JPH0145524B2 - - Google Patents
Info
- Publication number
- JPH0145524B2 JPH0145524B2 JP58035476A JP3547683A JPH0145524B2 JP H0145524 B2 JPH0145524 B2 JP H0145524B2 JP 58035476 A JP58035476 A JP 58035476A JP 3547683 A JP3547683 A JP 3547683A JP H0145524 B2 JPH0145524 B2 JP H0145524B2
- Authority
- JP
- Japan
- Prior art keywords
- nozzle
- control device
- flue
- dry distillation
- gas
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock 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 to run boilers and other incinerators (hereinafter simply referred to as incinerators). The present invention relates to improvements in combustion equipment to be operated.
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8Aにのぞむ煙
道先端にバーナーとしての機能を発揮するバーナ
ー部6にノズル6A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 6A was disposed in a burner section 6 functioning as a burner at the tip of the flue extending into the crater 8A of the incinerator 8, and an auxiliary burner 7 was disposed 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6
Aより焼却炉8の火口8Aに向つて燃焼炎を噴出
させ、焼却炉を稼動させるようにしたものであ
る。そして、しばらくした後に、補助バーナー7
の運転を止めるが、このときは、上記バーナー部
6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
過時に燃焼することになる。 In order to operate the incinerator with this device,
First, open the lid 11 of the dry distillation can 1, put fuel such as an old tire into the dry distillation can 1 from the fuel input port 10, ignite it from the ignition port 9, close the lid 11, and supply fuel from the variable air volume blower 3. The dry distilled gas is sent to the nozzle 6A, which has been previously heated with the auxiliary burner 7 until the dry distilled gas is ignited, and the dry distilled gas sent there is heated. At the same time, when the dry distilled gas passes through the nozzle 6A, it is ignited and burned, and the nozzle 6
The incinerator is operated by ejecting combustion flame from A toward the crater 8A of the incinerator 8. Then, after a while, the auxiliary burner 7
However, at this time, the nozzle 6A' arranged in the burner section 6 is sufficiently heated, so from now on, the dry distilled gas passing through the nozzle 6A of the burner section 6 is transferred to the nozzle 6A of the burner section 6. It will burn when passing through.
しかし、従来の方式によるときは、バーナー部
6に配されるノズル6Aの温度を700℃まで上昇
しないと黒煙を発したり、炎が安定せず、その為
補助バーナー7を30分ないし40分程度稼動させな
くてはならず、又消火時も同じようにこれを稼動
しなければならなかつた。 However, when using the conventional method, unless the temperature of the nozzle 6A arranged in the burner part 6 is raised to 700°C, black smoke is emitted and the flame becomes unstable. It had to be operated for a certain amount of time, and it had to be operated in the same way when extinguishing a fire.
本発明は、この不都合を排除するものである。 The present invention eliminates this disadvantage.
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、焼却炉の火
口にのぞむ煙道先端に形成したバーナー部6に、
電源19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ノズル6
Bを配し、且つ上記煙道5中にガス流量検出器1
4、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1に付属する風量可変送風
機3或は、乾溜缶1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. In the burner part 6 formed at the tip of the flue 5 that looks into the crater of the incinerator,
Nozzle 6 consisting of an electrical resistance heating element equipped with a terminal for connecting a circuit supplied with electricity from a power source 19
B, and a gas flow rate detector 1 in the flue 5.
4. Arrange gas component detectors 15, etc., input the detected values detected by each detector, and receive the input signal to send the variable air volume blower 3 attached to the dry distillation can 1 or the dry distillation can 1 A control device 17 that adjusts and operates the stretched roistle 2 is provided outside the flue, and the detector and the control device are connected by a circuit, and the control device 17 and a control device for the variable air volume blower 3 are connected. 18 and the Rostre swing control device 16 are connected through a circuit. Since the present invention is constructed as described above, when it is to be operated, first, the dry distillation can 1 is operated in the conventional manner to generate dry distillation gas, which is directed to the incinerator 8 through the flue 5. Send it out.
