JPH0145523B2 - - Google Patents

Info

Publication number
JPH0145523B2
JPH0145523B2 JP58035475A JP3547583A JPH0145523B2 JP H0145523 B2 JPH0145523 B2 JP H0145523B2 JP 58035475 A JP58035475 A JP 58035475A JP 3547583 A JP3547583 A JP 3547583A JP H0145523 B2 JPH0145523 B2 JP H0145523B2
Authority
JP
Japan
Prior art keywords
control device
gas
dry distillation
flue
air volume
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.)
Expired
Application number
JP58035475A
Other languages
Japanese (ja)
Other versions
JPS59161611A (en
Inventor
Goei Nakajima
Shigemi Oono
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.)
TONAMI DENKI ENJINIARINGU KK
Original Assignee
TONAMI DENKI ENJINIARINGU KK
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 TONAMI DENKI ENJINIARINGU KK filed Critical TONAMI DENKI ENJINIARINGU KK
Priority to JP58035475A priority Critical patent/JPS59161611A/en
Publication of JPS59161611A publication Critical patent/JPS59161611A/en
Publication of JPH0145523B2 publication Critical patent/JPH0145523B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/143Feedstock the feedstock being recycled material, e.g. plastics

Landscapes

  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Coke Industry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

【発明の詳細な説明】 この発明は、古タイヤ、廃プラスチツク製品等
を還元燃焼させて、これから乾溜ガスを発生さ
せ、この乾溜ガスを燃料としてボイラー、その他
焼却炉(以下単に焼却炉という)等を稼動させる
燃焼装置の改良に関するものである。
[Detailed Description of the Invention] This invention reduces and burns old tires, waste plastic products, etc. to generate dry distilled gas, and uses this dry distilled gas as fuel for boilers, other incinerators (hereinafter simply referred to as incinerators), etc. This invention relates to improvements to combustion equipment that operate.

従来普通に用いられていた上記の装置の大要
は、第1図に示すとおり、上部に燃料投入口10
とこれを密閉する蓋11を備え、下方に点火口9
を備えてなり、且つ、その下方に風量可変送風機
3を備えて成るとともに内部にはロストル2を配
した乾溜缶1の排気口と焼却炉8の火口8Aとを
煙道5で連継し、焼却炉8の火口にのぞむ煙道先
端にバーナーとしての機能を発揮するノズル6
A′を配し、該ノズル6A′の手前に補助バーナー
7を配して成るものであつた。
As shown in Figure 1, the above-mentioned device that has been commonly used in the past has a fuel inlet 10 at the top.
and a lid 11 that seals this, and an ignition port 9 below.
It is equipped with a variable air volume blower 3 below it, and the exhaust port of the dry distillation can 1, which has a roistle 2 arranged inside, and the crater 8A of the incinerator 8 are connected by a flue 5, A nozzle 6 that functions as a burner is located at the tip of the flue leading into the crater of the incinerator 8.
A' and an auxiliary burner 7 in front of the nozzle 6A'.

この装置を以て焼却炉を稼動するためには、ま
ず、乾溜缶1の蓋11を開いて古タイヤ等の燃料
を燃料投入口10から乾溜缶1中に投入し、これ
を点火口9より着火して蓋11を閉じ、風量可変
送風機3′から給気を行つて乾溜して乾溜ガスを
発生させ、発生した乾溜ガスを、予め、補助バー
ナー7を以て乾溜ガスが発火するまでに加熱して
おいた上記ノズル6Aまで送り、ここに送りこま
れる乾溜ガスを加熱すると同時に上記乾溜ガスが
ノズル6Aを通過する際点火して燃焼し、ノズル
6Aより焼却炉8の火口8Aに向つて火炎を噴出
させ焼却炉を稼動させるようにしたものである。
In order to operate an incinerator using this device, first open the lid 11 of the dry distillation can 1, pour fuel such as an old tire into the dry distillation can 1 through the fuel inlet 10, and ignite it through the ignition port 9. Then, the lid 11 was closed, and air was supplied from the variable air volume blower 3' to perform dry distillation to generate dry distilled gas, and the generated dry distilled gas was heated in advance with the auxiliary burner 7 until the dry distilled gas was ignited. The dry distilled gas is sent to the nozzle 6A, and at the same time, the dry distilled gas is ignited and burned as it passes through the nozzle 6A, and a flame is ejected from the nozzle 6A toward the crater 8A of the incinerator 8. It is designed to operate.

