JP2019081849A - Carbonizing apparatus and carbonizing method - Google Patents

Carbonizing apparatus and carbonizing method Download PDF

Info

Publication number
JP2019081849A
JP2019081849A JP2017209897A JP2017209897A JP2019081849A JP 2019081849 A JP2019081849 A JP 2019081849A JP 2017209897 A JP2017209897 A JP 2017209897A JP 2017209897 A JP2017209897 A JP 2017209897A JP 2019081849 A JP2019081849 A JP 2019081849A
Authority
JP
Japan
Prior art keywords
furnace
carbonization
open
section
carbonizing
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.)
Granted
Application number
JP2017209897A
Other languages
Japanese (ja)
Other versions
JP7007158B2 (en
Inventor
伊藤 智章
Tomoaki Ito
智章 伊藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ONEWORLD CORP
Original Assignee
ONEWORLD CORP
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by ONEWORLD CORP filed Critical ONEWORLD CORP
Priority to JP2017209897A priority Critical patent/JP7007158B2/en
Publication of JP2019081849A publication Critical patent/JP2019081849A/en
Application granted granted Critical
Publication of JP7007158B2 publication Critical patent/JP7007158B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Coke Industry (AREA)

Abstract

To provide a carbonizing apparatus and a carbonizing method which prevent an explosion or ignition to a carbonized material in a high-temperature carbonizing furnace when opening an open/close door just after carbonizing.SOLUTION: A carbonizing apparatus of the present invention comprises: a carbonizing furnace 2 which comprises an open/close door 4 and carbonizes an object in a non-communicated state by closing the open/close door 4; and a preparatory furnace 3 which is switchable from a communicated state to a non-communicated state with the carbonizing furnace 2 by opening/closing the open/close door 4, and comprises a steam injection hole 31 for injecting steam in the non-communicated state. The steam injection hole is temporally injecting steam in the preparatory furnace 3 in the non-communicated state while the carbonizing furnace 2 is carbonizing the object. Thus, during carbonizing, temperature in the preparatory furnace 3 reasonably falls and steam is condensed, and oxygen concentration in the preparatory furnace 3 falls. Thereby, when opening the open/close door after carbonizing, an explosion or an ignition to residue of waste do not occur in the high-temperature carbonizing furnace.SELECTED DRAWING: Figure 1

Description

本発明は、高温になった炭化炉内の爆発又は炭化処理物への引火を防止することのできる炭化処理装置及び炭化処理方法に関する。   The present invention relates to a carbonization treatment apparatus and a carbonization treatment method capable of preventing explosion in a high temperature carbonization furnace or ignition of carbonization treatment products.

一般的に、廃棄物等の炭化処理は、廃棄物等の対象物に過熱水蒸気を噴射する等の高温の加熱処理を施すとともに、炭化炉内の空気を排出して炭化炉内を無酸素又は低酸素の状態にして行われる。そのため、炭化処理の直後に炭化炉の開閉扉が開けられると、炭化炉外の酸素が未だ高温の炭化炉内に一気に流入し、炭化炉内で爆発が起きたり、未だ高温の炭化処理物又はその残渣に引火したりするという問題があった。   In general, carbonization of wastes and the like is performed by performing high-temperature heat treatment such as injecting superheated steam onto a target object such as waste, discharging the air in the carbonization furnace to make the inside of the carbonization furnace oxygen-free or It is done in a state of hypoxia. Therefore, when the opening / closing door of the carbonization furnace is opened immediately after carbonization, oxygen outside the carbonization furnace flows into the carbonization furnace at a high temperature at a stroke, explosion occurs in the carbonization furnace, or the high temperature carbonized product or There was a problem that the residue was ignited.

従来、本願出願人により、有機性廃棄物を移送コンベアに載せ、複数の区画に仕切られた一連の炭化処理炉内を通過させながら、区画毎に設定された温度で前記有機性廃棄物を過熱水蒸気処理することにより、有機物の炭化処理を行う有機物の炭化処理装置が提供されている(特許文献1)。   Conventionally, the applicant of the present invention places organic waste on a transfer conveyor and passes it through a series of carbonization furnaces divided into a plurality of compartments while heating the organic waste at a temperature set for each compartment. The carbonization processing apparatus of the organic substance which carbonizes the organic substance is provided by carrying out steam processing (patent document 1).

また、水蒸気又は過熱水蒸気を熱処理器内に噴射することで炭化処理を行う炭化物の製造方法であって、炭化処理中に対象物たる有機物から揮発ガスや分解ガス等が発生しても、これらガス分が温度の下がった水蒸気の凝縮水に吸収されて排出されるため、これらガス分がそのまま外部へ放出されて引火爆発するのを防止することのできる炭化物の製造方法が開示されている。   Moreover, it is a manufacturing method of the carbide which performs carbonization processing by injecting steam or superheated steam into the heat treatment equipment, and even if volatilization gas, decomposition gas, etc. are generated from the organic substance which is an object during carbonization processing, these gases There is disclosed a method of producing a carbide capable of preventing the gas component from being discharged outside as it is and exploding as it is absorbed by the condensed water of the water vapor whose temperature has dropped and discharged.

特開2013−524539号JP 2013-524539 特開2013−64379号JP 2013-64379

しかしながら、特許文献1に記載の技術は、一連の炭化処理炉の最初の区画で炭化処理が終了した後、当該処理後の廃棄物が移送コンベアで次の区画へと搬送されるとともに、新たな廃棄物が外部から開閉扉を開けて最初の区画へと搬入される際、高温となった最初の区画に外部から一気に酸素が流入し、最初の区画内で爆発が起きたり、未だ高温である廃棄物の残渣に引火したりするという問題があった。   However, according to the technology described in Patent Document 1, after the carbonization treatment is completed in the first section of the series of carbonization treatment furnaces, the waste after the treatment is transported to the next section by the transfer conveyor, and When waste is opened to the first compartment by opening the door from the outside, oxygen rushes from the outside into the first compartment that has become hot, explosion occurs in the first compartment, or it is still hot There was a problem of igniting waste residue.

また、特許文献2に記載の技術は、前記ガス分による爆発又は引火を防止することができるものの、水蒸気の温度が低下して凝縮水となるまで待機せねばならず、直ぐには炭化処理物を取り出すことはできなかった。また、仮に炭化処理直後に熱処理器から炭化処理物を取り出すとしても、高温となった熱処理器の開閉扉を開けた際には、無酸素又は低酸素状態の熱処理器内に外部から一気に酸素が流入し、熱処理機内で爆発したり、炭化処理物の残渣に引火したりするというおそれがあった。   In addition, although the technology described in Patent Document 2 can prevent explosion or ignition due to the gas content, it is necessary to wait until the temperature of the steam drops and becomes condensed water, and the carbonized product is immediately I could not take it out. In addition, even if the carbonized product is taken out of the heat treatment apparatus immediately after carbonization, oxygen is immediately generated from the outside in the heat treatment apparatus in an anoxia or low oxygen state when the heat treatment apparatus opening door is opened. There was a risk that it would flow, explode in the heat treatment machine, or ignite the residue of the carbonized product.

