JP2005265197A - Operation method for pyrolizing facility and pyrolizing facility - Google Patents

Operation method for pyrolizing facility and pyrolizing facility Download PDF

Info

Publication number
JP2005265197A
JP2005265197A JP2004073683A JP2004073683A JP2005265197A JP 2005265197 A JP2005265197 A JP 2005265197A JP 2004073683 A JP2004073683 A JP 2004073683A JP 2004073683 A JP2004073683 A JP 2004073683A JP 2005265197 A JP2005265197 A JP 2005265197A
Authority
JP
Japan
Prior art keywords
gas
rotary furnace
thermal decomposition
exhaust
furnace
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.)
Pending
Application number
JP2004073683A
Other languages
Japanese (ja)
Inventor
Yoshiyuki Kashiwagi
佳行 柏木
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.)
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
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 Meidensha Corp, Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Corp
Priority to JP2004073683A priority Critical patent/JP2005265197A/en
Publication of JP2005265197A publication Critical patent/JP2005265197A/en
Pending legal-status Critical Current

Links

Images

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
    • Y02P10/00Technologies related to metal processing
    • Y02P10/10Reduction of greenhouse gas [GHG] emissions
    • Y02P10/143Reduction of greenhouse gas [GHG] emissions of methane [CH4]

Abstract

<P>PROBLEM TO BE SOLVED: To early detect leakage of decomposition gas from a seal part and prevent leakage of decomposition gas from the seal part. <P>SOLUTION: A gas sensor for detecting at least one kind of decompositon gas component is provided in the vicinity of an atmospheric air side of the seal parts 4, 6. Opening of an exhaust damper of an exhaust blower for exhausting combustion exhaust gas from a decomposition gas combustion furnace 16 for burning gas from a rotary furnace is increased to increase displacement based on a detection signal of the gas sensor, and pressure in the rotary furnace is reduced to prevent leakage of gas from the seal parts 4, 6. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

この発明は、各種の有機性物質を含む原料(各種の有機物を含む固形物、各種汚泥、土壌等)を熱分解反応により減容、減量化する設備に係り、特に回転炉を使用した熱分解手段におけるシール部から熱分解ガスの漏洩があった場合における熱分解施設の運転方法及び熱分解施設に関するものである。   TECHNICAL FIELD The present invention relates to equipment for reducing and reducing the volume of raw materials containing various organic substances (solids containing various organic substances, various sludges, soils, etc.) by a thermal decomposition reaction, and in particular, thermal decomposition using a rotary furnace. The present invention relates to a method for operating a pyrolysis facility and a pyrolysis facility when pyrolysis gas leaks from a seal portion in the means.

各種原料(被処理物)である各種有機性物質、各種汚泥、土壌、土砂等を、間接加熱による還元性の雰囲気において熱分解反応を行い、乾燥、炭化、灰化、浄化等の加工を加えることが行われている。回転炉の内部に原料を収納して間接加熱により原料を熱分解する熱分解手段を使用する場合、回転炉の両端部には、シール手段を介して静止ボックス(原料の投入、加工品の排出)を備えている。シール手段は極めて重要であり、劣化すると、外部から空気が浸入し、内部の原料が発火する可能性がある。又、内部の分解ガスが漏洩し、同時に臭気も漏洩する可能性がある。従って、シール手段のメンテナンス(定期的な増し締め、交換)等により、シール機能の維持が図られている。   Various raw materials (materials to be treated), various organic substances, various sludges, soil, earth and sand, etc. are subjected to thermal decomposition reaction in a reducing atmosphere by indirect heating, and processing such as drying, carbonization, ashing, purification is added Things have been done. When using pyrolysis means that contains raw materials inside the rotary furnace and pyrolyzes the raw materials by indirect heating, stationary boxes (feeding of raw materials and discharging processed products) are provided at both ends of the rotary furnace via sealing means. ). The sealing means is extremely important, and when it deteriorates, air may enter from the outside and the internal raw materials may ignite. In addition, internal decomposition gas may leak, and odor may also leak at the same time. Therefore, the sealing function is maintained by maintenance (periodic retightening and replacement) of the sealing means.

このガスの漏洩を防止するものとして、特許文献1が知られている。当該技術は、シール部を包囲してシール部から漏洩した分解ガスを捕集するガス捕集手段を設け、捕集したガスを別室に導入する技術である。又、回転炉内の圧力は、負圧で運転していれば、内部の分解ガスがシール部から漏洩することはないが、発生ガス量が急激に多くなった場合には、回転炉内の圧力は正圧となり、漏洩することとなった。
特開平10−206021号公報
Patent document 1 is known as what prevents the leakage of this gas. This technique is a technique for providing gas collecting means for surrounding the seal portion and collecting the decomposition gas leaked from the seal portion, and introducing the collected gas into a separate chamber. Moreover, if the pressure in the rotary furnace is operating at a negative pressure, the internal cracked gas will not leak from the seal part, but if the amount of generated gas increases rapidly, The pressure became positive and leaked.
Japanese Patent Laid-Open No. 10-206021