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、焼却炉の火口8Aにのぞんでバーナ
ー6としての役割を果たすために配されたノズル
6Bに予め電源19からの電気を供給しておく。
この通電により、ノズル6Bは電気抵抗発熱体で
ある金属により作られているので熱発する。この
発熱は、上記した乾溜ガスがノズル6Bを通過す
る際着火して燃焼するのに十分な温度にまで発熱
させておく。 In order to generate this dry distilled gas, electricity from the power source 19 is supplied in advance to the nozzle 6B, which is placed at the tip of the flue, that is, the crater 8A of the incinerator, and serves as the burner 6. .
Due to this energization, the nozzle 6B generates heat because it is made of metal, which is an electrical resistance heating element. This heat is generated to a temperature sufficient to ignite and burn the above-mentioned dry distilled gas when it passes through the nozzle 6B.
この実施例を示すと、5V〜20Vの電流をノズ
ルに流すことにより3分〜5分で700℃まで加熱
させた。 In this example, the nozzle was heated to 700°C in 3 to 5 minutes by passing a current of 5V to 20V 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6Bにまで達したときは、上記ノズ
ル6Bは、電源19からの通電により十分加熱さ
れているので、上記乾溜ガスが上記ノズル6Bを
通過する際確実に着火して燃焼し、黒煙を発する
ことなく燃焼炎となつて焼却炉8の火口に向つて
噴出され、焼却炉はその機能を十分に果すことが
できた。この燃焼噴出が或る程度継続した後は、
電源からの電気供給を止めても、ノズルは十分加
熱されているので爾後の燃焼噴出には支障はな
い。 Under this condition, when the dry distillation gas generated in the dry distillation tank 1 reaches the nozzle 6B by the air blown from the variable air volume blower 3, the nozzle 6B is energized by the power source 19. Since it is sufficiently heated, the dry distilled gas reliably ignites and burns when passing through the nozzle 6B, becomes a combustion flame without emitting black smoke, and is ejected toward the crater of the incinerator 8. was able to fully fulfill its function. After this combustion eruption continues for a certain amount of time,
Even if the electricity supply from the power source is stopped, the nozzle is sufficiently heated, so there will be no problem with subsequent combustion spewing.
又、本発明の実施でノズルの予熱に費す燃料費
用は従来方式と比べて大幅に節約ができた。この
ようにして、本発明によるときは、燃焼装置を中
途で一時停止するような場合の再稼動には従来方
式と異なり、短時間ですむという長所も併せもつ
ものである。 Further, by implementing the present invention, the fuel cost for preheating the nozzle can be significantly reduced compared to the conventional method. In this way, the present invention also has the advantage that, unlike the conventional method, restarting the combustion apparatus when the combustion apparatus is temporarily stopped midway can be restarted in a short time.
ただ、上記燃焼中に乾溜缶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。 However, if the amount or concentration of gas sent from the dry distiller decreases during the above-mentioned combustion, the combustion calories will decrease, which is expected to cause various problems in combustion in the incinerator.
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おり行なわ
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1内での燃えカスがロスト
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、乾溜缶内に十分空気を送り込むことができな
いの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 the gas or the decrease in the concentration of the 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 burnt residue inside the dry distillation can 1 accumulates on the roaster 2, and as a result, the variable air volume blower 3
This is because the air blown from the dry distillation tank is blocked by the roistle part, and sufficient air cannot be sent into the dry distillation tank, so that reductive combustion within the dry distillation tank is not completely carried out.