また、前記最初の区画又は熱処理器内の温度が低下するのを待ってから開閉扉を開け、炭化処理物を取り出すことも可能ではあるが、その待機時間により炭化処理物の生産性が非効率となってしまう。特に、前記特許文献1の炭化処理装置のように、対象物たる廃棄物を一連の炭化炉内の複数の区画ごとに順々に搬送して炭化処理を行うような場合は、最初の区画の温度が低下するのを待ってから廃棄物を移送コンベアで次の区画へと搬送すると、その後の複数の区画で処理待ちが発生し、炭化処理物の生産性がより一層非効率になるという問題があった。   In addition, it is possible to open the open / close door after waiting for the temperature in the first section or the heat treatment unit to drop and take out the carbonized product, but the waiting time makes the productivity of the carbonized product inefficient. It becomes. In particular, as in the carbonization treatment apparatus of Patent Document 1, in the case where the object waste is sequentially conveyed by each of a plurality of sections in a series of carbonization furnaces to carry out a carbonization process, If wastes are transported to the next section by the transfer conveyor after waiting for the temperature to drop, there will be waiting for processing in multiple sections after that, and the productivity of carbonized products will become even more inefficient. was there.

そこで、本発明は、炭化処理の直後に開閉扉を開けても、高温になった炭化炉内の爆発又は炭化処理物への引火を防止することのできる炭化処理装置及び炭化処理方法を提供することを課題とした。   Therefore, the present invention provides a carbonization treatment apparatus and a carbonization treatment method capable of preventing explosion in a high temperature carbonization furnace or ignition of a carbonization treatment even if the open / close door is opened immediately after carbonization treatment. Was an issue.

上記課題を解決するために、本発明は次のように構成した。すなわち、本発明に係る炭化処理装置は、開閉扉を備え、当該開閉扉を閉じた密閉状態で対象物を炭化処理する炭化炉と、前記開閉扉を開閉することで前記炭化炉と連通可能又は密閉状態となり、当該密閉状態で水蒸気を噴射する水蒸気噴射孔を備えた予備炉とからなり、前記炭化炉で対象物を炭化処理中に、密閉状態の前記予備炉内に水蒸気を噴射して凝結させ、当該予備炉内の酸素濃度を低下させることを特徴としている。   In order to solve the above-mentioned subject, the present invention was constituted as follows. That is, the carbonization treatment apparatus according to the present invention includes an open / close door, and a carbonization furnace that carbonizes an object in a closed state with the open / close door closed, and can communicate with the carbonization furnace by opening or closing the open / close door The preliminary furnace is provided with a steam injection hole for injecting steam in a sealed state in the sealed state, and during the carbonization processing of the object in the carbonizing furnace, the steam is injected into the preliminary furnace in the sealed state to condense. To lower the oxygen concentration in the preliminary furnace.

また、炭化処理方法は、開閉扉を備え、当該開閉扉を閉じた密閉状態で対象物を炭化処理する炭化炉と、前記開閉扉を開閉することで前記炭化炉と連通可能又は密閉状態となり、当該密閉状態で水蒸気を噴射する水蒸気噴射孔を備えた予備炉とからなる炭化処理装置における炭化処理方法であって、前記炭化炉に対象物を搬入する工程と、前記開閉扉を閉じて炭化炉及び予備炉を密閉状態にし、当該炭化炉で対象物を炭化処理する工程と、前記炭化炉での炭化処理中に、前記予備炉内に水蒸気噴射孔から水蒸気を一時的に噴射する工程と、前記炭化炉での炭化処理に要する時間をかけて予備炉内を低温化させるとともに水蒸気を凝結させ、当該予備炉内の酸素濃度を低下させる工程と、炭化処理後に前記開閉扉を開け、酸素濃度が低下し、且つ、低温化した予備炉内と高温の炭化炉内とを連通させることで、高温の炭化炉内の温度を低下させる工程とを含むことを特徴としている。   In addition, the carbonization treatment method includes an open / close door, and a carbonization furnace that carbonizes an object in a closed state with the open / close door closed, and opens or closes the open / close door to allow communication with the carbonization furnace or to be closed. It is a carbonization processing method in a carbonization processing device which consists of a preliminary furnace provided with a steam injection hole which injects steam in the said sealed state, and the process of carrying in a target object to the carbonization furnace, closing the opening-and-closing door, and a carbonization furnace And setting the preliminary furnace in a closed state, carbonizing the object in the carbonizing furnace, and temporarily injecting steam from the steam injection holes into the preliminary furnace during carbonization in the carbonizing furnace; The time required for carbonization in the carbonization furnace is lowered, the temperature in the preliminary furnace is lowered and the water vapor is condensed to reduce the oxygen concentration in the preliminary furnace, and the open / close door is opened after the carbonization treatment. Decrease, and By communicating the low temperature of the pre-furnace and hot carbonization furnace is characterized by comprising the step of reducing the hot temperature of carbonization furnace.

また、炭化処理装置は、複数種類の油分が含有された廃棄物の原料を、開閉扉で開閉可能に区切られた複数の区画からなる一連の炭化炉内に通過させ、当該複数の区画ごとに異なる温度で過熱水蒸気処理をして炭化処理物を得る炭化処理装置であって、前記一連の炭化炉の最初の区画よりも前に、開閉扉で開閉可能に区切られた予備区画を設けてなり、当該予備区画は、密閉状態で水蒸気を噴射する水蒸気噴射孔を備え、前記炭化炉で廃棄物を炭化処理中に水蒸気を噴射して凝結させ、当該予備炉内の酸素濃度を低下させることを特徴としている。   In addition, the carbonization treatment apparatus passes a raw material of waste containing a plurality of types of oil components into a series of carbonizing furnaces composed of a plurality of sections which are partitioned openably and closably by an open / close door, and for each of the plurality of sections A carbonizing apparatus for obtaining a carbonized product by superheated steam processing at different temperatures, wherein a spare section partitioned openable and closable by an opening and closing door is provided prior to the first section of the series of carbonizing furnaces. The preliminary section includes a steam injection hole for injecting steam in a closed state, and the waste is sprayed and condensed during the carbonization treatment of the waste in the carbonizing furnace to reduce the oxygen concentration in the preliminary furnace. It is characterized.

さらに、炭化処理方法は、複数種類の油分が含有された廃棄物の原料を、開閉扉で開閉可能に区切られた複数の区画からなる一連の炭化炉内に通過させ、当該複数の区画ごとに異なる温度で過熱水蒸気処理をして炭化処理物を得る炭化処理装置であって、前記一連の炭化炉の最初の区画よりも前に予備区画を設け、当該予備区画が開閉扉を閉じた密閉状態で水蒸気を噴射する水蒸気噴射孔を備えてなる炭化処理装置における炭化処理方法であって、前記予備区画の炭化炉端部側から廃棄物を搬入し、前記最初の区画へと搬送する工程と、前記開閉扉を閉じて最初の区画及び予備区画を密閉状態にし、当該最初の区画で廃棄物に炭化処理をする工程と、前記最初の区画での炭化処理中に、前記予備区画内に水蒸気噴射孔から水蒸気を一時的に噴射する工程と、前記最初の区画での炭化処理に要する時間をかけて、予備区画内の低温化させるとともに水蒸気を凝結させ、当該予備区画内の酸素濃度を低下させる工程と、炭化処理後に前記開閉扉を開け、酸素濃度が低下し、且つ、低温化した予備区画内と高温の最初の区画内とを連通させることで、高温の最初の区画内の温度を低下させる工程と、前記最初の区画で炭化処理をした廃棄物を、異なる温度での炭化処理のために次の区画へと搬送する工程とを含むことを特徴としている。   Furthermore, in the carbonization treatment method, a raw material of waste containing a plurality of types of oil components is passed through a series of carbonization furnaces composed of a plurality of sections which can be opened and closed by an open / close door, and for each of the plurality of sections A carbonization treatment apparatus for obtaining a carbonized product by superheated steam treatment at different temperatures, wherein a preliminary section is provided prior to the first section of the series of carbonizing furnaces, and the preliminary section is in a closed state with the open / close door closed. A carbonization treatment method in the carbonization treatment apparatus comprising the steam injection holes for injecting the steam, wherein waste is carried in from the carbonization furnace end side of the preliminary section, and transported to the first section; The opening and closing door is closed to seal the first compartment and the reserve compartment, and the waste material is carbonized in the first compartment, and the steam injection holes in the reserve compartment during the carbonization treatment in the first compartment Temporarily blow water vapor from And cooling the temperature in the preparatory compartment and condensing water vapor to reduce the concentration of oxygen in the preparatory compartment over the time required for the carbonization in the first compartment, and the opening and closing after the carbonization. Lowering the temperature in the high temperature initial compartment by opening the door, communicating the low temperature oxygen concentration and communicating the low temperature preliminary compartment with the high temperature initial compartment; Transporting the carbonized waste material to the next section for carbonization treatment at different temperatures.

