JP2016090215A - Low temperature thermal decomposition treatment furnace - Google Patents

Low temperature thermal decomposition treatment furnace Download PDF

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JP2016090215A
JP2016090215A JP2014235041A JP2014235041A JP2016090215A JP 2016090215 A JP2016090215 A JP 2016090215A JP 2014235041 A JP2014235041 A JP 2014235041A JP 2014235041 A JP2014235041 A JP 2014235041A JP 2016090215 A JP2016090215 A JP 2016090215A
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organic matter
decomposition
ash
magnetic air
tank
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義秋 小野寺
Yoshiaki Onodera
義秋 小野寺
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GOJO KK
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Abstract

PROBLEM TO BE SOLVED: To provide a low temperature thermal decomposition treatment furnace in which an amount of supply of magnetization air can be made uniform and organic matter can be positively thermally decomposed.SOLUTION: A low temperature thermal decomposition treatment furnace 100 comprises: a hollow rectangular parallelepiped organic matter decomposition tank 3 having at its upper surface an organic matter feeding port and at its lower surface magnetization air supply plate 5 so as to thermally decompose an organic matter fed from the organic matter feeding port at low temperature; a magnetization air tank 2 arranged below the magnetization air supply plate to supply magnetization air to the organic matter decomposition tank through the magnetization air supply plate; an air magnetization device for supplying magnetization air to the magnetization air tank; a decomposition ash accumulated depth adjustment mechanism for adjusting an accumulation depth of decomposed ash accumulated at the bottom surface of the organic matter decomposition tank constant; a decomposition ash discharging mechanism for discharging the surplus decomposition ash accumulated at the bottom surface of the organic matter decomposition tank; a gas discharging facility for discharging gas generated in the organic matter decomposition tank; and a counter-flow prevention mechanism installed at a decomposition ash discharging port of the decomposition ash discharging mechanism to prevent the surrounding air from counter-flowing into the organic matter decomposition tank.SELECTED DRAWING: Figure 1

Description

本発明は、廃棄物である有機物を低温度(例えば、摂氏400度未満)で熱分解処理する低温熱分解処理炉に関する。  The present invention relates to a low-temperature pyrolysis furnace that decomposes organic matter that is waste at a low temperature (for example, less than 400 degrees Celsius).

本出願人は、有機物の処理方法として、ダイオキシンの発生防止のために有機物を低温で熱分解する低温熱分解処理炉を既に提案している(例えば、特許文献1)。
この炉は、外槽内に形成された有機物分解槽と、外槽の下部において有機物分解槽から隔成された空気室と、空気室へ磁気空気を供給する給送手段と、有機物分解槽と空気室とを連通させる給気孔と、給気孔の上部を覆う庇部と、給気孔の下部に突出されたガイド部材と、を備えている。
そして、有機物分解槽の下部には外槽の外部に通じる排出路を備え、空気室は有機物分解槽と空気室とを仕切る斜板を有し、斜板は有機物熱分解槽底面中央に設置される排出路に向かって傾斜している。
The present applicant has already proposed a low-temperature pyrolysis furnace that thermally decomposes an organic substance at a low temperature in order to prevent generation of dioxins as a method for treating the organic substance (for example, Patent Document 1).
The furnace includes an organic substance decomposition tank formed in the outer tank, an air chamber separated from the organic substance decomposition tank at a lower portion of the outer tank, a feeding means for supplying magnetic air to the air chamber, an organic substance decomposition tank, An air supply hole that communicates with the air chamber, a flange that covers an upper portion of the air supply hole, and a guide member that protrudes below the air supply hole are provided.
The lower part of the organic matter decomposition tank is provided with a discharge path leading to the outside of the outer tank, the air chamber has a swash plate that partitions the organic matter decomposition tank and the air chamber, and the swash plate is installed at the center of the bottom of the organic matter decomposition tank. Inclined toward the discharge path.

上記構造により、不燃物の発生を抑制しつつ、有機物を確実かつ効率よく分解することを目的としていた。  The above structure aims to reliably and efficiently decompose organic substances while suppressing the generation of non-combustible substances.

特開2014−94326号JP 2014-94326 A

しかしながら、上記提案に係る低温熱分解処理炉は、底面がV字型構造を有するので、有機物が熱分解されることにより生成される分解灰(セラミック灰)は底面に均一な厚さで堆積することはなく、堆積層の厚さは底面両端部で薄く、底面中心部で厚くなる。  However, since the bottom surface of the low-temperature pyrolysis furnace according to the above proposal has a V-shaped structure, decomposed ash (ceramic ash) generated by pyrolyzing organic matter is deposited on the bottom surface with a uniform thickness. In other words, the thickness of the deposited layer is thin at both ends of the bottom surface and thick at the center of the bottom surface.

この結果、底面に設けられる給気孔から供給される磁気空気を有機物分解槽内に均一に供給することができない。
このため、有機物分解槽内で酸素濃度が均一とならず、有機物を確実に熱分解することが困難となるという課題を生じる。
As a result, the magnetic air supplied from the air supply holes provided on the bottom surface cannot be uniformly supplied into the organic matter decomposition tank.
For this reason, the oxygen concentration is not uniform in the organic matter decomposition tank, and there arises a problem that it is difficult to reliably thermally decompose the organic matter.