そして、しばらくした後に補助バーナー7の運
転を止めるか、補助バーナー7の運転を止めて
も、この運転を止めるときは上記バーナー部に配
されたノズル6Aが十分に加熱されているので以
後は、このバーナー部6のノズル6Aを通過する
乾溜ガスはバーナー部6のノズル6Aを通過時に
燃焼し焼却炉を継続して稼動することになる。
Then, after a while, the operation of the auxiliary burner 7 is stopped, or even if the operation of the auxiliary burner 7 is stopped, the nozzle 6A arranged in the burner part is sufficiently heated when the operation is stopped. The dry distilled gas passing through the nozzle 6A of the burner section 6 burns when passing through the nozzle 6A of the burner section 6, thereby continuously operating the incinerator.

しかし、従来の装置の欠点は、煙道5中に流れ
る乾溜ガスが、流動中に温度が低下した場合、バ
ーナー部6に達してノズル6Aから噴出されると
きに着火しにくかつたり或は、煙道5の内面にタ
ールを付着させそのため乾溜ガスの流通を疎害す
ることがあつた。
However, the disadvantage of the conventional device is that if the temperature of the dry distilled gas flowing in the flue 5 drops during the flow, it may be difficult to ignite when it reaches the burner section 6 and is ejected from the nozzle 6A. In some cases, tar was deposited on the inner surface of the flue 5, which impeded the flow of the dry distilled gas.

本発明は、従来の欠点を除去するためになされ
た発明であつて、その構成を第2図に示す図示実
施例によつて説明すると、乾溜缶1の排気口と焼
却炉8の火口8Aをむすぶ煙道5の、焼却炉8の
火口8Aにのぞむ煙道先端に形成したバーナー部
6にいたる途中に、電源20からの電気の供給を
うける回路を結線する端子を備えた電気抵抗発熱
体から成る筒体12を配し、且つ上記煙道5中に
ガス流量検出器14、ガス成分検出器15等を配
置し、それぞれの検出器が検出した検出値を入力
して、その入力信号を受けて上記乾溜缶に付属す
る風量可変送風機3或は、乾溜缶に張設されたロ
ストル2を調整稼動するようにした制御装置17
を煙道外に設けて、上記検出器と上記制御装置1
7とを回路で結線し、且つ該制御装置17と風量
可変送風機3の制御装置18並にロストルの揺動
制御装置16とを回路を以て結線したものであ
る。本発明は、上記の如く構成されているので、
これを作動させるときは、まず従来どうりの手順
で乾溜缶1を操作して乾溜ガスを発生させこれを
煙道5を通して焼却炉8に向つて送り出す。
The present invention was made in order to eliminate the drawbacks of the conventional technology, and its configuration will be explained with reference to the illustrated embodiment shown in FIG. From an electric resistance heating element that is provided with a terminal for connecting a circuit that receives electricity from a power source 20, on the way to the burner part 6 formed at the tip of the flue 5 that extends into the crater 8A of the incinerator 8. A cylindrical body 12 consisting of A control device 17 is adapted to adjust and operate the variable air volume blower 3 attached to the dry distillation can or the roistle 2 stretched over the dry distillation can.
is installed outside the flue, and the detector and the control device 1 are connected to each other.
7 are connected by a circuit, and the control device 17 is connected to the control device 18 of the variable air volume blower 3 and the swing control device 16 of the rostol by a circuit. Since the present invention is configured as described above,
To operate this, first, the dry distillation can 1 is operated in the conventional manner to generate dry distillation gas, which is sent through the flue 5 toward the incinerator 8.

この乾溜ガスを発生させるに当つて、煙道の先
端すなわち、焼却炉8の火口8Aにのぞんでバー
ナーとしての役割を果たすために配されたノズル
6Aを予め加熱しておく。この加熱は、上記した
乾溜ガスがノズルを通過する際着火して燃焼する
のに十分な温度にまでたかめておく。
In order to generate this dry distilled gas, a nozzle 6A placed at the tip of the flue, that is, at the crater 8A of the incinerator 8 and serving as a burner, is heated in advance. This heating is performed to raise the temperature to a temperature sufficient to ignite and burn the dry distilled gas as it passes through the nozzle.