上記したように、シール部から漏洩したガスを捕集して処理することは、悪臭等を拡散させない有効な手段であるが、漏洩を早期に発見して熱分解施設の運転制御を行うことも重要である。シール部からガスが漏洩することは、発生ガス量が多くなっていることであり、ガス捕集手段でガスを捕集して燃焼炉に導入して燃焼させるだけでは、安定した分解ガス漏洩対策を行うことができない。   As described above, collecting and processing the gas leaked from the seal portion is an effective means that does not diffuse malodors, etc., but it is also possible to detect the leak early and control the operation of the thermal decomposition facility. is important. Gas leakage from the seal part means that the amount of generated gas is large. By simply collecting the gas with the gas collecting means, introducing it into the combustion furnace and burning it, a stable countermeasure against cracked gas leakage is possible. Can not do.

発明者は、分解ガス漏洩の早期発見と早期対策を実施する手段を創出した。即ち、シール部の気体成分を捕集し、この気体の成分変化を検知することにより、ガスが漏洩していることを知ることができることに着目した。又、シール部から分解ガスが漏洩していることを早期に検知し、操作員に早期に知らせて施設の状況と漏洩対策が行えるように、早期発見と早期対策を実施することが必要である。即ち、シール部近傍にガスセンサを設け、このガスセンサにより原料より発生した分解ガス成分を検知する。この検知できるということは、回転炉内の発生ガス量が急激に増加し、回転炉内の圧力が上昇していることであり、減圧するためにはガスの増加量に見合ったガス量を排気することが必要である。   The inventor has created a means for early detection of cracked gas leaks and early countermeasures. That is, attention was paid to the fact that the gas can be known to leak by collecting the gas component of the seal portion and detecting the change in the gas component. In addition, early detection and early countermeasures are required so that cracked gas leaks from the seal part can be detected early and the operator can be informed early so that the situation of the facility and leakage countermeasures can be taken. . That is, a gas sensor is provided in the vicinity of the seal portion, and a cracked gas component generated from the raw material is detected by this gas sensor. This detection means that the amount of gas generated in the rotary furnace has increased rapidly and the pressure in the rotary furnace has increased, and in order to reduce the pressure, the amount of gas commensurate with the amount of gas increase is exhausted. It is necessary to.

そのためには、排気ブロアの後段に備えている排気ダンパを制御(開度を大きくする)して、ガス燃焼炉及び回転炉内の圧力を低下させるために、排気量を多くした制御をすることが必要であることに着目した。さらには、回転炉から分解ガスを吸引するエゼクタの搬送力を大きくすることに着目した。このようなことに着目することにより、分解ガス漏洩の早期発見と早期対策が実施できることに着目した。   To do so, control the exhaust damper in the rear stage of the exhaust blower (increase the opening) and control the exhaust volume to increase the pressure in the gas combustion furnace and rotary furnace. Focused on the need for Furthermore, we focused on increasing the transport force of the ejector that sucks the cracked gas from the rotary furnace. Focusing on this fact, we focused on the fact that early detection and early countermeasures for cracked gas leakage can be implemented.

この発明は上記のような課題を解決するために成されたものであり、シール部からの分解ガスの漏洩を早期に発見するとともに、シール部からのガスの漏洩を防止することができる熱分解施設の運転方法及び熱分解施設を得ることを目的とする。   The present invention has been made to solve the above-described problems, and is capable of detecting the leakage of cracked gas from the seal portion at an early stage and capable of preventing gas leak from the seal portion. The purpose is to obtain a facility operating method and a pyrolysis facility.

この発明の請求項1に係る熱分解施設の運転方法は、回転炉の両端部にシール部を介して静止ボックスを設け、回転炉の内部に原料を収納して間接加熱により原料を熱分解する熱分解手段を備えた熱分解施設の運転方法において、シール部の大気側近傍に熱分解により発生する分解ガス成分の少なくとも1種類を検知するガスセンサを設けるとともに、回転炉からのガスを燃焼するガス燃焼手段を設け、ガスセンサの検知信号に基づき、ガス燃焼手段からの燃焼排ガスを排出する排気ブロアの排気ダンパのダンパ開度を大きくして排気量を大きくし、回転炉内圧力を減圧するものである。   In the operation method of the thermal decomposition facility according to the first aspect of the present invention, stationary boxes are provided at both ends of the rotary furnace via seals, the raw material is stored inside the rotary furnace, and the raw material is pyrolyzed by indirect heating. In a method for operating a thermal decomposition facility equipped with a thermal decomposition means, a gas sensor for detecting at least one kind of decomposition gas component generated by thermal decomposition is provided in the vicinity of the atmosphere side of the seal portion, and gas for combusting gas from a rotary furnace Combustion means is provided, and based on the detection signal of the gas sensor, the damper opening of the exhaust blower that discharges the combustion exhaust gas from the gas combustion means is increased to increase the exhaust amount, and the rotary furnace pressure is reduced. is there.