すなわち、磁気空気が多量に供給される両端部では有機物は燃焼してしまい、磁気空気が少量しか供給されない底面中央部では有機物は熱分解されずに未処理のまま底面から排出されてしまうことがあった。  That is, the organic matter burns at both ends where a large amount of magnetic air is supplied, and the organic matter is discharged from the bottom without being thermally decomposed at the center of the bottom where only a small amount of magnetic air is supplied. there were.

本発明は上記課題に鑑みなされたものであって、有機物分解槽内への磁気空気の供給量を均一とし、有機物を確実に熱分解処理することのできる低温熱分解処理炉を提供することを目的とする。  The present invention has been made in view of the above problems, and provides a low-temperature pyrolysis furnace that can uniformly supply the magnetic air into the organic matter decomposition tank and can reliably thermally decompose the organic matter. Objective.

本発明に係る低温熱分解処理炉は、上面に有機物投入口を、下面に磁気空気供給板を有し、有機物投入口から投入される有機物を低温熱分解する中空直方体形状の有機物分解槽と、磁気空気供給板の下部に配置され磁気空気供給板を介して有機物分解槽に磁気空気を供給する磁気空気槽と、磁気空気槽に磁気空気を供給する空気磁化装置と、有機物分解槽の底面に堆積する分解灰の堆積深さを一定に調整する分解灰堆積深さ調整機構と、有機物分解槽の底面に堆積する余剰の分解灰を排出する分解灰排出機構と、有機物分解槽内で発生するガスを排気するガス排出設備と、分解灰排出機構の分解灰排出口に設置され大気が有機物分解槽に逆流することを防止するために分解灰排出機構の分解灰排出口に設置される逆流防止機構と、を有する。  The low-temperature pyrolysis furnace according to the present invention has an organic matter inlet on the upper surface, a magnetic air supply plate on the lower surface, and a hollow cuboid-shaped organic matter decomposition tank that thermally decomposes organic matter introduced from the organic matter inlet, A magnetic air tank disposed under the magnetic air supply plate for supplying magnetic air to the organic matter decomposition tank via the magnetic air supply plate, an air magnetizing device for supplying magnetic air to the magnetic air tank, and a bottom surface of the organic matter decomposition tank Decomposition ash deposition depth adjustment mechanism that adjusts the deposition depth of the decomposed ash to deposit, a decomposition ash discharge mechanism that discharges excess decomposed ash deposited on the bottom of the organic matter decomposition tank, and an organic matter decomposition tank Backflow prevention installed at the decomposition ash discharge port of the decomposition ash discharge mechanism to prevent the air from flowing back to the organic matter decomposition tank installed at the decomposition ash discharge port of the gas discharge facility and the decomposition ash discharge mechanism And a mechanism.

この構成により、本発明に係る低温熱分解処理炉は、有機物分解槽内の有機物を確実に低温熱分解することができることとなる。  With this configuration, the low-temperature pyrolysis furnace according to the present invention can reliably perform low-temperature pyrolysis of organic substances in the organic substance decomposition tank.

本発明に係る低温熱分解処理炉は、分解灰堆積深さ調整機構が磁気空気供給板の一辺と並行に設置される複数本の分解灰体積深さ調整スクリューである。  The low-temperature pyrolysis treatment furnace according to the present invention is a plurality of cracked ash volume depth adjusting screws in which the cracked ash accumulation depth adjusting mechanism is installed in parallel with one side of the magnetic air supply plate.

この構成により、本発明に係る低温熱分解処理炉は、所定温度以上の分解灰の堆積深さを一定に維持し、所定温度未満の分解灰を取り除くことが可能となる。  With this configuration, the low-temperature pyrolysis furnace according to the present invention can maintain the deposition depth of cracked ash at a predetermined temperature or higher and remove cracked ash at a temperature lower than the predetermined temperature.

本発明に係る低温熱分解処理炉は、分解灰排出機構が分解灰量調整スクリューの両端下部に分解灰量調整スクリューと直角に設置される分解灰排出スクリューである。  The low-temperature pyrolysis treatment furnace according to the present invention is a cracked ash discharge screw in which a cracked ash discharge mechanism is installed at both ends of the cracked ash amount adjusting screw at right angles to the cracked ash amount adjusting screw.

この構成により、本発明に係る低温熱分解処理炉は、所定温度未満の余剰な分解灰を確実に排出可能となる。  With this configuration, the low-temperature pyrolysis furnace according to the present invention can reliably discharge excess cracked ash having a temperature lower than a predetermined temperature.

本発明に係る低温熱分解処理炉は、逆流防止機構が分解灰排出スクリューの分解灰排出口に設置される遮断回転弁である。  The low-temperature pyrolysis furnace according to the present invention is a shut-off rotary valve in which a backflow prevention mechanism is installed at the cracked ash discharge port of the cracked ash discharge screw.

この構成により、本発明に係る低温熱分解処理炉は、分解灰の排出中であるか否かに拘らず、有機物分解槽内に磁化されていない大気が流入することを防止できることとなる。  With this configuration, the low-temperature pyrolysis furnace according to the present invention can prevent the unmagnetized air from flowing into the organic matter decomposition tank regardless of whether or not the decomposition ash is being discharged.