本発明に係る炭化処理装置及び炭化処理方法によれば、前記炭化炉又は最初の区画に開閉扉を介して連通可能に前記予備炉又は予備区画を設け、炭化炉又は最初の区画で炭化処理中に予備炉又は予備区画に一時的に水蒸気を噴射することにより、炭化炉又は最初の区画で炭化処理をしている間に、予備炉又は予備区画の温度が自然に低下するとともに前記水蒸気が凝結し、予備炉又は予備区画内の温度を低下させ、且つ、酸素濃度を低下させることができる。これにより、前記炭化炉又は最初の区画での炭化処理直後に開閉扉を開けても、未だ高温の炭化炉又は最初の区画内に酸素が一気に流入することがなく、また、炭化炉又は最初の区画内の温度が低下することから、炭化炉又は最初の区画での爆発又は引火を防止することができる。   According to the carbonization treatment apparatus and the carbonization treatment method according to the present invention, the preliminary furnace or the preliminary section is provided in the carbonization furnace or the first section so as to be in communication with the first section via the opening and closing door. By temporarily injecting steam into the pre-furnace or pre-compartment, the temperature of the pre-furnace or pre-compartment naturally decreases while the carbonization furnace or the first section is carbonized, and the steam is condensed. Can reduce the temperature in the preheater or the precompartment and reduce the oxygen concentration. As a result, even if the open / close door is opened immediately after carbonization in the carbonization furnace or the first section, oxygen does not flow into the carbonization furnace or the first section which is still high in temperature, and the carbonization furnace or the first Since the temperature in the compartment is lowered, explosion or ignition in the carbonization furnace or the first compartment can be prevented.

また、炭化処理直後であっても炭化炉又は最初の区画の開閉扉を開けることができるので、前記のように炭化炉又は最初の区画から炭化処理物を取り出したり、次の区画へ搬送したりするために待機する必要がなく、スムーズに炭化処理を行えることから炭化処理物の生産性を向上させることができる。   In addition, since it is possible to open the opening / closing door of the carbonization furnace or the first section even immediately after the carbonization process, as described above, the carbonized product is taken out of the carbonization furnace or the first section or transported to the next section There is no need to stand by to perform the carbonization process smoothly, and the productivity of the carbonized product can be improved.

本発明に係る炭化処理装置の構造を示す概略図である。It is the schematic which shows the structure of the carbonization treatment apparatus which concerns on this invention. 他の実施例の炭化処理装置の構造を示す概略図である。It is the schematic which shows the structure of the carbonization treatment apparatus of another Example.

以下、図面に基づいて本発明を具体的に説明する。まず、図1は、本発明に係る炭化処理装置1の構成を示す概略図である。炭化処理装置1は、基本的には、炭化炉2、予備炉3及びその間の開閉扉4とから構成されている。   Hereinafter, the present invention will be specifically described based on the drawings. First, FIG. 1 is a schematic view showing the configuration of a carbonization treatment apparatus 1 according to the present invention. The carbonization treatment apparatus 1 basically includes a carbonization furnace 2, a preliminary furnace 3, and an open / close door 4 therebetween.

炭化炉2は、水蒸気又は過熱水蒸気を噴射する水蒸気噴射孔21を備え、ボイラ22から過熱水蒸気発生手段23を介して水蒸気又は過熱水蒸気を水蒸気噴射孔21から噴射し、廃棄物Xに対して水蒸気又は過熱水蒸気処理を施す。また、炭化炉2は、前記開閉扉4を設けた側面に連通口24を開口させ、その対向する側面位置に有機性の廃棄物Xを搬入出する搬入出口25が設けられている。また、当該搬入出口25には、開閉可能な扉26が設置されている。当該開閉扉4及び扉26は、炭化炉2の側面に沿って上下に昇降させることによって開閉するように構成されている。   The carbonization furnace 2 is provided with a steam injection hole 21 for injecting steam or superheated steam, and steam or superheated steam is injected from the steam injection hole 21 from the boiler 22 via the superheated steam generating means 23, Or apply superheated steam treatment. Moreover, the carbonization furnace 2 opens the communication port 24 in the side surface which provided the said opening / closing door 4, and the loading / unloading port 25 which carries in / out the organic waste X is provided in the side position which opposes. Further, a door 26 which can be opened and closed is installed at the loading / unloading port 25. The open / close door 4 and the door 26 are configured to open and close by moving up and down along the side surface of the carbonization furnace 2.

過熱水蒸気発生手段23は、当該ボイラ23より供給された水蒸気から過熱水蒸気を発生させる誘導加熱式の過熱水蒸気発生装置などであって、過熱水蒸気を発生させることができればこれに限定されるものではない。過熱水蒸気発生手段23で発生させる過熱水蒸気の温度は、廃棄物Xを十分に炭化させるには150℃以上であるのが好ましく、さらに、廃棄物Xに含まれるごみの種類により、エネルギーコストを抑制しつつ炭化処理を十分に行うには、60℃〜1300℃とするのが好ましい。   The superheated steam generating means 23 is, for example, an induction heating type superheated steam generator that generates superheated steam from steam supplied from the boiler 23, and is not limited to this as long as it can generate superheated steam. . The temperature of the superheated steam generated by the superheated steam generating means 23 is preferably 150 ° C. or more in order to sufficiently carbonize the waste X. Furthermore, the type of waste contained in the waste X suppresses the energy cost In order to carry out the carbonization treatment sufficiently, it is preferable to set the temperature to 60 ° C. to 1300 ° C.

予備炉3は、水蒸気を噴射する水蒸気噴射孔31を備え、ボイラ32で生成した水蒸気を予備炉3内に噴射可能に構成されている。また、予備炉3の前記炭化炉2と対向する面には、連通口33が設けられており、前記炭化炉2の連通口24との間に開閉扉4が設置されている。また、予備炉3は、前記噴射した水蒸気が凝結した水を排出する排出口34が下方に形成されている。   The preliminary furnace 3 includes steam injection holes 31 for injecting steam, and is configured to be capable of injecting the steam generated by the boiler 32 into the preliminary furnace 3. Further, a communication port 33 is provided on the surface of the preliminary furnace 3 facing the carbonization furnace 2, and an open / close door 4 is provided between the communication port 24 and the carbonization furnace 2. Further, the preliminary furnace 3 is formed at the lower side with a discharge port 34 for discharging the water to which the jetted water vapor has condensed.

予備炉3は、前記水蒸気噴射孔31から水蒸気を一時的に噴射させ、予備炉3内の空気を排除して予備炉3内の水蒸気が占める割合を増加させることにより、これら水蒸気が時間を経て予備炉3内の温度が自然に低下して水滴となるに伴い、予備炉3内の酸素濃度を低下させることができる。   The preliminary furnace 3 temporarily injects steam from the steam injection holes 31 and removes the air in the preliminary furnace 3 to increase the ratio of the steam in the preliminary furnace 3 so that these steams pass time. As the temperature in the preliminary furnace 3 naturally drops to become water droplets, the oxygen concentration in the preliminary furnace 3 can be reduced.