請求項2に係る熱分解施設の運転方法は、回転炉の両端部にシール部を介して静止ボックスを設け、回転炉の内部に原料を収納して間接加熱により原料を熱分解する熱分解手段を備えた熱分解施設の運転方法において、シール部の大気側近傍に熱分解により発生する分解ガス成分の少なくとも1種類を検知するガスセンサを設けるとともに、回転炉内からのガスを燃焼するガス燃焼手段を設け、ガスセンサの検知信号に基づき、回転炉内のガスをガス燃焼炉に導入するエゼクタの送風量を大きくし、回転炉内圧力を減圧するものである。   The operation method of the thermal decomposition facility according to claim 2 is a thermal decomposition means in which stationary boxes are provided at both ends of the rotary furnace via seals, the raw material is stored inside the rotary furnace, and the raw material is thermally decomposed by indirect heating. And a gas combustion means for combusting a gas from the rotary furnace while providing a gas sensor for detecting at least one kind of cracked gas component generated by pyrolysis near the atmosphere side of the seal portion And the amount of air blown by the ejector for introducing the gas in the rotary furnace into the gas combustion furnace is increased based on the detection signal of the gas sensor, and the pressure in the rotary furnace is reduced.

請求項3に係る熱分解施設は、回転炉の両端部にシール部を介して静止ボックスを設け、回転炉の内部に原料を収納して間接加熱により原料を熱分解する熱分解手段と、熱分解により発生した分解ガスを燃焼するガス燃焼手段と、ガス燃焼手段からの燃焼排ガスを排気する排気ブロアと、シール部の大気側近傍に設けられ、分解ガス成分の少なくとも1種類を検知するガスセンサと、排気ブロアの排気量を制御し、ガスセンサの検知信号に基づき、ダンパ開度を大きく制御される排気ダンパとを備えたものである。   The pyrolysis facility according to claim 3 is provided with a stationary box at both ends of the rotary furnace via seals, a thermal decomposition means for storing the raw material in the rotary furnace and thermally decomposing the raw material by indirect heating, A gas combustion means for burning the cracked gas generated by the decomposition, an exhaust blower for exhausting the combustion exhaust gas from the gas combustion means, a gas sensor provided in the vicinity of the atmosphere side of the seal portion and detecting at least one kind of the cracked gas component; And an exhaust damper that controls the exhaust amount of the exhaust blower and largely controls the damper opening based on the detection signal of the gas sensor.

請求項4に係る熱分解施設は、分解ガスを回転炉からガス燃焼手段に導入するとともに、ガスセンサの検知信号に基づき送風量が制御されるエゼクタを設けたものである。   The thermal decomposition facility according to claim 4 is provided with an ejector for introducing the cracked gas from the rotary furnace to the gas combustion means and for controlling the air flow rate based on the detection signal of the gas sensor.

請求項5に係る熱分解施設は、ガスセンサの検知信号に基づき、警報を発信する警報装置を設けたものである。   The pyrolysis facility according to claim 5 is provided with an alarm device for issuing an alarm based on the detection signal of the gas sensor.

以上のようにこの発明によれば、シール部の大気側近傍に熱分解により発生する分解ガス成分の少なくとも1種類を検知するガスセンサを設けており、シール部からの分解ガスの漏洩を早期に発見することができる。又、ガスセンサからの検知信号を受けて、警報を発信するようにしており、これによっても分解ガスの漏洩を早期に発見することができる。又、ガスセンサの検知信号に基づき、ガス燃焼手段からの燃焼排ガスを排出する排気ブロアの排気ダンパのダンパ開度を大きくしており、これによって排気量が増大し、回転炉内の圧力が減圧されて、シール部からのガスの漏洩を防止することができる。また、ガスセンサの検知信号に基づき、回転炉内のガスをガス燃焼炉に導入するエゼクタの送風量を増大しており、これによって回転炉内の圧力を減圧することができ、シール部からのガスの漏洩を防止することができる。   As described above, according to the present invention, the gas sensor for detecting at least one kind of decomposition gas component generated by thermal decomposition is provided in the vicinity of the atmosphere side of the seal portion, and the leak of the decomposition gas from the seal portion is detected early. can do. In addition, an alarm is issued in response to a detection signal from the gas sensor, so that a leak of cracked gas can be detected at an early stage. Also, the damper opening of the exhaust damper of the exhaust blower that discharges the combustion exhaust gas from the gas combustion means is increased based on the detection signal of the gas sensor, thereby increasing the exhaust amount and reducing the pressure in the rotary furnace. Thus, leakage of gas from the seal portion can be prevented. In addition, based on the detection signal of the gas sensor, the amount of air blown by the ejector that introduces the gas in the rotary furnace into the gas combustion furnace is increased, whereby the pressure in the rotary furnace can be reduced, and the gas from the seal portion can be reduced. Leakage can be prevented.