この状態の下で、乾溜缶1で発生された乾溜ガ
スが風量可変送風機3から起生される送風によつ
て上記ノズル6Aにまで達したときは、上記ノズ
ル6Aは、十分加熱されているので、上記乾溜ガ
スが上記ノズル6Aを通過する際着火して燃焼
し、燃焼炎となつて焼却炉8の火口8Aに向つて
噴射され焼却炉はその機能を果たすことになる。
Under this condition, when the dry distillation gas generated in the dry distillation tank 1 reaches the nozzle 6A due to the air blown from the variable air volume blower 3, the nozzle 6A is sufficiently heated. When the dry distilled gas passes through the nozzle 6A, it ignites and burns, becoming a combustion flame and being injected toward the crater 8A of the incinerator 8, allowing the incinerator to perform its function.

この燃焼噴射が或る程度継続した後は、電源2
0からの電気供給を止めても、上記ノズル6Aは
十分加熱されているので、爾後の燃焼噴射に支障
を来たすことはない。
After this combustion injection continues for a certain amount of time, the power supply 2
Even if the electricity supply from Nozzle 0 is stopped, the nozzle 6A is sufficiently heated, so that it will not interfere with subsequent combustion injection.

しかも、本発明によるときは、煙道5の途中に
上記した構成の筒体12を配してあるのでこれに
電源20から温度調節装置13を介して通電して
おけば、上記筒体12は電気抵抗によつて発熱す
るので、煙道5中を流れる乾溜ガスがこの筒体1
2を通過するとき、この筒体12によつて加温さ
れ、加温された状態でノズルにまで達する。従つ
てノズルに達した加温された乾溜ガスはノズル6
Aから噴出されるとき確実に着火されることにな
る。又、前記した乾溜ガスは煙道中で加温される
ので、ガス成分からタールが分解してこれが煙道
内面に付着し、それが原因で乾溜ガスの流通を阻
害したりすることはない。
Moreover, according to the present invention, since the cylinder 12 having the above-mentioned structure is disposed in the middle of the flue 5, if the cylinder 12 is energized from the power source 20 via the temperature control device 13, the cylinder 12 can be opened. Since heat is generated due to electrical resistance, the dry distilled gas flowing through the flue 5 is heated by this cylinder 1.
2, it is heated by this cylindrical body 12, and reaches the nozzle in a heated state. Therefore, the heated dry distilled gas that has reached the nozzle is
When ejected from A, it will definitely be ignited. Further, since the above-mentioned dry distillation gas is heated in the flue, tar is not decomposed from the gas components and adheres to the inner surface of the flue, thereby preventing the flow of the dry distillation gas from being obstructed.

また、乾溜ガスの燃焼噴出中に、乾溜缶1から
送られてくるガス量、或はガス濃度が減少したと
きは、その燃焼カロリーが低下し、焼却炉での燃
焼に種々の支障を来たすことが予想される。
Additionally, if the amount of gas sent from the dry distillation tank 1 or the gas concentration decreases during the combustion spout of dry distillation gas, the combustion calories will decrease, causing various problems to combustion in the incinerator. is expected.

このガスの流量の減少或は流れるガス濃度の減
少は、乾溜缶内での還元燃焼が理想どうりに行な
われていないことによるものである。これは、風
量可変送風機3から乾溜缶1内に送風する送風量
が少ないか、或は乾溜缶内での燃えかすがロスト
ル2上に滞積して、その結果、風量可変送風機3
から送風される空気がロストル部分で遮断され
て、乾溜缶1内に十分空気を送り込むことができ
ないで乾溜缶内での還元燃焼が完全に行なわれて
いないことによるものである。
This decrease in the flow rate of gas or the decrease in the concentration of flowing gas is due to the fact that reductive combustion within the dry distillation vessel is not performed as ideally. This is because the amount of air blown into the dry distillation can 1 from the variable air volume blower 3 is small, or the embers inside the dry distillation can accumulate on the roaster 2, and as a result, the variable air volume blower 3
This is because the air blown from the dry distillation vessel 1 is blocked by the roistle portion, and sufficient air cannot be sent into the dry distillation vessel 1, so that reductive combustion within the dry distillation vessel 1 is not completely carried out.