開閉扉4は、前記の通り、炭化炉2と予備炉3の間に設けられており、これら側面に沿って上方へスライドさせることで炭化炉2と予備炉3を連通させる。一方、炭化炉2で炭化処理を施す際には、これら側面に沿って下方へスライドさせることで炭化炉2と予備炉3を密閉させるように設置されている。なお、当該開閉扉4は、本実施例では、上下への昇降するように構成したが、炭化炉2と予備炉3を連通させ、且つ、密閉させるように構成できれば、どのような開閉扉4の態様であってもよい。   As described above, the open / close door 4 is provided between the carbonization furnace 2 and the preliminary furnace 3, and is made to communicate with the carbonization furnace 2 and the preliminary furnace 3 by sliding it upward along these side surfaces. On the other hand, when the carbonization treatment is performed in the carbonization furnace 2, the carbonization furnace 2 and the preliminary furnace 3 are sealed by sliding downward along the side surfaces. Although the open / close door 4 is configured to move up and down in the present embodiment, any open / close door 4 can be configured as long as the carbonization furnace 2 and the auxiliary furnace 3 can be communicated and sealed. It may be an aspect of

また、図示はしないが、本実施例の炭化処理装置1には、前記構成要素を操作制御する操作制御手段や前記炭化炉2及び予備炉3内の温度を検知して前記操作制御手段に送信する温度検知手段が設けられている。また、炭化炉2には、炭化処理により排出される廃棄液等を排出するための排出口が設けられている。   Further, although not shown, the carbonization treatment apparatus 1 of the present embodiment detects the temperature in the operation control means for controlling the operation of the component and the temperature in the carbonization furnace 2 and the spare furnace 3 and transmits it to the operation control means. Temperature detection means is provided. Further, the carbonization furnace 2 is provided with a discharge port for discharging waste liquid and the like discharged by the carbonization treatment.

このように炭化炉2に予備炉3を連通可能に併設し、予備炉3に水蒸気を噴射可能に構成した炭化処理装置1によれば、炭化炉2での炭化処理中に、予備炉3に一時的に水蒸気を噴射し、炭化炉2での炭化処理が終了するまでの時間を掛けて予備炉3内の温度を自然に低下させることにより、前記水蒸気が凝結するとともに予備炉3内の酸素濃度も低下する。そして、前記開閉扉4を上方へスライドさせて開けることにより、炭化炉2の温度も低下し、また、予備炉3内の酸素濃度が低下しているため、炭化炉2内での爆発や廃棄物Xの残渣への引火を防止することができる。   As described above, according to the carbonization treatment apparatus 1 in which the preliminary furnace 3 is communicatively connected to the carbonization furnace 2 and the steam can be jetted to the preliminary furnace 3, the preliminary furnace 3 can be By temporarily injecting steam and taking time to complete the carbonization treatment in the carbonization furnace 2 to naturally lower the temperature in the preliminary furnace 3, the steam condenses and oxygen in the preliminary furnace 3 Concentration also decreases. Then, by sliding the open / close door 4 upward, the temperature of the carbonization furnace 2 is also lowered, and since the oxygen concentration in the preliminary furnace 3 is lowered, explosion and disposal in the carbonization furnace 2 are caused. It is possible to prevent the ignition of the residue of substance X.

このように構成した炭化処理装置1における炭化処理の手順について、以下に説明する。   The procedure of the carbonization process in the carbonization treatment apparatus 1 configured as described above will be described below.

まず、前記炭化炉2の扉26を上方へスライドさせて搬入出口25を開き、当該搬入出口25から炭化炉2内に炭化処理の対象物である有機性の廃棄物Xを搬入する。   First, the door 26 of the carbonizing furnace 2 is slid upward to open the loading / unloading port 25, and the organic waste X to be carbonized is loaded into the carbonizing furnace 2 from the loading / unloading port 25.

次に、炭化炉2の前記扉26と開閉扉4を下方へスライドさせて閉じ、炭化炉2及び予備炉3を密閉状態にする。その後、炭化炉2内に所定の温度、例えば、60℃〜1300℃の水蒸気又は過熱水蒸気を水蒸気噴射孔21から噴射し、所定の時間間隔、例えば、数十分〜数時間にわたって廃棄物Xに対して炭化処理を施す。   Next, the door 26 and the open / close door 4 of the carbonization furnace 2 are slid downward and closed, and the carbonization furnace 2 and the preliminary furnace 3 are sealed. Thereafter, steam or superheated steam at a predetermined temperature, for example, 60 ° C. to 1300 ° C., is injected from the steam injection holes 21 into the carbonization furnace 2, and waste X is applied for a predetermined time interval, for example, several tens minutes to several hours. Apply carbonization treatment.

ここで、前記炭化処理を開始した段階で、前記予備炉3の水蒸気噴射孔31から水蒸気を一時的に噴射し、予備炉3内の空気を排除させ、予備炉3内に水蒸気が満たされるようにする。このように水蒸気で満たされた予備炉3内は、前記炭化炉2で炭化処理をしている間に、その内部の温度が低下し、水蒸気が凝結していく。それに伴い、予備炉3内の酸素濃度も低下していく。   Here, at the stage where the carbonization treatment is started, steam is temporarily injected from the steam injection holes 31 of the preliminary furnace 3 so that air in the preliminary furnace 3 is eliminated, and the preliminary furnace 3 is filled with steam. Make it As described above, while the inside of the preliminary furnace 3 filled with water vapor is carbonized in the carbonization furnace 2, the temperature of the inside decreases and the water vapor condenses. Along with that, the oxygen concentration in the preliminary furnace 3 also decreases.

そして、炭化炉2での炭化処理が終了する頃には、予備炉3内の温度が常温程度〜約60℃にまで低下しており、且つ、予備炉3内の酸素濃度が低い状態になっている。この状態で開閉扉4を開け、炭化炉2と予備炉3を連通させると、炭化炉2の温度も低下し、また、酸素濃度も低いので炭化処理の直後であっても炭化炉2で爆発や廃棄物Xの残渣への引火が起こらないようにすることができる。   Then, by the time the carbonization treatment in the carbonization furnace 2 is completed, the temperature in the preliminary furnace 3 is lowered to about normal temperature to about 60 ° C., and the oxygen concentration in the preliminary furnace 3 is low. ing. If the open / close door 4 is opened in this state and the carbonization furnace 2 and the preliminary furnace 3 are communicated, the temperature of the carbonization furnace 2 also decreases, and since the oxygen concentration is also low, explosion occurs in the carbonization furnace 2 even immediately after carbonization treatment And waste X residue can be prevented from igniting.

最後に、前記扉26を上方にスライドさせて開け、搬入出口25から炭化炉2内の炭化した廃棄物X、すなわち炭化処理物を取り出す。   Finally, the door 26 is slid upward and opened, and the carbonized waste X in the carbonization furnace 2, ie, the carbonized product, is taken out from the loading / unloading port 25.

このように、本実施例の炭化処理装置及び前記工程によれば、前記の通り、炭化処理後の炭化炉2での爆発等を防止することができ、また、炭化処理直後であっても炭化処理物を取り出すことができることから、次の廃棄物Xに対して直ぐに炭化処理を施すことができ、炭化処理物の生産性を向上させることができる。   Thus, according to the carbonization treatment apparatus of the present embodiment and the above steps, as described above, explosion and the like in the carbonization furnace 2 after carbonization treatment can be prevented, and carbonization treatment even immediately after carbonization treatment Since the treated material can be taken out, the next waste material X can be carbonized immediately, and the productivity of the carbonized material can be improved.