以下、この発明を実施するための最良の形態を図面とともに説明する。図1はこの発明の実施最良形態による熱分解施設の構成図を示し、1は原料が供給される回転炉であり、被処理物を間接加熱により乾燥処理、熱分解処理することが可能であり、回転炉1の周囲には回転炉1を外部から加熱する外部加熱手段2が設けられ、外部加熱手段2内には熱風炉3から熱風ガスが導入され、この熱風ガスは回転炉1を外部加熱した後、排出、循環される。回転炉1と外部加熱手段2とにより回転加熱処理炉が形成され、乾燥炉(加熱熱風温度300〜450℃)、炭化炉(加熱熱風温度400〜650℃)等として利用される。   The best mode for carrying out the present invention will be described below with reference to the drawings. FIG. 1 is a configuration diagram of a thermal decomposition facility according to the best mode of the present invention. Reference numeral 1 denotes a rotary furnace to which raw materials are supplied, and it is possible to dry and thermally decompose a workpiece by indirect heating. An external heating means 2 for heating the rotary furnace 1 from the outside is provided around the rotary furnace 1, and hot air gas is introduced into the external heating means 2 from the hot air furnace 3. After heating, it is discharged and circulated. A rotary heat treatment furnace is formed by the rotary furnace 1 and the external heating means 2, and is used as a drying furnace (heating hot air temperature 300 to 450 ° C.), a carbonizing furnace (heating hot air temperature 400 to 650 ° C.), and the like.

回転炉1の一端側にはシール部4を介して被処理物の投入ボックス(静止ボックス)5が設けられ、回転炉1の他端側には同じくシール部6を介して排出ボックス(静止ボックス)7が設けられる。又、回転炉1の両端側には環状の突出部1a,1bが設けられ、突出部1a,1bは回転支持ローラ8,9により回転自在に支持される。回転炉1における突出部1bの端部側にはスプロケット10が設けられ、スプロケット10に係合されたチェーン11は駆動源であるモータ12にに取り付けられたスプロケット13と係合する。   An input box (stationary box) 5 to be processed is provided on one end side of the rotary furnace 1 via a seal portion 4, and a discharge box (stationary box) is also provided on the other end side of the rotary furnace 1 via a seal portion 6. ) 7 is provided. In addition, annular protrusions 1 a and 1 b are provided at both ends of the rotary furnace 1, and the protrusions 1 a and 1 b are rotatably supported by rotation support rollers 8 and 9. A sprocket 10 is provided on the end side of the protruding portion 1b in the rotary furnace 1, and the chain 11 engaged with the sprocket 10 engages with a sprocket 13 attached to a motor 12 as a drive source.

投入ボックス5から投入された被処理物はガイド14を介して回転炉1内に導入される。回転炉1はモータ12により回転駆動され、回転炉1内に導入された被処理物は攪拌されながら排出側へ移送される。回転炉1内は熱風ガスにより所定温度に加熱され、被処理物は間接加熱により乾燥(水分除去)されて乾燥物となり、乾燥物はさらに間接加熱により熱分解処理(炭化処理)されて炭化物となり、これらの乾燥物や炭化物は排出ボックス7を介して処理物として取り出される。又、回転炉1内で発生した熱分解ガス等はエゼクタ15により排出ボックス7から吸引されて取り出され、分解ガス燃焼炉16に送入され、燃焼浄化される。   An object to be processed introduced from the introduction box 5 is introduced into the rotary furnace 1 through the guide 14. The rotary furnace 1 is rotationally driven by a motor 12, and the workpiece introduced into the rotary furnace 1 is transferred to the discharge side while being stirred. The inside of the rotary furnace 1 is heated to a predetermined temperature by hot air gas, the object to be processed is dried by indirect heating (moisture removal) to become a dried substance, and the dried substance is further pyrolyzed (carbonized) by indirect heating to become a carbide. These dried products and carbides are taken out as processed products through the discharge box 7. Further, pyrolysis gas and the like generated in the rotary furnace 1 are sucked out of the discharge box 7 by the ejector 15 and taken out, and sent to the cracked gas combustion furnace 16 for combustion purification.