本発明に係る低温熱分解処理炉は、磁気空気供給板が、下端から上端に向かって斜め上方に延伸する第1の磁気空気隙間板と、第1の磁気空気隙間板の上端の下側に隙間を隔てて配置される上端から下端に向かって斜め下方に延伸する第2の磁気空気隙間板と、第1の磁気空気隙間板の下端と第2の磁気空気隙間板の下端との間に配置され分解灰量調整スクリューを格納するスクリュー格納溝と、からなる。  In the low-temperature pyrolysis furnace according to the present invention, the magnetic air supply plate extends below the upper end of the first magnetic air gap plate and the first magnetic air gap plate extending obliquely upward from the lower end toward the upper end. Between the lower end of the second magnetic air gap plate and the second magnetic air gap plate, the second magnetic air gap plate extending obliquely downward from the upper end to the lower end disposed with a gap therebetween And a screw storage groove for storing the cracked ash amount adjusting screw.

この構成により、本発明に係る低温熱分解処理炉は、分解灰が均一の深さで堆積するとともに、有機物分解槽内に常時磁気空気を供給することが可能となる。  With this configuration, the low-temperature pyrolysis furnace according to the present invention can deposit cracked ash at a uniform depth and always supply magnetic air into the organic matter decomposition tank.

本発明に係る低温熱分解処理炉は、分解灰量調整スクリューが、互いに逆方向に回転する第1の分解灰量調整スクリューと第2の分解灰量調整スクリューとが交互に配置される。  In the low-temperature pyrolysis furnace according to the present invention, the first cracked ash amount adjusting screw and the second cracked ash amount adjusting screw in which the cracked ash amount adjusting screw rotates in opposite directions are alternately arranged.

この構成により、本発明に係る低温熱分解処理炉は、分解灰の堆積深さを確実に一定に維持できることとなる。  With this configuration, the low-temperature pyrolysis furnace according to the present invention can reliably maintain the deposition depth of cracked ash constant.

本発明に係る低温熱分解炉によれば、ダイオキシンの発生を抑制しつつ有機物を確実に低温熱分解して、有機物を重量比で10分の1ないしは容積比で100分の1に低減することが可能となる。  According to the low-temperature pyrolysis furnace according to the present invention, the organic matter is reliably subjected to low-temperature pyrolysis while suppressing the generation of dioxins, and the organic matter is reduced to 1/10 by weight or 1/100 by volume. Is possible.

本発明に係る低温熱分解処理炉の実施形態の正面断面図(a)および側面断面図(b)である。It is a front sectional view (a) and a side sectional view (b) of an embodiment of a low temperature pyrolysis furnace according to the present invention. 本発明に係る低温熱分解処理炉の実施形態の低温熱分解処理炉下部の断面図(a)、および部分拡大斜視図(b)である。It is sectional drawing (a) of the low-temperature pyrolysis processing furnace lower part of embodiment of the low-temperature pyrolysis processing furnace based on this invention, and a partial expansion perspective view (b). 有機物処理槽の下部に構成される低温熱分解灰排出部の断面図である。It is sectional drawing of the low-temperature pyrolysis ash discharge part comprised in the lower part of an organic substance processing tank. 磁気空気槽の底面に複数個取り付けられる磁気ケースの断面図(a)および下面図(b)である。It is sectional drawing (a) and bottom view (b) of the magnetic case with which two or more are attached to the bottom face of a magnetic air tank. 低温熱分解処理炉を暖機するための暖機運転フローチャートである。It is a warm-up operation flowchart for warming up the low-temperature pyrolysis furnace. 低温熱分解処理炉の通常運転フローチャートである。It is a normal operation flowchart of a low-temperature pyrolysis treatment furnace.

以下本発明の実施形態を、図面を参照しつつ、説明する。
図1は、本発明に係る低温熱分解処理炉の実施形態の正面断面図(a)および側面断面図(b)である。
また、図2は本発明に係る低温熱分解処理炉の実施形態の低温熱分解処理炉下部の断面図(a)、および部分拡大斜視図(b)である。
Embodiments of the present invention will be described below with reference to the drawings.
FIG. 1 is a front sectional view (a) and a side sectional view (b) of an embodiment of a low temperature pyrolysis furnace according to the present invention.
FIG. 2 is a cross-sectional view (a) and a partially enlarged perspective view (b) of the lower part of the low temperature pyrolysis furnace of the embodiment of the low temperature pyrolysis furnace according to the present invention.

すなわち、本発明に係る低温熱分解処理炉100は、中空直方体状の外箱1内の下部に磁気空気槽2が、上部に有機物分解槽3が積み重ねられた構造を有する。
有機物分解槽3と磁気空気槽2とは磁気空気供給板5で仕切られている。また、有機物分解槽3の上面は下部開閉蓋15によって覆われている。
なお、有機物分解槽3には開口板7が設けられており、暖機運転時に有機物分解槽3に藁等の初期燃料を有機物分解槽3に直接供給できるようになっている。
That is, the low-temperature pyrolysis furnace 100 according to the present invention has a structure in which the magnetic air tank 2 is stacked in the lower part of the hollow rectangular parallelepiped outer box 1 and the organic substance decomposition tank 3 is stacked in the upper part.
The organic matter decomposition tank 3 and the magnetic air tank 2 are partitioned by a magnetic air supply plate 5. The upper surface of the organic matter decomposition tank 3 is covered with a lower opening / closing lid 15.
The organic substance decomposition tank 3 is provided with an opening plate 7 so that initial fuel such as soot can be directly supplied to the organic substance decomposition tank 3 during the warm-up operation.