次に、第二実施例の炭化処理装置1について、図2を用いて具体的に説明する。   Next, the carbonization treatment apparatus 1 of the second embodiment will be specifically described with reference to FIG.

本実施例に係る炭化処理装置1は、基本的には、区画A乃至区画Gごとに区切られた一連の炭化炉2と、一連の炭化炉2の前に設けられた予備区画3と、各区画ごとに仕切るための開閉扉4と、有機性の廃棄物Xを載せてこれら区画内の内側を搬送する搬送手段5とから構成されている。なお、これら構成要素を操作制御する操作制御手段と区画ごとの温度を検知して操作制御手段に送信する温度検知手段も設けられている。   The carbonization treatment apparatus 1 according to the present embodiment basically includes a series of carbonizing furnaces 2 divided into sections A to G, a preliminary section 3 provided in front of the series of carbonizing furnaces 2, and the like. It comprises an opening / closing door 4 for partitioning the compartments, and a transport means 5 for carrying the organic waste X and transporting the inside of the compartments. An operation control means for controlling the operation of these components and a temperature detection means for detecting the temperature of each section and transmitting the temperature to the operation control means are also provided.

一連の炭化炉2は、開閉扉4で区画ごとに仕切られており、本実施例では、区画A乃至区画Gの七つの区画に分割されている。当該各区画は、一連の炭化炉2の両端側と各区画間に設けられた開閉扉4を開閉することで炭化炉2内を連通させたり、夫々の区画を独立空間にしたりすることが可能となっている。   The series of carbonizing furnaces 2 is partitioned into sections by the open / close door 4 and, in this embodiment, is divided into seven sections of section A to section G. The respective compartments can communicate the inside of the carbonizing furnace 2 by opening and closing the open / close door 4 provided between both ends of the series of carbonizing furnaces 2 and between the respective compartments, or can make the respective compartments be independent spaces It has become.

このように分割された区画A乃至Gのうち、本実施例においては、最初の区画Aは、炭化炉2内に搬入された廃棄物Xをボイラ22から送られた水蒸気を水蒸気噴射孔31から噴射することで加熱し、その廃棄物Xを減容するための区画である。また、中間の区画B乃至Eは、区画ごとに夫々過熱水蒸気発生手段23を備えており、廃棄物Xに含有される油分の気化温度差に応じて所定の異なる温度、例えば、区画Aで150℃の温度の水蒸気、区画Bで300℃、区画Cで450℃、区画Dで600℃の温度の過熱水蒸気が水蒸気噴射孔31から供給されるようになっている。また、区画E、区画F及び最後の区画Gは、炭化処理物を炭化炉2から搬出する前に緩やかに冷却するための区画であって、区画Eには150℃程度の過熱水蒸気が供給され、区画Fには前記ボイラ22から水蒸気が供給され、当該区画Gには冷却用の送風機6が備えられている。なお、区画Eは、廃棄物Xの種類によっては、1300℃等の600℃以上の高温で過熱水蒸気処理を施し、区画F及び区画Gにおいて炭化処理物を冷却するようにしてもよい。   Among the divisions A to G divided in this way, in the present embodiment, the first division A receives the water vapor sent from the boiler 22 of the waste X carried into the carbonization furnace 2 from the water vapor injection holes 31 It is a section for heating by injecting and volume reduction of the waste X. Further, the intermediate sections B to E are provided with superheated steam generation means 23 for each section, and the predetermined different temperatures according to the vaporization temperature difference of the oil contained in the waste X, for example, 150 in the section A Water vapor at a temperature of ° C., superheated steam at a temperature of 300 ° C. in section B, 450 ° C. in section C, and 600 ° C. in section D is supplied from the steam injection holes 31. Section E, section F and the last section G are sections for gently cooling the carbonized product before taking it out of the carbonizing furnace 2, and the section E is supplied with superheated steam at about 150 ° C. Water vapor is supplied from the boiler 22 to the section F, and the section G is provided with a blower 6 for cooling. Depending on the type of waste X, the section E may be subjected to superheated steam treatment at a high temperature of 600 ° C. or higher such as 1300 ° C. to cool the carbonized product in the sections F and G.

予備区画3は、前記水蒸気噴射孔31から水蒸気を一時的に噴射させ、予備区画3内の空気を排除して予備区画3内の水蒸気が占める割合を増加させることにより、これら水蒸気が時間を経て予備区画3内の温度が自然に低下して水滴となるに伴い、予備区画3内の酸素濃度を低下させることができる。   The spare compartment 3 temporarily injects steam from the steam injection holes 31 and removes the air in the spare compartment 3 to increase the ratio of the steam in the spare compartment 3 so that the water vapor passes over time. The oxygen concentration in the reserve compartment 3 can be reduced as the temperature in the reserve compartment 3 naturally drops to become water droplets.

開閉扉4は、炭化炉2の各区画と予備区画の間に設けられており、上方へスライドさせることで各区画を連通させ、一方、炭化炉2の各区画で炭化処理を施す際には、下方へスライドさせることでこれら区画内を密閉させるように設置されている。なお、当該開閉扉4は、本実施例では、上下への昇降するように構成したが、各区画を連通させ、且つ、密閉させるように構成できれば、どのような開閉扉4の態様であってもよい。   The open / close door 4 is provided between each section of the carbonization furnace 2 and the spare section, and is made to communicate with each section by sliding upward, while when performing carbonization treatment in each section of the carbonization furnace 2 , It is installed to seal the inside of these compartments by sliding downward. In the present embodiment, the open / close door 4 is configured to move up and down in the vertical direction, but it is an aspect of any open / close door 4 as long as the sections can be communicated and sealed. It is also good.

前記搬送手段5は、移送コンベアであって、前記廃棄物Xを載置して前記予備区画3から炭化炉2の内側を前記区画A乃至区画Gの順で搬送する。なお、当該廃棄物Xは、容器7に収容された状態で搬送手段5に載置されている。また、搬送手段5は、廃棄物Xが各区画での処理を行うごとに作動され、例えば、ある廃棄物Xを区画Aから区画Bへ搬送すると、その区画Bで行われる過熱水蒸気処理の経過時間を待ってから、廃棄物Xを区画Cへと搬送する。このようにして、区画Aから区画Gまで順々に各区画で廃棄物Xに対して処理が施される。また、搬送手段3は、搬送経路に沿って区画ごとに複数のモーターが設置されており、操作制御手段からの指示に基づいて廃棄物Xを搬送する。   The transfer means 5 is a transfer conveyer, places the waste X, and transfers the inside of the carbonization furnace 2 from the reserve section 3 in the order of the sections A to G. In addition, the said waste X is mounted in the conveyance means 5 in the state accommodated in the container 7. FIG. Further, the transport means 5 is activated each time the waste X performs the treatment in each section, for example, when a certain waste X is transported from the section A to the section B, the progress of the superheated steam treatment performed in the section B After waiting for time, the waste X is transported to section C. In this way, waste X is treated in each of the compartments A to G in sequence. In addition, a plurality of motors are installed in each section along the transport path, and the transport unit 3 transports the waste X based on an instruction from the operation control unit.