又、シール部4,6を包囲して捕集ダクト17,18が設けられ、シール部4,6から漏洩した分解ガスを捕集する。また、シール部4,6の大気側近傍、ここでは捕集ダクト17,18にはガスセンサ19,20が設けられる。ガスセンサ19,20は分解ガス成分の少なくとも1種類を検知する。分解ガス成分は原料によって種々異なり、例えば炭化水素(メタン、エチレン、アセチレン等)、水素、NOx、SOx、CO、CO2等であるが、事前に調査し、例えば検知対象成分をCOと定める。ガスセンサ19,20がシール部4,6からの分解ガスの漏洩を検知すると、この検知信号は警報装置21へ送られ、ブザーが鳴らされたり、あるいは監視画面にガス漏れが表示される。なお、ガスセンサ19,20としては、複数種類を設けてもよく、複数箇所に設けてもよい。   Further, collection ducts 17 and 18 are provided so as to surround the seal portions 4 and 6, and the decomposition gas leaked from the seal portions 4 and 6 is collected. Gas sensors 19 and 20 are provided in the vicinity of the atmosphere of the seal portions 4 and 6, here in the collection ducts 17 and 18. The gas sensors 19 and 20 detect at least one kind of cracked gas component. The cracked gas components vary depending on the raw materials, and are, for example, hydrocarbons (methane, ethylene, acetylene, etc.), hydrogen, NOx, SOx, CO, CO2, and the like. When the gas sensors 19 and 20 detect the leakage of cracked gas from the seal portions 4 and 6, this detection signal is sent to the alarm device 21, and a buzzer sounds or a gas leak is displayed on the monitoring screen. The gas sensors 19 and 20 may be provided in a plurality of types or in a plurality of locations.

分解ガス燃焼炉16からの燃焼排ガスは熱交換機22によって冷却され、排気ブロア24によってバグフィルタ23を介して排出される。この際、ガスセンサ19,20のガス漏れ検知信号を受けて、排気ブロア24の排気ダンパ25の開度を大きくし、分解ガス燃焼炉16からの排気量を大きくして、回転炉1内の圧力を低下させ、シール部4,6からの分解ガスの漏洩を防止する。回転炉1内の圧力は通常負圧(例えば、−8〜−3mmH2O)であるが、分解ガスが急激に発生した場合や、パッキンが劣化した場合には、分解ガスがパッキン部分から大気中に漏洩し、臭気を飛散させる。このような場合、上記のように排気量を大きくして回転炉1内の圧力を低下させることにより、分解ガスの漏洩を防止する。また、回転炉1内の減圧は、回転炉1内のガスを分解ガス燃焼炉16に送入するエゼクタ15の送風量を、ガスセンサ19,20のガス漏洩検知信号を受けて大きくすることによっても、達成することができる。   The combustion exhaust gas from the cracked gas combustion furnace 16 is cooled by the heat exchanger 22 and discharged through the bag filter 23 by the exhaust blower 24. At this time, the gas leak detection signal of the gas sensors 19 and 20 is received, the opening of the exhaust damper 25 of the exhaust blower 24 is increased, the amount of exhaust from the cracked gas combustion furnace 16 is increased, and the pressure in the rotary furnace 1 is increased. And the leakage of cracked gas from the seal portions 4 and 6 is prevented. The pressure in the rotary furnace 1 is usually a negative pressure (for example, −8 to −3 mmH 2 O). However, when the cracked gas is suddenly generated or when the packing is deteriorated, the cracked gas enters the atmosphere from the packing portion. Leaks and disperses odor. In such a case, leakage of cracked gas is prevented by increasing the displacement and reducing the pressure in the rotary furnace 1 as described above. Further, the pressure in the rotary furnace 1 can be reduced by increasing the amount of air blown from the ejector 15 that feeds the gas in the rotary furnace 1 to the cracked gas combustion furnace 16 in response to the gas leak detection signals from the gas sensors 19 and 20. Can be achieved.

図2は図1の要部縦断拡大図を示し、排出ボックス7の内壁部7aには回転炉1の端部が挿通される筒部7bが形成され、回転炉1にも筒部7bの外周側に位置する筒部1cが形成され、筒部1c,7b間にはグランドパッキン26が配設され、またセラミックスからなる補助シール部材27を介してパッキン押さえ28が筒部1cに取り付けられ、また排出ボックス7の内壁部7aとパッキン押さえ28との間にもセラミックスからなる補助シール部材29が配設され、これらによってシール部6が形成される。又、このシール部6を覆って捕集ダクト18が設けられ、グランドパッキン26から漏れ出た分解ガスは捕集ダクト18により捕集される。捕集ダクト18にはガスセンサ20が設けられ、捕集されたガスの成分を検知する。   FIG. 2 shows an enlarged vertical cross-sectional view of the main part of FIG. 1. A cylindrical part 7 b into which the end of the rotary furnace 1 is inserted is formed on the inner wall part 7 a of the discharge box 7. A cylindrical portion 1c located on the side is formed, a gland packing 26 is disposed between the cylindrical portions 1c and 7b, and a packing presser 28 is attached to the cylindrical portion 1c via an auxiliary seal member 27 made of ceramics. An auxiliary seal member 29 made of ceramics is also disposed between the inner wall portion 7a of the discharge box 7 and the packing presser 28, and the seal portion 6 is formed thereby. A collection duct 18 is provided so as to cover the seal portion 6, and the decomposition gas leaking from the gland packing 26 is collected by the collection duct 18. A gas sensor 20 is provided in the collection duct 18 to detect a component of the collected gas.