有機物分解槽3と磁気空気槽2とを仕切る磁気空気供給板5は、図2に示すように、斜め右(または左)上に延びる第1の磁気空気隙間板51と、第1の磁気空気隙間板51の上端の下側から隙間をおいて右(または左)下に延びる第2の磁気空気隙間板52と、第1の磁気空気隙間板51と第2の磁気空気隙間板52のそれぞれの下端の間に配置されるスクリュー収納溝53と、が順に配置された構成を有する。  As shown in FIG. 2, the magnetic air supply plate 5 that partitions the organic matter decomposition tank 3 and the magnetic air tank 2 includes a first magnetic air gap plate 51 that extends diagonally right (or left), and a first magnetic air. Each of a second magnetic air gap plate 52 extending from the lower side of the upper end of the gap plate 51 to the right (or left) with a gap therebetween, and the first magnetic air gap plate 51 and the second magnetic air gap plate 52, respectively. And a screw storage groove 53 arranged between the lower ends of the two.

第2の磁気空気隙間板52の先端は、第1の磁気空気隙間板51の先端の下側に隙間をあけて配置され、その隙間から磁気空気が有機物分解槽3内に供給されるようになっている。
すなわち、磁気空気供給板5は、細かい凹凸はあるものの、全体的に平坦とし、有機物分解槽3内に磁気空気を均一に供給可能な構造となっている。
The tip of the second magnetic air gap plate 52 is arranged with a gap below the tip of the first magnetic air gap plate 51 so that magnetic air is supplied into the organic matter decomposition tank 3 from the gap. It has become.
That is, the magnetic air supply plate 5 is flat as a whole, although it has fine irregularities, and has a structure that can uniformly supply magnetic air into the organic matter decomposition tank 3.

有機物分解槽3内で有機物が低温熱分解されると、大部分は窒素ガス、水素ガス、酸素ガス等のガスとなって大気に放出されるが、一部は分解灰として磁気空気供給板5上に堆積する。  When the organic matter is pyrolyzed at a low temperature in the organic matter decomposition tank 3, most of it is released into the atmosphere as a gas such as nitrogen gas, hydrogen gas, oxygen gas, etc., but a part of it is decomposed ash and the magnetic air supply plate 5 Deposit on top.

有機物を確実に分解するためには、有機物分解槽3内に磁気空気を均一に供給するだけでなく、磁気空気供給板5上に堆積する分解灰の厚さを所定の深さに維持することが必要である。
さらに、有機物の分解を維持するためには分解灰が所定温度以上であることも必要であるので、堆積した分解灰の下側から順次有機物分解槽3の外に排出することが必要となる。
ここで、所定温度とは外部から熱エネルギを加えることなく、低温熱分解を持続できる分解灰の温度であり、摂氏150〜180度の温度を意味する。
In order to reliably decompose the organic matter, not only the magnetic air is uniformly supplied into the organic matter decomposition tank 3, but also the thickness of the decomposed ash deposited on the magnetic air supply plate 5 is maintained at a predetermined depth. is necessary.
Furthermore, in order to maintain the decomposition of the organic matter, it is also necessary that the decomposed ash is at a predetermined temperature or higher, so that it is necessary to sequentially discharge the organic matter decomposition tank 3 from the lower side of the accumulated decomposed ash.
Here, the predetermined temperature is the temperature of cracked ash that can maintain low-temperature pyrolysis without applying heat energy from the outside, and means a temperature of 150 to 180 degrees Celsius.

そこで、本発明に係る低温熱分解処理炉100では、分解灰の堆積深さを一定に調整するための分解灰堆積深さ調整機構および分解灰を排出するための分解灰排出機構を備えている。
分解灰堆積深さ調整機構は、分解灰の下側を所定深さ削り取ることができるものであればよいが、本実施例では分解灰堆積深さ調整スクリュー9を採用している。
また、分解灰排出機構は、分解灰堆積深さ調整機構で削り取られた分解灰を低温熱分解処理炉100外に排出できるものであれば、本実施例では分解灰排出スクリュー8を使用している。
Therefore, the low-temperature pyrolysis furnace 100 according to the present invention includes a cracked ash deposition depth adjustment mechanism for adjusting the deposition depth of cracked ash to a constant and a cracked ash discharge mechanism for discharging cracked ash. .
The decomposition ash accumulation depth adjusting mechanism may be any mechanism that can scrape the lower side of the decomposition ash to a predetermined depth, but in this embodiment, the decomposition ash accumulation depth adjusting screw 9 is employed.
Further, the cracked ash discharge mechanism uses a cracked ash discharge screw 8 in this embodiment as long as the cracked ash scraped by the cracked ash accumulation depth adjusting mechanism can be discharged out of the low-temperature pyrolysis furnace 100. Yes.

なお、分解灰堆積深さ調整機構としては、分解灰の下部を所定の厚さで削り取る削り板を往復動させる機構、あるいは、三角翼を周囲に取り付けた円柱棒を往復動させる機構などを適用することができる。
また、分解灰排出機構としては、ベルトコンベア等を適用することができる。
As the cracked ash accumulation depth adjustment mechanism, a mechanism that reciprocates a cutting plate that scrapes the lower part of the cracked ash at a predetermined thickness, or a mechanism that reciprocates a cylindrical rod with a triangular wing attached around it, etc. can do.
Moreover, a belt conveyor etc. can be applied as a decomposition ash discharge | emission mechanism.

