02-25|Green Alex E S|A method and apparatus for gasifying or liquefying biomass|
    WO2006130977A1|2005-06-08|2006-12-14|The University Of Western Ontario|Apparatus and process for the pyrolysis of agricultural biomass|
    EP2351812A2|2008-10-16|2011-08-03|Rm Materiais Refratários Ltda.|Apparatus and process for thermal decomposition of any kind of organic material|
    CN101434846A|2008-12-15|2009-05-20|黄荣胜|Method and apparatus for biomass ion catalytic pyrolysis gasification|CN110375309A|2019-07-17|2019-10-25|梁慧|A kind of solid waste processing system with hazardous waste pretreatment process|
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