しかし、本発明は、上記の如く煙道にガス流量
検出器14、ガス成分検出器15が配置してある
ので、万一乾溜缶から流れてくるガス量或はガス
濃度が減少したときは、直ちにそれを検出するこ
とができるようになつている。
However, in the present invention, since the gas flow rate detector 14 and gas component detector 15 are arranged in the flue as described above, in the event that the amount of gas flowing from the dry distillation tank or the gas concentration decreases, It is now possible to detect it immediately.

そして、これらの検出器が、上記した状態を検
知したときは、直ちに、これらの検出器と回路を
配して結ばれている制御装置17にその検出値が
入力され、その入力によつて制御装置17が作動
して、風量可変送風機3の制御装置18を作動し
てその回転数を上げて送風量を増すとか、或は、
ロストル2を揺動する装置16をうごかしてロス
トル2を揺動してロストル2上に滞積した燃えか
すをロストル2からふりおとし、乾溜缶内の通気
性をよくして乾溜缶内に投入されている燃料の燃
焼を良好にし、乾溜缶内で発生する乾溜ガスを所
期の流量、濃度に調制することができる。
When these detectors detect the above-mentioned conditions, the detected values are immediately input to the control device 17 connected to these detectors by a circuit, and the control is performed based on the input. The device 17 is activated to activate the control device 18 of the variable air volume blower 3 to increase its rotation speed and increase the amount of air blown, or
The device 16 for shaking the rostle 2 is moved to shake the rostle 2, and the embers accumulated on the rostle 2 are shaken off from the rostle 2, improving the ventilation inside the dry distillation can, and the embers are poured into the dry distillation can. It is possible to improve the combustion of the fuel in the dry distillation tank, and to adjust the flow rate and concentration of the dry distillation gas generated in the dry distillation tank to the desired flow rate and concentration.

又、この作動によつて煙道5を流れるガスの流
量、或は濃度が所期の値に達したときは、これを
また上記検出器が検知し、これを上記制御装置1
7に入力し、その信号をうけた上記制御装置17
が作動して風量可変送風機3の回転数を下げると
か、或はロストル2の揺動を停止する。
Further, when the flow rate or concentration of gas flowing through the flue 5 reaches a desired value due to this operation, the detector detects this again, and the control device 1 detects this.
7, and the control device 17 receives the signal.
is activated to lower the rotational speed of the variable air volume blower 3 or to stop the swinging of the roistle 2.

このようにして、本発明によれば、常に所期の
値のガス量とガス濃度をもつ乾溜ガスを発生、供
給することができる。
In this way, according to the present invention, it is possible to always generate and supply dry distilled gas having the desired gas amount and gas concentration.

又、前記した煙道に配する筒体12については
第3図に示すように筒体12の噴出口に電気抵抗
の大きい金属線を以て形成した金網Xを張設する
とか或は、筒体本体の内側に電気抵抗の大きい金
属板を以て第4図第5図に示すように桟Y或は格
子Z状に組込むように構成してもよい。このよう
に構成することによつて、電源20から所定の電
流を筒体12に流すと、筒体12に流れた電気
は、筒体本体並に筒体噴口に張設された金網或は
筒体本体に組込まれた金属板に通電して、これが
電気抵抗により発熱することになり、筒体12を
通過する乾溜ガスは一層効率よく加温される。
Regarding the cylinder 12 disposed in the flue, as shown in FIG. A metal plate with high electrical resistance may be incorporated inside the structure in the form of a crosspiece Y or a lattice Z as shown in FIGS. 4 and 5. With this configuration, when a predetermined current is passed through the cylinder 12 from the power source 20, the electricity flowing through the cylinder 12 is transferred to the cylinder body as well as the wire mesh or cylinder stretched over the cylinder nozzle. Electricity is applied to the metal plate incorporated in the main body, which generates heat due to electrical resistance, and the dry distilled gas passing through the cylinder 12 is heated more efficiently.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は従来の燃焼炉の大要を示す略図、第2
図は本発明にかゝる燃焼炉の大要を示す略図、第
3,4,5図はバーナー部に配するノズルの構成
を示す略図。 図中、1は乾溜缶、3は風量可変送風機、5は
煙道、6は煙道先端のバーナー部、6Aはバーナ
ー部に配するノズル、8は焼却炉、8Aは焼却炉
の火口、12は筒体、20は電源、14はガス流
量検出器、15はガス成分検出器、16はロスト
ルの揺動制御装置、17はロストル、風量可変送
風機の調整稼動制御装置、18は風量可変送風
機、Xは金属線で構成した金網、Yは金属板で構
成した桟、Zは金属板で構成した格子。
Figure 1 is a schematic diagram showing the outline of a conventional combustion furnace, Figure 2
The figure is a schematic diagram showing the outline of the combustion furnace according to the present invention, and Figures 3, 4, and 5 are schematic diagrams showing the configuration of the nozzle arranged in the burner section. In the figure, 1 is a dry distillation can, 3 is a variable air volume blower, 5 is a flue, 6 is a burner section at the tip of the flue, 6A is a nozzle arranged in the burner section, 8 is an incinerator, 8A is a crater of the incinerator, 12 1 is a cylinder body, 20 is a power source, 14 is a gas flow rate detector, 15 is a gas component detector, 16 is a swing control device for Rostr, 17 is an adjustment operation control device for Rostr, a variable air volume blower, 18 is a variable air volume blower, X is a wire mesh made of metal wire, Y is a crosspiece made of metal plates, and Z is a lattice made of metal plates.