図3は有機物分解槽3の下部に構成される分解灰排出部の断面図である。
分解灰排出部は、有機物分解槽3に向かって開口するスクリュー収納溝53に格納される複数本の分解灰堆積深さ調整スクリュー9と、分解灰体積深さ調整スクリュー9の両端下側に配置される分解灰排出スクリュー8とで構成されている。
FIG. 3 is a cross-sectional view of the cracked ash discharge portion configured at the lower part of the organic matter decomposition tank 3.
The cracked ash discharge part is disposed below the both ends of the plurality of cracked ash accumulation depth adjusting screws 9 stored in the screw storage grooves 53 that open toward the organic matter decomposition tank 3 and the cracked ash volume depth adjusting screw 9. And the decomposed ash discharge screw 8.

分解灰堆積深さ調整スクリュー9は、隣り合う分解灰堆積深さ調整スクリュー9が互いに逆方向に回転するようになっている。
2本の分解灰排出スクリュー8は、分解灰体積深さ調整スクリュー9の両端下部に分解灰堆積深さ調整スクリュー9と直角方向に配置され、分解灰体積深さ調整スクリュー9によって端部に運搬された分解灰を外箱1の外部に排出するようになっている。
The cracked ash deposition depth adjusting screw 9 is configured such that adjacent cracked ash deposition depth adjusting screws 9 rotate in opposite directions.
The two cracked ash discharge screws 8 are disposed at the lower ends of both ends of the cracked ash volume depth adjusting screw 9 in a direction perpendicular to the cracked ash accumulation depth adjusting screw 9, and are conveyed to the ends by the cracked ash volume depth adjusting screw 9. The decomposed ash is discharged to the outside of the outer box 1.

なお、分解灰排出スクリュー8の分解灰排出口には、排出口の閉止状態だけでなく開放状態でも排出口から有機物分解槽3の中に磁化されていない空気が流入することを防止する逆流防止機構を設置することが必要である。
そして、本実施例では逆流防止機構として、遮断回転弁10を適用している。
The cracked ash discharge port of the cracked ash discharge screw 8 prevents backflow that prevents unmagnetized air from flowing into the organic matter decomposition tank 3 from the discharge port not only when the discharge port is closed but also when it is open. It is necessary to install a mechanism.
In this embodiment, the shutoff rotary valve 10 is applied as a backflow prevention mechanism.

図4は、磁気空気槽2の底面に複数個取り付けられる磁気ケース20の断面図(a)および下面図(b)であって、磁気ケースフランジ201、磁気ケース外筒202、および永久磁石203で構成される。  FIG. 4 is a cross-sectional view (a) and a bottom view (b) of the magnetic case 20 attached to the bottom surface of the magnetic air tank 2, and includes a magnetic case flange 201, a magnetic case outer cylinder 202, and a permanent magnet 203. Composed.

すなわち、磁気ケース外筒202の上端は磁気ケースフランジ201に取り付けられ、他端は大気に開口している。磁気ケース外筒202の内側には6千〜1万ガウス程度の磁束密度の永久磁石203が例えば4個配置され、磁気ケース外筒202に吸い込まれる大気に含まれる酸素を磁化する。
なお、永久磁石203を磁気ケース内側に取り付けることにより、効率的に磁化することができる。
That is, the upper end of the magnetic case outer cylinder 202 is attached to the magnetic case flange 201, and the other end is open to the atmosphere. For example, four permanent magnets 203 having a magnetic flux density of about 6,000 to 10,000 gauss are arranged inside the magnetic case outer cylinder 202 to magnetize oxygen contained in the atmosphere sucked into the magnetic case outer cylinder 202.
In addition, it can magnetize efficiently by attaching the permanent magnet 203 inside a magnetic case.

そして、磁気ケースフランジ201の中心には磁気空気供給口204が穿孔されており、磁気空気を磁気空気槽2に供給するようになっている。
なお、磁気空気の流路を構成する部分の部材としては磁性体を使用することが好ましい。
A magnetic air supply port 204 is bored in the center of the magnetic case flange 201 so that magnetic air is supplied to the magnetic air tank 2.
In addition, it is preferable to use a magnetic body as a member of the part which comprises the flow path of magnetic air.

図1に示すように、下部開閉蓋15の上部には、上部貯蔵部12が設けられており、上部貯蔵部12の上面は上部開閉ジャッキ14によって開閉される上部開閉蓋13で覆われている。  As shown in FIG. 1, an upper storage part 12 is provided on the upper part of the lower opening / closing lid 15, and the upper surface of the upper storage part 12 is covered with an upper opening / closing lid 13 that is opened and closed by an upper opening / closing jack 14. .

また、図1に示すように、有機物分解槽3の上部には排気管21が取り付けられており、有機物分解槽3内で発生する排気ガスを排出するようになっている。
排気管21は浄煙装置18を介して磁気空気排風機17に接続されており、浄煙装置18によりタール分などを除去した排気ガスを大気に排気するようになっている。
As shown in FIG. 1, an exhaust pipe 21 is attached to the upper part of the organic matter decomposition tank 3, and exhaust gas generated in the organic matter decomposition tank 3 is discharged.
The exhaust pipe 21 is connected to the magnetic air blower 17 via the smoke purifier 18, and exhaust gas from which tar and the like are removed by the smoke purifier 18 is exhausted to the atmosphere.