図3(a)は排気ダンパ25の開度制御による分解ガス燃焼炉16からの燃焼排ガスの流量の調整を示し、排気ブロア24は一定回転数で運転し、ガスセンサ19,20によりガス漏れが検出された場合には排気ダンパ25の開度を大きくし、排出風量を大きくする。これにより、分解ガス燃焼炉16内の圧力を低下させ、回転炉1内の圧力も低下させて、シール部4,6からの分解ガスの漏洩を防止する。又、図3(b)の場合には、ガスセンサ19,20によりシール部4,6からのガス漏れが検出された場合、モータ15aを有するエゼクタ15の導入ダンパ30の開度を大きくし、回転炉1から配管31を介した分解ガス燃焼炉16への導入風量を大きくし、これにより回転炉1内の圧力を低下させ、シール部4,6からの分解ガスの漏洩を防止する。   3A shows adjustment of the flow rate of the combustion exhaust gas from the cracked gas combustion furnace 16 by controlling the opening degree of the exhaust damper 25, the exhaust blower 24 is operated at a constant rotational speed, and gas leaks are detected by the gas sensors 19, 20. If so, the opening degree of the exhaust damper 25 is increased to increase the exhaust air volume. As a result, the pressure in the cracked gas combustion furnace 16 is lowered, and the pressure in the rotary furnace 1 is also lowered, thereby preventing the cracked gas from leaking from the seal portions 4 and 6. In the case of FIG. 3B, when the gas sensors 19 and 20 detect gas leakage from the seal portions 4 and 6, the opening degree of the introduction damper 30 of the ejector 15 having the motor 15a is increased to rotate. The amount of air introduced from the furnace 1 to the cracked gas combustion furnace 16 via the pipe 31 is increased, thereby reducing the pressure in the rotary furnace 1 and preventing leakage of cracked gas from the seal portions 4 and 6.

上記したように、排気ダンパ25の開度制御及び導入ダンパ30の開度制御をガスセンサ19,20の検知信号を受けて自動的に行ったが、これらの開度制御を手動操作により行ってもよい。手動操作の場合には、手動により開度設定値の変更を行う。   As described above, the opening degree control of the exhaust damper 25 and the opening degree control of the introduction damper 30 are automatically performed in response to the detection signals of the gas sensors 19 and 20, but the opening degree control may be performed manually. Good. In the case of manual operation, the opening setting value is changed manually.

上記した実施最良形態においては、シール部の大気側近傍に分解ガスの少なくとも1種類を検知するガスセンサを設けており、シール部4,6からのガス漏洩を早期に発見することができる。又ガスセンサの検知信号を受けて警報を発信する警報装置を設けており、これによっても早期発見が可能となる。又、ガスセンサの検知信号に基づき、分解ガス燃焼炉16からの燃焼排ガスを排出する排気ブロアの排気ダンパの開度を大きくして排気量を大きくし、回転炉内の圧力を減圧しており、シール部4,6からのガス漏洩を防止することができる。又、ガスセンサの検知信号に基づき、回転炉1内のガスを分解ガス燃焼炉16に導入するエゼクタ15の送風量を増大するようにしており、これによって回転炉1内の圧力が減圧され、シール部4,6からのガス漏洩が防止される。   In the above-described best embodiment, a gas sensor for detecting at least one kind of cracked gas is provided in the vicinity of the atmosphere of the seal portion, so that gas leakage from the seal portions 4 and 6 can be detected at an early stage. In addition, an alarm device for receiving an alarm signal from the gas sensor and providing an alarm is provided, which also enables early detection. Further, based on the detection signal of the gas sensor, the opening amount of the exhaust blower of the exhaust blower for discharging the combustion exhaust gas from the cracked gas combustion furnace 16 is increased to increase the exhaust amount, and the pressure in the rotary furnace is reduced. Gas leakage from the seal portions 4 and 6 can be prevented. Further, based on the detection signal of the gas sensor, the amount of air blown from the ejector 15 for introducing the gas in the rotary furnace 1 into the cracked gas combustion furnace 16 is increased, whereby the pressure in the rotary furnace 1 is reduced and the seal is sealed. Gas leakage from the parts 4 and 6 is prevented.

この発明の実施最良形態による熱分解施設の構成図である。It is a block diagram of the thermal decomposition facility by this embodiment best mode. 図1の要部縦断拡大図である。It is a principal part longitudinal cross-sectional enlarged view of FIG. この発明の実施最良形態による排気ブロア及びエゼクタによる燃焼排ガス及び分解ガスの風量調整の説明図である。It is explanatory drawing of the air volume adjustment of the combustion exhaust gas and cracked gas by the exhaust blower and ejector by this Embodiment best mode.