しかし、本発明は、上記の如く煙道5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 the gas component detector 15 are arranged in the flue 5 as described above, in the unlikely event that the amount of gas flowing from the dry distillation tank or
When the gas concentration decreases, it can be detected 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 to move the device 16 that swings the roistle 2 to shake the roistle 2. The combustion residue that has accumulated on the dry distillation can is shaken off from the dry distillation can by moving, and the air permeability inside the dry distillation can is improved to improve the combustion of the fuel put into the dry distillation can, and the combustion residue generated inside the dry distillation can is improved. The dry distillation gas can be adjusted 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、前記した焼却炉8の火口8Aにのぞむ煙道
の先端に形成されるバーナー部6に配するノズル
6Bについては、第3図に示すようにノズルの噴
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、ノズル本体の内側に第
4,5図に示すように電気抵抗の大きい金属板を
以て桟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1
9から所定の電流をノズル6Bに流すと、ノズル
6Bに流れた電気は、ノズル本体並にノズル噴口
に張設された金網或はノズル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、ノズルに送りこまれた乾溜ガスはノ
ズルから噴射される際一層着火しやすくなる。 Furthermore, as for the nozzle 6B disposed in the burner section 6 formed at the tip of the flue extending into the crater 8A of the incinerator 8, as shown in FIG. The formed wire mesh X may be stretched, or a metal plate with high electrical resistance may be incorporated inside the nozzle body in the form of a crosspiece Y or a grid Z, as shown in FIGS. 4 and 5. With this configuration, the power supply 1
When a predetermined current is passed through the nozzle 6B from the nozzle 9, the electricity flowing through the nozzle 6B will energize the nozzle body as well as the wire mesh stretched over the nozzle nozzle or the metal plate built into the nozzle body, which will increase the electrical resistance. This generates heat, and the dry distilled gas fed into the nozzle is more likely to ignite when it is injected from the nozzle.
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、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は風量可変送風機の制御装置、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, 14 is a gas flow rate detector, 15 is a gas component detector, 16 17 is a Rostle swing control device, 17 is a Rostle variable air volume blower adjustment operation control device,
18 is a control device for a variable air volume blower, X is a wire mesh made of metal wires, Y is a crosspiece made of metal plates, and Z is a grid made of metal plates.
Claims (1)
すぶ煙道5の、焼却炉の火口にのぞむ煙道先端に
形成したバーナー部6に、電源19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
抗発熱体から成るノズル6B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1
5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
1に付属する風量可変送風機3或は、乾溜缶1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
記制御装置とを回路で結線し、且つ該制御装置1
7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. Connect a circuit that receives electricity from a power source 19 to the burner part 6 formed at the tip of the flue 5 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 of the incinerator. A nozzle 6B made of an electrical resistance heating element equipped with a terminal is disposed in the flue 5, and a gas flow rate detector 14 and a gas component detector 1 are disposed in the flue 5.
5, etc., and input the detected values detected by each detector, and in response to the input signal, the variable air volume blower 3 attached to the dry distillation can 1 or the rostol 2 stretched over the dry distillation can 1 A control device 17 is provided outside the flue, and the detector and the control device are connected by a circuit, and the control device 1
7 and a control device 18 of the variable air volume blower 3 as well as a swing control device 16 of the rostre are connected through a circuit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58035476A JPS59161612A (en) | 1983-03-04 | 1983-03-04 | Combustion device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58035476A JPS59161612A (en) | 1983-03-04 | 1983-03-04 | Combustion device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59161612A JPS59161612A (en) | 1984-09-12 |
JPH0145524B2 true JPH0145524B2 (en) | 1989-10-04 |
Family
ID=12442815
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58035476A Granted JPS59161612A (en) | 1983-03-04 | 1983-03-04 | Combustion device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59161612A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE513063C2 (en) * | 1998-08-21 | 2000-06-26 | Bengt Sture Ershag | Process for the recovery of carbon and hydrocarbon compounds from polymeric material, preferably in the form of discarded tires, by pyrolysis in a pyrolysis reactor |
US8006407B2 (en) * | 2007-12-12 | 2011-08-30 | Richard Anderson | Drying system and method of using same |
JP7142393B2 (en) * | 2019-04-25 | 2022-09-27 | 株式会社日省エンジニアリング | Organic matter processing equipment |
JP7142394B2 (en) * | 2019-06-28 | 2022-09-27 | 株式会社日省エンジニアリング | Organic matter treatment equipment with steam generation function |
-
1983
- 1983-03-04 JP JP58035476A patent/JPS59161612A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS59161612A (en) | 1984-09-12 |
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