このように構成された炭化処理装置1は、例えば、前記のように最初の区画Aの処理温度が150℃で、区画Bの処理温度が300℃とし、各区画での炭化処理後に区画A及び区画B間の開閉扉4を上方にスライドさせて開けると、高温の区間Bによって区間A内の温度も200℃以上となる。このような状態で、予備区画3と最初の区画Aの間の開閉扉4を開けると、前記の通り、予備区画3では温度の低下による水蒸気の凝結に伴って酸素濃度が低下していることから、最初の区画Aでは爆発が起こらず、また、区画Aでの処理後の廃棄物Xの残渣への引火も防止することができる。   The carbonization treatment apparatus 1 configured in this way has, for example, the treatment temperature of the first section A at 150 ° C. and the treatment temperature of the section B at 300 ° C. as described above, and after the carbonization treatment in each section When the open / close door 4 between the sections B is slid upward and opened, the temperature in the section A also becomes 200 ° C. or more due to the high-temperature section B. In such a state, when the open / close door 4 between the reserve compartment 3 and the first compartment A is opened, as described above, in the reserve compartment 3, the oxygen concentration is lowered along with the condensation of water vapor due to the temperature decrease. As a result, no explosion occurs in the first section A, and ignition of waste X after treatment in section A can also be prevented.

次に、第二実施例の炭化処理装置1における炭化処理の手順について、以下に説明する。   Next, the procedure of the carbonization process in the carbonization treatment apparatus 1 of the second embodiment will be described below.

まず、予備区画3の外側(図中左側)の搬送手段5に廃棄物Xを収容した容器7を載置し、搬送手段5を作動させて予備区画3の内側へと搬送する。そして、予備区画3の外側の搬送手段5にさらに廃棄物Xを収容した二番目の容器7を載置し、搬送手段5を作動させて予備区画3の内側へと搬送する。これに伴い、最初に載置した容器7は、最初の区画Aへと搬送される。   First, the container 7 containing the waste X is placed on the transfer means 5 outside the reserve section 3 (left side in the drawing), and the transfer means 5 is operated to transfer to the inside of the reserve section 3. Then, the second container 7 containing the waste X is placed on the transfer means 5 outside the reserve section 3, and the transfer means 5 is operated to transfer the waste X to the inside of the reserve section 3. Along with this, the container 7 placed first is transported to the first section A.

次に、予備区画3の外側の開閉扉4及び各区画間の開閉扉4を下方にスライドさせて閉じ、これら区画を密閉状態にした上で、最初の区画Aで、所定の温度且つ所定の時間間隔で、例えば150℃の温度で1時間30分にわたって最初に載置した容器7の廃棄物Xに炭化処理を施す。   Next, the open / close door 4 on the outer side of the reserve section 3 and the open / close door 4 between the sections are slid downward to make these sections sealed, and then in the first section A, the predetermined temperature and the predetermined At time intervals, waste X in container 7 initially placed at a temperature of, for example, 150 ° C. for one and a half hours is carbonized.

ここで、前記炭化処理を開始した段階で、前記予備区画3の水蒸気噴射孔31から水蒸気を一時的に噴射し、予備区画3内の空気を排除させ、予備区画3内に水蒸気が満たされるようにする。このように水蒸気で満たされた予備区画3内は、前記最初の区画Aで炭化処理をしている間に、その内部の温度が低下し、水蒸気が凝結していく。それに伴い、予備区画3内の酸素濃度も低下していく。   Here, when the carbonization process is started, water vapor is temporarily injected from the water vapor injection holes 31 of the reserve compartment 3 so that air in the reserve compartment 3 is eliminated, and the reserve compartment 3 is filled with water vapor. Make it As described above, in the preliminary section 3 filled with water vapor, while the carbonization treatment is performed in the first section A, the temperature of the inside decreases and the water vapor condenses. Along with that, the oxygen concentration in the reserve section 3 also decreases.

そして、最初の区画Aでの炭化処理が終了する頃には、予備区画3内の温度が常温程度〜約60℃にまで低下しており、且つ、予備区画3内の酸素濃度が低い状態になっている。この状態で開閉扉4を開け、最初の区画Aと予備区画3を連通させると、最初の区画Aの温度も低下し、また、酸素濃度も低いので炭化処理の直後であっても最初の区画Aで爆発や廃棄物Xの残渣への引火が起こらないようにすることができる。   Then, by the time the carbonization treatment in the first section A is completed, the temperature in the preliminary section 3 is lowered to about normal temperature to about 60 ° C., and the oxygen concentration in the preliminary section 3 is low. It has become. In this state, when the open / close door 4 is opened and the first compartment A and the reserve compartment 3 are communicated, the temperature of the first compartment A also decreases, and the oxygen concentration is also low. A can prevent explosion and ignition of waste X residue.

また、最初の区画Aで最初に載置した容器7の廃棄物Xの炭化処理中に、予備区画3の外側の搬送手段5に三番目の容器7を載置しておく。前記の通り、最初の区画Aで炭化処理が終了すると、開閉扉Aが開けられ、三番目の容器7が予備区画3へ、二番目の容器7が最初の区画Aへ、最初の容器7が区画Bへと夫々搬送される。そして、例えば、区画Bでは300℃の過熱水蒸気処理を、区画Aでは150℃の水蒸気処理を1時間30分間にわたって施し、当該炭化処理が開始されると、予備区画3では一時的に水蒸気が噴射され、前記の通り、前記区画A及び区画Bの炭化処理中に温度及び酸素濃度を低下させる。   In addition, while carbonizing the waste X of the container 7 placed first in the first section A, the third container 7 is placed on the transport means 5 outside the reserve section 3. As described above, when the carbonization process is completed in the first compartment A, the open / close door A is opened, the third container 7 into the reserve compartment 3, the second container 7 into the first compartment A, the first container 7 Each is transported to section B. Then, for example, superheated steam treatment at 300 ° C. in compartment B and steam treatment at 150 ° C. in compartment A for 1 hour and 30 minutes, and when the carbonization treatment is started, steam is temporarily injected in reserve compartment 3 And, as noted above, reduce the temperature and oxygen concentration during carbonization of compartments A and B.

ここで、三番目の容器7を予備区画3へと搬送するに際して、二番目の容器7が最初の区画Aへ、最初の容器7が区画Bへと夫々搬送され炭化処理が開始されても、三番目の容器7は、予備区画3の外側の搬送手段5で所定の時間、例えば、約20〜30分間に亘って待機させ、予備区画3内をカラの状態でその温度を水蒸気の噴射によって冷却させた後、予備区画3の外側(図中左側)の開閉扉4を開けて予備区画3内に搬送させることもできる。これは、前回の炭化処理後に、予備区画3及び最初の区画Aの間の開閉扉4を開けた際、最初の区画Aの温度は低下する一方で、予備区画3の温度が100℃以上に上昇した場合、予備区画3の外側の開閉扉4を開けると外側から酸素が一気に流れ込み、予備区画3で爆発や廃棄物Xへの引火が起きるおそれがあるためである。その後、予備区画3では、残りの約1時間〜1時間10分に亘って前記一時的な水蒸気の噴射ののち、前記の通り、区画A及び区画Bの炭化処理中に予備区画3の温度及び酸素濃度を低下させる。これにより、より安全に予備区画3の外側の開閉扉3を開けることができ、また、区画Aでの前記1時間30分間の炭化処理の直後に、予備区画3及び区画Aの間の開閉扉4を開けることもできる。   Here, when transporting the third container 7 to the reserve section 3, even if the second container 7 is transported to the first section A and the first container 7 to the section B and carbonization processing is started, The third container 7 is caused to stand by for a predetermined time, for example, about 20 to 30 minutes, by the transport means 5 outside the reserve compartment 3, and the temperature of the third compartment 7 is sprayed by After cooling, the open / close door 4 on the outside (left side in the drawing) of the reserve section 3 can be opened and transported into the reserve section 3. This is because, when the open / close door 4 between the reserve section 3 and the first section A is opened after the previous carbonization treatment, the temperature of the first section A decreases while the temperature of the reserve section 3 becomes 100 ° C. or more When it rises, if the open / close door 4 outside the reserve section 3 is opened, oxygen flows in from the outside at a stretch, and there is a possibility that explosion or ignition to the waste X may occur in the reserve section 3. Thereafter, in the reserve section 3, after the temporary steam injection for the remaining about 1 hour to 1 hour 10 minutes, as described above, the temperature of the reserve section 3 during the carbonization treatment of the sections A and B and Reduce the oxygen concentration. Thereby, the door 3 outside the reserve section 3 can be opened more safely, and immediately after the carbonization treatment for 1 hour 30 minutes in the section A, the door between the reserve section 3 and the section A You can also open 4.