符号の説明Explanation of symbols

1…回転炉
2…外部加熱手段
4,6…シール部
5,7…静止ボックス
15…エゼクタ
16…分解ガス燃焼炉
17,18…捕集ダクト
19,20…ガスセンサ
21…警報装置
24…排気ブロア
25…排気ダンパ
30…導入ダンパ
DESCRIPTION OF SYMBOLS 1 ... Rotary furnace 2 ... External heating means 4, 6 ... Seal part 5, 7 ... Static box 15 ... Ejector 16 ... Decomposition gas combustion furnace 17, 18 ... Collection duct 19, 20 ... Gas sensor 21 ... Alarm device 24 ... Exhaust blower 25 ... Exhaust damper 30 ... Introduction damper

Claims (5)

回転炉の両端部にシール部を介して静止ボックスを設け、回転炉の内部に原料を収納して間接加熱により原料を熱分解する熱分解手段を備えた熱分解施設の運転方法において、シール部の大気側近傍に熱分解により発生する分解ガス成分の少なくとも1種類を検知するガスセンサを設けるとともに、回転炉からのガスを燃焼するガス燃焼手段を設け、ガスセンサの検知信号に基づき、ガス燃焼手段からの燃焼排ガスを排出する排気ブロアの排気ダンパのダンパ開度を大きくして排気量を大きくし、回転炉内圧力を減圧することを特徴とする熱分解施設の運転方法。   In the operation method of the thermal decomposition facility, the sealing portion is provided with a stationary box at both ends of the rotary furnace via the seal portion, and the thermal furnace is provided with a thermal decomposition means for storing the raw material in the rotary furnace and thermally decomposing the raw material by indirect heating. A gas sensor for detecting at least one kind of cracked gas component generated by thermal decomposition is provided in the vicinity of the atmosphere side, and a gas combustion means for combusting the gas from the rotary furnace is provided. From the gas combustion means based on the detection signal of the gas sensor The operation method of the thermal decomposition facility characterized by enlarging the damper opening of the exhaust damper of the exhaust blower that discharges the combustion exhaust gas, increasing the exhaust amount, and reducing the pressure in the rotary furnace. 回転炉の両端部にシール部を介して静止ボックスを設け、回転炉の内部に原料を収納して間接加熱により原料を熱分解する熱分解手段を備えた熱分解施設の運転方法において、シール部の大気側近傍に熱分解により発生する分解ガス成分の少なくとも1種類を検知するガスセンサを設けるとともに、回転炉内からのガスを燃焼するガス燃焼手段を設け、ガスセンサの検知信号に基づき、回転炉内のガスをガス燃焼炉に導入するエゼクタの送風量を大きくし、回転炉内圧力を減圧することを特徴とする熱分解施設の運転方法。   In the operation method of the thermal decomposition facility, the sealing portion is provided with a stationary box at both ends of the rotary furnace via the seal portion, and the thermal furnace is provided with a thermal decomposition means for storing the raw material in the rotary furnace and thermally decomposing the raw material by indirect heating. A gas sensor for detecting at least one kind of cracked gas component generated by thermal decomposition is provided in the vicinity of the atmosphere side, and a gas combustion means for combusting the gas from the rotary furnace is provided. Based on the detection signal of the gas sensor, The operation method of the thermal decomposition facility characterized by increasing the blowing volume of the ejector which introduces this gas into the gas combustion furnace, and reducing the pressure in the rotary furnace. 回転炉の両端部にシール部を介して静止ボックスを設け、回転炉の内部に原料を収納して間接加熱により原料を熱分解する熱分解手段と、熱分解により発生した分解ガスを燃焼するガス燃焼手段と、ガス燃焼手段からの燃焼排ガスを排気する排気ブロアと、シール部の大気側近傍に設けられ、分解ガス成分の少なくとも1種類を検知するガスセンサと、排気ブロアの排気量を制御し、ガスセンサの検知信号に基づき、ダンパ開度を大きく制御される排気ダンパとを備えたことを特徴とする熱分解施設。   A stationary box is provided at both ends of the rotary furnace via seals, a thermal decomposition means for storing the raw material in the rotary furnace and thermally decomposing the raw material by indirect heating, and a gas for burning the cracked gas generated by the thermal decomposition A combustion means, an exhaust blower that exhausts combustion exhaust gas from the gas combustion means, a gas sensor that is provided near the atmosphere side of the seal portion and detects at least one kind of decomposition gas component, and controls the exhaust amount of the exhaust blower; A pyrolysis facility comprising an exhaust damper whose damper opening is largely controlled based on a detection signal of a gas sensor. 分解ガスを回転炉からガス燃焼手段に導入するとともに、ガスセンサの検知信号に基づき送風量が制御されるエゼクタを設けたことを特徴とする請求項3記載の熱分解施設。   The thermal decomposition facility according to claim 3, further comprising an ejector that introduces the cracked gas from the rotary furnace into the gas combustion means and that controls an air flow rate based on a detection signal of the gas sensor. ガスセンサの検知信号に基づき、警報を発信する警報装置を設けたことを特徴とする請求項3又は4記載の熱分解施設。

The pyrolysis facility according to claim 3 or 4, further comprising an alarm device for transmitting an alarm based on a detection signal of the gas sensor.