なお、磁気空気排風機17の下流側には磁気空気調整バルブ16が配置されており、排気ガス量を調整できるようになっている。
また、有機物分解槽3の側板の内側には煙道遮蔽板4が設置されていて、有機物分解槽3内の有機物が直接排気管21に流入することを防止している。
A magnetic air adjusting valve 16 is disposed downstream of the magnetic air exhauster 17 so that the amount of exhaust gas can be adjusted.
A flue shielding plate 4 is installed inside the side plate of the organic matter decomposition tank 3 to prevent the organic matter in the organic matter decomposition tank 3 from flowing directly into the exhaust pipe 21.

また、有機物分解槽3には、上部に槽内の雰囲気温度を計測をするための有機物分解槽内温度センサ24が、中部に有機物を感知するための有機物センサ11が、下部に分解灰の温度を検知するための分解灰温度センサ40が設置されている。
さらに、低温熱分解処理炉100は、有機物の分解度合を検出するために、例えばロードセルである重量計測センサ50を介して据え付けられている。
The organic matter decomposition tank 3 has an organic substance decomposition tank temperature sensor 24 for measuring the atmospheric temperature in the tank at the upper part, an organic substance sensor 11 for sensing organic substances in the middle part, and a decomposition ash temperature at the lower part. A decomposition ash temperature sensor 40 for detecting the above is installed.
Furthermore, the low-temperature pyrolysis furnace 100 is installed via a weight measurement sensor 50 that is a load cell, for example, in order to detect the degree of decomposition of organic matter.

次に、本発明に係る低温熱分解処理炉100の運用方法を説明する。
図5は、低温熱分解処理炉100を予熱するための初期運転方法を示すフローチャートである。
Next, an operation method of the low temperature pyrolysis furnace 100 according to the present invention will be described.
FIG. 5 is a flowchart showing an initial operation method for preheating the low temperature pyrolysis furnace 100.

まず、有機物分解槽の側板に取り付けられた開口板7を解放し、有機物分解槽3内に藁を投入する(ステップW1)。
次に、上部開閉蓋13を開状態とし、含水率50パーセント以下の有機物を上部貯蔵槽12に投入する(ステップW2)。
その後、下部開閉蓋15を開とし、有機物を有機物分解槽3内の藁の上に落下させる(ステップW3)。
First, the opening plate 7 attached to the side plate of the organic matter decomposition tank is released, and the soot is put into the organic matter decomposition tank 3 (step W1).
Next, the upper open / close lid 13 is opened, and an organic substance having a moisture content of 50% or less is put into the upper storage tank 12 (step W2).
Thereafter, the lower opening / closing lid 15 is opened, and the organic matter is dropped onto the basket in the organic matter decomposition tank 3 (step W3).

次に、上部開閉蓋13および下部開閉蓋15を閉止する(ステップW4)。
次に、磁気空気排風機17の運転を開始し、藁に着火する(ステップW5)。
そして、有機物分解槽3内の温度が摂氏250度以上350度以下となるように磁気空気調整バルブの開度を調整する(ステップW6)。
Next, the upper opening / closing lid 13 and the lower opening / closing lid 15 are closed (step W4).
Next, the operation of the magnetic air exhauster 17 is started and the soot is ignited (step W5).
Then, the opening degree of the magnetic air adjustment valve is adjusted so that the temperature in the organic matter decomposition tank 3 is 250 degrees centigrade or more and 350 degrees centigrade or less (step W6).

すると、有機物分解槽3内の有機物の低温熱分解が始まり、その際に発生する分解熱により低温熱分解処理炉100の暖機が開始される(ステップW7)。
有機物分解槽3内の有機物の低温熱分解が進み、有機物センサ11が有機物を検出しなくなった時をもって暖機を終了する(ステップW8)。
Then, the low temperature thermal decomposition of the organic substance in the organic substance decomposition tank 3 starts, and warming up of the low temperature thermal decomposition treatment furnace 100 is started by the decomposition heat generated at that time (step W7).
Warm-up is completed when the low temperature thermal decomposition of the organic matter in the organic matter decomposition tank 3 has progressed and the organic matter sensor 11 no longer detects the organic matter (step W8).

図6は、低温熱分解処理炉100の通常運転方法を示すフローチャートである。
まず、有機物分解槽3の下部の分解灰排出部に設置されている分解灰温度センサ40により検出される分解灰の温度が摂氏150度以上であること、有機物センサ11が有機物を検出していないことを確認する(ステップN1)。
FIG. 6 is a flowchart showing a normal operation method of the low-temperature pyrolysis furnace 100.
First, the temperature of the decomposed ash detected by the decomposed ash temperature sensor 40 installed in the decomposed ash discharge part at the lower part of the organic substance decomposition tank 3 is 150 degrees Celsius or more, and the organic substance sensor 11 does not detect the organic substance. (Step N1).

次に、上部開閉蓋13を開状態とし、有機物を上部貯蔵槽12に投入し、上部開閉蓋13を閉止する(ステップN2)。
次に、下部開閉蓋11を開き、有機物を有機物分解槽3に落下させる(ステップN3)。
有機物が有機物分解槽3に落下したことを確認して下部開閉蓋を閉止する(ステップN4)。
すると、有機物分解槽3の底部にある分解灰の熱により有機物の低温熱分解が始まり、大部分は炭酸ガス、窒素ガス、水蒸気となって大気に放出され、残りは分解灰となって底部に堆積する(ステップN5)。
Next, the upper opening / closing lid 13 is opened, an organic substance is put into the upper storage tank 12, and the upper opening / closing lid 13 is closed (step N2).
Next, the lower opening / closing lid 11 is opened, and the organic matter is dropped into the organic matter decomposition tank 3 (step N3).
After confirming that the organic matter has fallen into the organic matter decomposition tank 3, the lower opening / closing lid is closed (step N4).
Then, the low-temperature pyrolysis of the organic matter starts by the heat of the cracked ash at the bottom of the organic matter cracking tank 3, most of which is released into the atmosphere as carbon dioxide, nitrogen gas and water vapor, and the rest as cracked ash at the bottom Deposit (Step N5).