Claims (1)

【特許請求の範囲】[Claims] 1 乾溜缶1の排気口と焼却炉8の火口8Aをむ
すぶ煙道5の、焼却炉8の火口8Aにのぞむ煙道
先端に形成したバーナー部6にいたる途中に、電
源20からの電気の供給をうける回路を結線する
端子を備えた電気抵抗発熱体から成る筒体12を
配し、且つ上記煙道5中にガス流量検出器14、
ガス成分検出器15等を配置し、それぞれの検出
器が検出した検出値を入力して、その入力信号を
受けて上記乾溜缶に付属する風量可変送風機3或
は、乾溜缶に張設されたロストル2を調整稼動す
るようにした制御装置17を煙道外に設けて、上
記検出器と上記制御装置17とを回路で結線し、
且つ該制御装置17と風量可変送風機3の制御装
置18並にロストルの揺動制御装置16とを回路
を以て結線したことを特徴とする燃焼装置。
1 Electricity is supplied from a power source 20 to the burner part 6 formed at the tip of the flue that connects the exhaust port of the dry distillation can 1 and the crater 8A of the incinerator 8, and which looks into the crater 8A of the incinerator 8. A cylindrical body 12 made of an electrical resistance heating element equipped with a terminal for connecting a circuit receiving the gas is disposed, and a gas flow rate detector 14 is disposed in the flue 5.
Gas component detectors 15, etc. are arranged, and the detection values detected by each detector are input, and in response to the input signal, the variable air volume blower 3 attached to the dry distillation can or the variable air volume blower 3 attached to the dry distillation can is A control device 17 that adjusts and operates the rostre 2 is provided outside the flue, and the detector and the control device 17 are connected by a circuit,
A combustion apparatus characterized in that the control device 17, the control device 18 of the variable air volume blower 3, and the swing control device 16 of the rostol are connected through a circuit.
JP58035475A 1983-03-04 1983-03-04 Combustion device Granted JPS59161611A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58035475A JPS59161611A (en) 1983-03-04 1983-03-04 Combustion device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58035475A JPS59161611A (en) 1983-03-04 1983-03-04 Combustion device

Publications (2)

Publication Number Publication Date
JPS59161611A JPS59161611A (en) 1984-09-12
JPH0145523B2 true JPH0145523B2 (en) 1989-10-04

Family

ID=12442793

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58035475A Granted JPS59161611A (en) 1983-03-04 1983-03-04 Combustion device

Country Status (1)

Country Link
JP (1) JPS59161611A (en)

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* Cited by examiner, † Cited by third party
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US8006407B2 (en) * 2007-12-12 2011-08-30 Richard Anderson Drying system and method of using same
CN113048493B (en) * 2021-03-09 2022-12-13 北京京仪自动化装备技术股份有限公司 Semiconductor waste gas treatment device and treatment method

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US11027011B2 (en) 2013-03-15 2021-06-08 The Trustees Of The University Of Pennsylvania Vaccines with biomolecular adjuvants

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