このように、当該炭化処理装置1は、廃棄物Xが収容された容器7が列を為して順々に各区画へと搬送され、炭化炉2の区画A乃至区画Gで夫々所定の時間間隔で処理がなされるとともに、予備区画3では、当該時間間隔ごとに前記水蒸気の凝結によって酸素濃度を低下させる構成となっている。かかる構成により、前記所定の時間間隔で施される最初の区画Aでの炭化処理ごとに開閉扉4を開けても、最初の区画A内に酸素が一気に流入することがなく、また、最初の区画A内の温度が低下することから、所定の時間間隔ごとの処理において最初の区画Aでの爆発又は引火を防止することができる。   As described above, in the carbonization treatment apparatus 1, the containers 7 in which the wastes X are stored are sequentially transported to each section in a row, and each of the sections A to G of the carbonizing furnace 2 has a predetermined time. The treatment is performed at intervals, and in the reserve section 3, the oxygen concentration is reduced by condensation of the water vapor at each time interval. With such a configuration, even if the open / close door 4 is opened for each carbonization treatment in the first section A applied at the predetermined time interval, oxygen does not flow into the first section A at a stretch, and the first section Since the temperature in the compartment A decreases, it is possible to prevent the explosion or ignition in the first compartment A in the processing at predetermined time intervals.

また、炭化処理直後であっても予備区画3と最初の区画A間の開閉扉4を開けることができるので、廃棄物Xを収容した容器7を最初の区画Aから次の区画Bへ搬送するために待機する必要がなく、スムーズに炭化処理を行えることから炭化処理物の生産性を向上させることができる   In addition, since the open / close door 4 between the reserve section 3 and the first section A can be opened immediately after carbonization, the container 7 containing waste X is transported from the first section A to the next section B. Because it is not necessary to wait for it and carbonization can be performed smoothly, productivity of carbonized material can be improved.

このように、本発明に係る炭化処理装置及び炭化処理方法によれば、炭化炉2又は最初の区画Aでの爆発等を防止でき、また、炭化処理直後であっても開閉扉4を開けることができることから、安全に且つスムーズに廃棄物Xに対して炭化処理を施すことができ、生産性の向上を図ることができる。 As described above, according to the carbonization treatment apparatus and the carbonization treatment method according to the present invention, explosion and the like in the carbonization furnace 2 or the first section A can be prevented, and the open / close door 4 is opened immediately after the carbonization treatment. As a result, the waste X can be carbonized safely and smoothly, and productivity can be improved.

1 炭化処理装置
2 炭化炉
21 水蒸気噴射孔
22 ボイラ
23 過熱水蒸気発生手段
24 連通口
25 搬入出口
26 扉
3 予備炉、予備区画
31 水蒸気噴射孔
32 ボイラ
33 連通口
34 排出口
4 開閉扉
5 搬送手段
6 送風機
7 容器
X 廃棄物
DESCRIPTION OF SYMBOLS 1 carbonization processing apparatus 2 carbonization furnace 21 steam injection hole 22 boiler 23 superheated steam generation means 24 communication port 25 loading / unloading 26 door 3 preparatory furnace, spare section 31 steam injection hole 32 boiler 33 communication port 34 discharge port 4 opening / closing door 5 conveyance means 6 Blower 7 Container X Waste

Claims (4)