有機物の低温熱分解中は、分解灰体積深さ調整スクリュー9を適切に運転して、分解灰が底面に一様の深さで堆積するようにする。
そして、余剰な分解灰は、分解灰排出スクリュー8により、低温熱分解処理炉100の外に排出する(ステップN6)。
During the low-temperature pyrolysis of the organic matter, the cracked ash volume depth adjusting screw 9 is appropriately operated so that the cracked ash is deposited at a uniform depth on the bottom surface.
Excess cracked ash is discharged out of the low-temperature pyrolysis furnace 100 by the cracked ash discharge screw 8 (step N6).

有機物の分解が進み、有機物センサ11が有機物を検出しなくなり、重量計測センサ50の計測値から有機物分解槽3内の有機物の低温熱分解が完了したと判断されると1バッチの処置は完了したものとして(ステップN7)ステップN2に戻り、処理を続行する。
なお、有機物を重量比で約50分の1もしくは容積比で約100分の1にまで熱分解する1バッチ処理には10時間程度を要する。
When the decomposition of the organic matter progresses, the organic matter sensor 11 stops detecting the organic matter, and when it is determined from the measurement value of the weight measurement sensor 50 that the low-temperature thermal decomposition of the organic matter in the organic matter decomposition tank 3 is completed, one batch of treatment is completed. As a result (step N7), the process returns to step N2 to continue the processing.
In addition, about 10 hours are required for 1 batch process which thermally decomposes organic substance to about 1/50 by weight ratio or about 1/100 by volume ratio.

以上説明したように、本発明に係る低温熱分解処理炉100は、分解灰は有機物分解槽3の底部に一様な深さで堆積するので、磁気空気槽2から有機物分解槽3内に均一に磁気空気を供給することが可能となり、有機物を確実に低温熱分解することができる。  As described above, in the low-temperature pyrolysis furnace 100 according to the present invention, the cracked ash is deposited at a uniform depth on the bottom of the organic matter decomposition tank 3, so that it is uniform from the magnetic air tank 2 into the organic matter decomposition tank 3. It becomes possible to supply magnetic air to the organic substance, and the organic matter can be reliably pyrolyzed at low temperature.

さらに、磁気空気槽2から有機物分解槽3に磁気空気を供給する隙間は、第1の磁気空気隙間板51の上端の下側に設けられているため、分解灰の堆積によって塞がれることはなく、磁気空気を確実に供給して有機物の低温分解を一層促進することが可能となる。  Furthermore, since the gap for supplying magnetic air from the magnetic air tank 2 to the organic matter decomposition tank 3 is provided below the upper end of the first magnetic air gap plate 51, it is not blocked by the accumulation of decomposed ash. In addition, it is possible to reliably supply magnetic air and further promote low-temperature decomposition of organic substances.

本発明に係る低温熱分解炉は、ダイオキシンの発生を抑制しつつ廃棄物である有機物を低温熱分解することができ、産業上有用である。  The low-temperature pyrolysis furnace according to the present invention is capable of low-temperature pyrolysis of organic matter that is waste while suppressing generation of dioxins, and is industrially useful.

1…外箱
2…磁気空気槽
3…有機物分解槽
4…煙道遮蔽板
5…磁気空気供給板
7…開口板
8…分解灰排出スクリュー
9…分解灰体積深さ調整スクリュー
10…遮断回転弁
11…有機物センサ
12…上部貯蔵槽
13…上部開閉蓋
14…上部開閉蓋開閉ジャッキ
15…下部開閉蓋
16…磁気空気調整バルブ
17…磁気空気排風機
18…浄煙装置
20…磁気ケース
21…排気管
24…有機物分解槽内温度センサ
40…分解灰温度センサ
50…重量計測センサ
51…第1の磁気空気隙間板
52…第2の磁気空気隙間板
53…スクリュー収納溝
203…永久磁石
DESCRIPTION OF SYMBOLS 1 ... Outer box 2 ... Magnetic air tank 3 ... Organic substance decomposition tank 4 ... Flue shielding plate 5 ... Magnetic air supply plate 7 ... Opening plate 8 ... Decomposition ash discharge screw 9 ... Decomposition ash volume depth adjusting screw 10 ... Shut-off rotary valve DESCRIPTION OF SYMBOLS 11 ... Organic substance sensor 12 ... Upper storage tank 13 ... Upper opening / closing lid 14 ... Upper opening / closing lid opening / closing jack 15 ... Lower opening / closing lid 16 ... Magnetic air adjustment valve 17 ... Magnetic air exhauster 18 ... Smoke purifier 20 ... Magnetic case 21 ... Exhaust Tube 24 ... Organic substance decomposition tank temperature sensor 40 ... Decomposition ash temperature sensor 50 ... Weight measurement sensor 51 ... First magnetic air gap plate 52 ... Second magnetic air gap plate 53 ... Screw storage groove 203 ... Permanent magnet

Claims (6)