JP2004073683A 2004-03-16 2004-03-16 Operation method for pyrolizing facility and pyrolizing facility Pending JP2005265197A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004073683A JP2005265197A (en) 2004-03-16 2004-03-16 Operation method for pyrolizing facility and pyrolizing facility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004073683A JP2005265197A (en) 2004-03-16 2004-03-16 Operation method for pyrolizing facility and pyrolizing facility

Publications (1)

Publication Number Publication Date
JP2005265197A true JP2005265197A (en) 2005-09-29

Family

ID=35089952

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004073683A Pending JP2005265197A (en) 2004-03-16 2004-03-16 Operation method for pyrolizing facility and pyrolizing facility

Country Status (1)

Country Link
JP (1) JP2005265197A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008039253A (en) * 2006-08-03 2008-02-21 Miura Co Ltd Dry distillation incinerator
JP2012087943A (en) * 2010-10-15 2012-05-10 Tsukishima Kikai Co Ltd Heat treatment equipment
CN103639185A (en) * 2013-12-26 2014-03-19 江苏盖亚环境工程有限公司 Heating kiln for restoring polluted soil
CN110440271A (en) * 2019-08-07 2019-11-12 李星余 A kind of flying ash processing unit being installed on rotary kiln
CN113307486A (en) * 2020-02-26 2021-08-27 住友电气工业株式会社 Glass base material manufacturing device
CN113606932A (en) * 2021-08-13 2021-11-05 济南大学 Method and device for evaluating and correcting on-line calculation parameters of thermal efficiency of rotary cement kiln

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008039253A (en) * 2006-08-03 2008-02-21 Miura Co Ltd Dry distillation incinerator
JP2012087943A (en) * 2010-10-15 2012-05-10 Tsukishima Kikai Co Ltd Heat treatment equipment
CN103639185A (en) * 2013-12-26 2014-03-19 江苏盖亚环境工程有限公司 Heating kiln for restoring polluted soil
CN110440271A (en) * 2019-08-07 2019-11-12 李星余 A kind of flying ash processing unit being installed on rotary kiln
CN113307486A (en) * 2020-02-26 2021-08-27 住友电气工业株式会社 Glass base material manufacturing device
CN113606932A (en) * 2021-08-13 2021-11-05 济南大学 Method and device for evaluating and correcting on-line calculation parameters of thermal efficiency of rotary cement kiln
CN113606932B (en) * 2021-08-13 2022-07-01 济南大学 Method and device for evaluating and correcting on-line calculation parameters of thermal efficiency of rotary cement kiln

Similar Documents

Publication Publication Date Title
KR100812121B1 (en) Drying system for sludge using waste heat recovery
JP2005265197A (en) Operation method for pyrolizing facility and pyrolizing facility
JP2005254032A (en) Method for operating pyrolytic facility and pyrolytic facility
JP2005257182A (en) Operating method for pyrolizing facility and pyrolizing facility
JP4026607B2 (en) Operation method of pyrolysis facility and pyrolysis facility
JP2005265198A (en) Operation method for pyrolizing facility and pyrolizing facility
JP4785453B2 (en) Odor alarm system for garbage disposal equipment
JP2006241354A (en) Waste gasification unit
JP2004263894A (en) Leak inspection method of heat treatment device and heat treatment device
JP4908914B2 (en) Processing equipment such as aluminum chips
JP4255066B2 (en) Exhaust gas treatment method and mechanism in carbonization apparatus
JP2005112373A (en) Bagging method and bagging system for fly ash
JPH10132235A (en) Waste disposing apparatus with cooler
JP4886243B2 (en) Waste treatment system
JP2007155231A (en) Cooling method and device for waste thermal decomposition char
JP3518355B2 (en) Drying method
JP2001040360A (en) Carbonizer for organic waste
JP2005112372A (en) Method for treating matter treated by indirect heating
JP2004249180A (en) Bag filter, its disaster prevention system and heating treatment facility
JP2005009907A (en) Method of inspecting leakage in heat-treating apparatus, and heat-treating apparatus
JP4364761B2 (en) Carbonization furnace for sludge containing organic matter
JP4685702B2 (en) Operation method of processing equipment such as aluminum chips
JP3744401B2 (en) Heat treatment method and heat treatment apparatus
JP2009165969A (en) Polluted soil detoxification system
JPH11287416A (en) Kiln type gasification incinerator

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20060414

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20070912

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20070918

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20080129