開閉扉を備え、当該開閉扉を閉じた密閉状態で対象物を炭化処理する炭化炉と、前記開閉扉を開閉することで前記炭化炉と連通可能又は密閉状態となり、当該密閉状態で水蒸気を噴射する水蒸気噴射孔を備えた予備炉とからなり、
前記炭化炉で対象物を炭化処理中に、密閉状態の前記予備炉内に水蒸気を噴射して凝結させ、当該予備炉内の酸素濃度を低下させることを特徴とする炭化処理装置。
A carbonization furnace which is provided with an open / close door and carbonizes an object in a closed state where the open / close door is closed, and opening or closing the open / close door enables communication with the carbonization furnace or becomes a closed state. And a pre-furnace with steam injection holes
A carbonization treatment apparatus characterized in that water vapor is injected and condensed in the closed preliminary furnace during carbonization treatment of an object in the carbonization furnace to reduce the oxygen concentration in the preliminary furnace.
開閉扉を備え、当該開閉扉を閉じた密閉状態で対象物を炭化処理する炭化炉と、前記開閉扉を開閉することで前記炭化炉と連通可能又は密閉状態となり、当該密閉状態で水蒸気を噴射する水蒸気噴射孔を備えた予備炉とからなる炭化処理装置における炭化処理方法であって、
前記炭化炉に対象物を搬入する工程と、
前記開閉扉を閉じて炭化炉及び予備炉を密閉状態にし、当該炭化炉で対象物を炭化処理する工程と、
前記炭化炉での炭化処理中に、前記予備炉内に水蒸気噴射孔から水蒸気を一時的に噴射する工程と、
前記炭化炉での炭化処理に要する時間をかけて予備炉内を低温化させるとともに水蒸気を凝結させ、当該予備炉内の酸素濃度を低下させる工程と、
炭化処理後に前記開閉扉を開け、酸素濃度が低下し、且つ、低温化した予備炉内と高温の炭化炉内とを連通させることで、高温の炭化炉内の温度を低下させる工程と、を含むことを特徴とする炭化処理方法。
A carbonization furnace which is provided with an open / close door and carbonizes an object in a closed state where the open / close door is closed, and opening or closing the open / close door enables communication with the carbonization furnace or becomes a closed state. A carbonization treatment method in a carbonization treatment apparatus comprising a preliminary furnace provided with steam injection holes
Loading an object into the carbonizing furnace;
Closing the open / close door to seal the carbonizing furnace and the preliminary furnace, and carbonizing the object in the carbonizing furnace;
Temporarily injecting steam from the steam injection holes into the preliminary furnace during carbonization treatment in the carbonizing furnace;
Taking the time required for the carbonization treatment in the carbonization furnace to lower the temperature in the preliminary furnace and condense the water vapor to reduce the oxygen concentration in the preliminary furnace;
After the carbonization treatment, opening the open / close door to reduce the oxygen concentration and connecting the inside of the low-temperature preliminary furnace to the high-temperature carbonization furnace, thereby reducing the temperature in the high-temperature carbonization furnace; A carbonization method characterized by including.
複数種類の油分が含有された廃棄物の原料を、開閉扉で開閉可能に区切られた複数の区画からなる一連の炭化炉内に通過させ、当該複数の区画ごとに異なる温度で過熱水蒸気処理をして炭化処理物を得る炭化処理装置であって、
前記一連の炭化炉の最初の区画よりも前に、開閉扉で開閉可能に区切られた予備区画を設けてなり、
当該予備区画は、密閉状態で水蒸気を噴射する水蒸気噴射孔を備え、前記炭化炉で廃棄物を炭化処理中に水蒸気を噴射して凝結させ、当該予備炉内の酸素濃度を低下させることを特徴とする炭化処理装置。
The raw material of waste containing multiple types of oil is passed through a series of carbonizing furnaces consisting of a plurality of compartments divided by open and close doors, and superheated steam treatment is performed at different temperatures for each of the plurality of compartments A carbonizing apparatus for obtaining a carbonized product,
Before the first section of the series of carbonizing furnaces, there is provided a spare section openably and closably separated by an open / close door,
The preliminary section is provided with steam injection holes for injecting steam in a closed state, and the waste is sprayed with steam during carbonization treatment in the carbonization furnace to condense, thereby reducing the oxygen concentration in the preliminary furnace. And carbonization processing equipment.
複数種類の油分が含有された廃棄物の原料を、開閉扉で開閉可能に区切られた複数の区画からなる一連の炭化炉内に通過させ、当該複数の区画ごとに異なる温度で過熱水蒸気処理をして炭化処理物を得る炭化処理装置であって、前記一連の炭化炉の最初の区画よりも前に予備区画を設け、当該予備区画が開閉扉を閉じた密閉状態で水蒸気を噴射する水蒸気噴射孔を備えてなる炭化処理装置における炭化処理方法であって、
前記予備区画の炭化炉端部側から廃棄物を搬入し、前記最初の区画へと搬送する工程と、
前記開閉扉を閉じて最初の区画及び予備区画を密閉状態にし、当該最初の区画で廃棄物に炭化処理をする工程と、
前記最初の区画での炭化処理中に、前記予備区画内に水蒸気噴射孔から水蒸気を一時的に噴射する工程と、
前記最初の区画での炭化処理に要する時間をかけて、予備区画内の低温化させるとともに水蒸気を凝結させ、当該予備区画内の酸素濃度を低下させる工程と、
炭化処理後に前記開閉扉を開け、酸素濃度が低下し、且つ、低温化した予備区画内と高温の最初の区画内とを連通させることで、高温の最初の区画内の温度を低下させる工程と、
前記最初の区画で炭化処理をした廃棄物を、異なる温度での炭化処理のために次の区画へと搬送する工程と、を含むことを特徴とする炭化処理方法。
The raw material of waste containing multiple types of oil is passed through a series of carbonizing furnaces consisting of a plurality of compartments divided by open and close doors, and superheated steam treatment is performed at different temperatures for each of the plurality of compartments Carbonization processing apparatus for obtaining a carbonized product, wherein a preliminary section is provided prior to the first section of the series of carbonizing furnaces, and the preliminary section injects water vapor in a closed state with the open / close door closed. A carbonization treatment method in a carbonization treatment apparatus comprising a hole, comprising:
Loading waste from the carbonization furnace end side of the preliminary section and transporting it to the first section;
Closing the open / close door to seal the first compartment and the reserve compartment, and carbonizing the waste in the first compartment;
Temporarily injecting steam from the steam injection holes into the spare zone during carbonization in the first zone;
Taking the time required for the carbonization treatment in the first compartment to cool the preparatory compartment and condense water vapor to reduce the concentration of oxygen in the preparatory compartment;
After the carbonization treatment, open the open / close door, reduce the oxygen concentration, and connect the inside of the low temperature reserve compartment with the inside of the high temperature first compartment, thereby reducing the temperature in the high temperature first compartment; ,
Transferring the carbonized waste in the first section to the next section for carbonization at different temperatures.
JP2017209897A 2017-10-31 2017-10-31 Carbonization equipment and carbonization method Active JP7007158B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2017209897A JP7007158B2 (en) 2017-10-31 2017-10-31 Carbonization equipment and carbonization method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2017209897A JP7007158B2 (en) 2017-10-31 2017-10-31 Carbonization equipment and carbonization method

Publications (2)

Publication Number Publication Date
JP2019081849A true JP2019081849A (en) 2019-05-30
JP7007158B2 JP7007158B2 (en) 2022-01-24

Family

ID=66670151

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2017209897A Active JP7007158B2 (en) 2017-10-31 2017-10-31 Carbonization equipment and carbonization method

Country Status (1)

Country Link
JP (1) JP7007158B2 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000313884A (en) * 1999-03-03 2000-11-14 Toyoda Techno Kk Waste treating method
JP2001115167A (en) * 1999-10-22 2001-04-24 Toyoda Techno Kk Dry distillation method using superheated steam as heat source and its apparatus
JP2002037687A (en) * 2000-07-25 2002-02-06 Toyoda Techno Kk Manufacturing method of organic fertilizer
WO2013011555A1 (en) * 2011-07-19 2013-01-24 株式会社ワンワールド Apparatus and method for carbonizing organic material
JP2013040054A (en) * 2011-08-11 2013-02-28 Lignyte Co Ltd Carbide and method for producing the carbide

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000313884A (en) * 1999-03-03 2000-11-14 Toyoda Techno Kk Waste treating method
JP2001115167A (en) * 1999-10-22 2001-04-24 Toyoda Techno Kk Dry distillation method using superheated steam as heat source and its apparatus
JP2002037687A (en) * 2000-07-25 2002-02-06 Toyoda Techno Kk Manufacturing method of organic fertilizer
WO2013011555A1 (en) * 2011-07-19 2013-01-24 株式会社ワンワールド Apparatus and method for carbonizing organic material
JP2013040054A (en) * 2011-08-11 2013-02-28 Lignyte Co Ltd Carbide and method for producing the carbide

Also Published As

Publication number Publication date
JP7007158B2 (en) 2022-01-24

Similar Documents

Publication Publication Date Title
JPS6116910B2 (en)
US4924785A (en) Thermal cleaning system
JP2008222901A (en) Carbonization apparatus
CN102154614A (en) Vacuum carburization processing method and vacuum carburization processing apparatus
US20110318698A1 (en) Zero water discharge oven cooling
US8945348B2 (en) Carbonization method and device
KR920001359B1 (en) Muffle furnace for continuous heat treatment
CN1643324A (en) Installation for the heat-treatment of parts
JP2019081849A (en) Carbonizing apparatus and carbonizing method
JP2004537645A (en) Processing of organic substances
WO2005080286A1 (en) Method of sealing glass panel assembly and sealing furnace
EP3775102B1 (en) Method and apparatus for processing biomass
JP4668358B2 (en) Induction heating type distillation furnace
US20080257709A1 (en) Method and Equipment for Whole Tyre Pyrolysis
US20190048166A1 (en) Hybrid processing of waste material
JP4667905B2 (en) Induction heating type distillation furnace
JP4641816B2 (en) Induction heating type distillation furnace
JP3235877U (en) Carbonized product manufacturing equipment
JP2004175921A (en) Carbonization method for organic waste
JP2019081848A (en) Manufacturing apparatus for carbonized material
JP6791577B2 (en) Carbonization equipment and carbonization method for organic matter
CN107202491A (en) A kind of two-layer equation refuse pyrolysis tunnel cave
JP4585348B2 (en) Method and apparatus for recovery and storage of combustion components from waste
JPS61255989A (en) Production of coke and container and apparatus
JP2003213271A (en) Method for carbonizing organic sludge and carbonization installation therefor

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20201030

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20210105

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20210826

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20210907

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20211007

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20211027

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20211007

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20211111

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20211214

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20220106

R150 Certificate of patent or registration of utility model

Ref document number: 7007158

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350