上面に有機物投入口を、下面に磁気空気供給板を有し、前記有機物投入口から投入される有機物を低温熱分解する中空直方体形状の有機物分解槽と、
前記磁気空気供給板の下部に配置され前記磁気空気供給板を介して前記有機物分解槽に磁気空気を供給する磁気空気槽と、
前記磁気空気槽に磁気空気を供給する空気磁化装置と、
前記有機物分解槽の底面に堆積する分解灰の堆積深さを一定に調整する分解灰堆積深さ調整機構と、
前記有機物分解槽の底面に堆積する余剰の分解灰を排出する分解灰排出機構と、
前記有機物分解槽内で発生するガスを排気するガス排出設備と、
前記分解灰排出機構の分解灰排出口に設置され、大気が前記有機物分解槽に逆流することを防止するために前記分解灰排出機構の分解灰排出口に設置される逆流防止機構と、を有する低温熱分解処理炉。
An organic matter input port on the upper surface, a magnetic air supply plate on the lower surface, and a hollow rectangular parallelepiped-shaped organic matter decomposition tank that thermally decomposes organic matter charged from the organic matter input port,
A magnetic air tank disposed under the magnetic air supply plate and supplying magnetic air to the organic matter decomposition tank through the magnetic air supply plate;
An air magnetizing device for supplying magnetic air to the magnetic air tank;
A decomposition ash deposition depth adjusting mechanism for adjusting the deposition depth of the decomposed ash deposited on the bottom surface of the organic matter decomposition tank to a constant;
A decomposition ash discharge mechanism for discharging excess decomposition ash deposited on the bottom surface of the organic matter decomposition tank;
A gas discharge facility for exhausting gas generated in the organic matter decomposition tank;
A reverse flow prevention mechanism installed at the decomposition ash discharge port of the decomposition ash discharge mechanism and installed at the decomposition ash discharge port of the decomposition ash discharge mechanism in order to prevent air from flowing back to the organic matter decomposition tank Low temperature pyrolysis furnace.
前記分解灰堆積深さ調整機構が、前記磁気空気供給板の一辺と並行に設置される複数本の分解灰体積深さ調整スクリューである請求項1に記載の低温熱分解処理炉。  2. The low-temperature pyrolysis furnace according to claim 1, wherein the cracked ash accumulation depth adjusting mechanism is a plurality of cracked ash volume depth adjusting screws installed in parallel with one side of the magnetic air supply plate. 前記分解灰排出機構が、前記分解灰量調整スクリューの両端下部に、前記分解灰量調整スクリューと直角に設置される分解灰排出スクリューである請求項1または請求項2に記載の低温熱分解処理炉。  3. The low-temperature pyrolysis treatment according to claim 1, wherein the cracked ash discharge mechanism is a cracked ash discharge screw installed at both ends of the cracked ash amount adjusting screw at a right angle to the cracked ash amount adjusting screw. Furnace. 前記逆流防止機構が、前記分解灰排出スクリューの分解灰排出口に設置される遮断回転弁である請求項1から請求項3のいずれか一項に記載の低温熱分解処理炉。  The low temperature pyrolysis furnace according to any one of claims 1 to 3, wherein the backflow prevention mechanism is a shut-off rotary valve installed at a cracked ash discharge port of the cracked ash discharge screw. 前記磁気空気供給板が、
下端から上端に向かって斜め上方に延伸する第1の磁気空気隙間板と、
前記第1の磁気空気隙間板の上端の下側に隙間を隔てて配置される上端から下端に向かって斜め下方に延伸する第2の磁気空気隙間板と、
前記第1の磁気空気隙間板の下端と前記第2の磁気空気隙間板の下端との間に配置され前記分解灰量調整スクリューを格納するスクリュー格納溝と、からなる請求項1から請求項4のいずれか一項に記載の低温熱分解処理炉。
The magnetic air supply plate is
A first magnetic air gap plate extending obliquely upward from the lower end toward the upper end;
A second magnetic air gap plate extending obliquely downward from the upper end to the lower end, with a gap disposed below the upper end of the first magnetic air gap plate;
5. A screw storage groove that is disposed between a lower end of the first magnetic air gap plate and a lower end of the second magnetic air gap plate and stores the cracked ash amount adjusting screw. The low-temperature pyrolysis treatment furnace according to any one of the above.
前記分解灰量調整スクリューは、互いに逆方向に回転する第1の分解灰量調整スクリューと第2の分解灰量調整スクリューとが交互に配置されるものである請求項1から請求項5のいずれか一項に記載の低温熱分解処理炉。  6. The cracked ash amount adjusting screw according to any one of claims 1 to 5, wherein a first cracked ash amount adjusting screw and a second cracked ash amount adjusting screw that are rotated in opposite directions are alternately arranged. A low-temperature pyrolysis furnace according to claim 1.
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Publication number Priority date Publication date Assignee Title
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JP2009113009A (en) * 2007-11-09 2009-05-28 Inretto Kk Gas cleaner, magnetic treatment apparatus, and gas cleaning method
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Publication number Priority date Publication date Assignee Title
JPS5230076A (en) * 1975-09-01 1977-03-07 Kubota Ltd Rotating stocker for incinerator
JPH03260510A (en) * 1990-03-08 1991-11-20 Hitachi Zosen Corp Refuse incinerator
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109174902A (en) * 2018-07-25 2019-01-11 南京格洛特环境工程股份有限公司 The autocatalytic cleavage technique of dioxin in solid waste

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