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JPH057605B2 - - Google Patents

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Publication number
JPH057605B2
JPH057605B2 JP5916585A JP5916585A JPH057605B2 JP H057605 B2 JPH057605 B2 JP H057605B2 JP 5916585 A JP5916585 A JP 5916585A JP 5916585 A JP5916585 A JP 5916585A JP H057605 B2 JPH057605 B2 JP H057605B2
Authority
JP
Japan
Prior art keywords
valve
temperature
opening
combustion
carbonization
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 - Lifetime
Application number
JP5916585A
Other languages
Japanese (ja)
Other versions
JPS61217618A (en
Inventor
Tsunehisa Matsuoka
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.)
MAITEI ENJINIARINGU KK
Original Assignee
MAITEI 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 MAITEI ENJINIARINGU KK filed Critical MAITEI ENJINIARINGU KK
Priority to JP5916585A priority Critical patent/JPS61217618A/en
Publication of JPS61217618A publication Critical patent/JPS61217618A/en
Publication of JPH057605B2 publication Critical patent/JPH057605B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Regulation And Control Of Combustion (AREA)
  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は雑芥、木屑、石炭、廃プラスチツク、
廃ゴム、タイヤ等の廃棄物を乾留ガス化燃焼して
熱エネルギーを取出す際に、運転開始時期及び終
期あるいは停止時における乾留用空気量を自動制
御して乾留炉内に生成し易い爆発限界の濃度範囲
を回避することを目的としてなされたものであ
る。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is applicable to garbage, wood chips, coal, waste plastics,
When waste materials such as waste rubber and tires are carbonized and burned to extract thermal energy, the amount of air for carbonization at the start of operation and at the end or stop is automatically controlled to reduce the explosive limit that is likely to be generated in the carbonization furnace. This was done with the aim of avoiding concentration ranges.

〔従来の技術〕 乾留ガス化炉において焚き始め、燃料投入時、
あるいは運転終期または停止時に炉内に停滞して
いる未燃ガスが空気と混合して爆発限界を構成す
ることは従来よりしばしば経験するところであ
り、ガス量が多い程爆発力は大であり、少ないと
きはバツクフアイヤー程度ですむが頗る危険であ
る。
[Conventional technology] When starting combustion in a carbonization gasifier and adding fuel,
Or, at the end of operation or when the furnace is shut down, unburned gas stagnant in the furnace mixes with air and forms the explosion limit, which has often been experienced. In some cases, it may only cause a backfire, but it is extremely dangerous.

乾留ガス化炉において冷態時より運転開始して
所定のガス出力を得るまでの間、ガス濃度は供給
空気量に左右される。特にその傾向は冷態時より
スタートする場合に顕著であり、空気量はガス発
生の状況に合わせて制御する必要がある。
In a carbonization gasification furnace, the gas concentration depends on the amount of air supplied from the start of operation in a cold state until a predetermined gas output is obtained. This tendency is particularly noticeable when starting from a cold state, and the amount of air needs to be controlled according to the gas generation situation.

一般に温度指示調節計(比例制御式)の制御範
囲は、比例帯が80%、100%特殊な場合は1〜
1000%のものもあるが、これらは構造が複雑にな
つて価格が高く一般的でない。温度指示調節計の
うち、価格が低廉で入手し易い汎用のものは比例
帯が1〜50%のものが多く、例えばフルスケール
が0〜1600℃、指針が設定値1200℃を越えて1600
℃に達したとき、空気調整弁が全閉となり、設定
値は下つて800℃に達したとき全開になつたとす
ると比例帯は (1600−800)/1600=0.5=50% であり、このような温度範囲の調節計は前述の雑
芥、木屑、石炭、廃プラスチツク、廃ゴム、タイ
ヤ等の廃棄物の乾留ガス化に適する。
Generally, the control range of a temperature indicating controller (proportional control type) is 80% in the proportional band, and 1 to 100% in special cases.
There are some that are 1000%, but these have complicated structures, are expensive, and are not common. Among the temperature indicating controllers, many of the inexpensive and easily available general-purpose ones have a proportional band of 1 to 50%, for example, the full scale is 0 to 1600℃, and the pointer is 1600℃ beyond the set value of 1200℃.
℃, the air adjustment valve is fully closed, the set value is lowered, and when the temperature reaches 800℃, it is fully opened.The proportional band is (1600-800)/1600=0.5=50%, and as shown below. The temperature range controller is suitable for the carbonization gasification of wastes such as the aforementioned garbage, wood chips, coal, waste plastics, waste rubber, and tires.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、この比例帯を有する温度指示調
節計では乾留ガス化炉の焚き始めの低温時でも空
気調整弁は全閉となつていまい、800℃以下では
空気調節弁の開度は調節不可能となり、このため
多量の過剰空気が炉内に導入されることとなり、
爆発限界を構成する危険性が大でありその対策が
望まれていた。この危険状態は乾留炉の運転終了
時あるいは停止時でも同様である。
However, with this temperature indicating controller having a proportional band, the air regulating valve cannot be fully closed even at low temperatures when the carbonization gasifier starts firing, and the opening of the air regulating valve cannot be adjusted below 800°C. This results in a large amount of excess air being introduced into the furnace.
There was a great danger of reaching the explosive limit, and countermeasures were desired. This dangerous situation is the same even when the carbonization furnace is finished operating or stopped.

また現在汎用されている比例帯50%の調節計で
は制御範囲限界外の制御は手動操作で補つている
ため乾留ガス化燃焼装置の完全自動化の障害とな
つていた。
Furthermore, with the currently widely used controllers with a proportional band of 50%, control outside the limits of the control range is compensated for by manual operation, which has been an obstacle to the complete automation of carbonization gasification and combustion equipment.

〔問題を解決するための手段〕[Means to solve the problem]

上記に鑑み、本発明は廃棄物の乾留ガス化初期
あるいは終期または停止時において空気導入が、
温度指示調節計の下限温度800℃に達するまでの
間あるいは終了時、下限温度800℃より常温にま
で低下する期間、温度指示調節計によれば開き過
ぎによる空気調整弁の開度を、別の装置によつて
炉内温度にマツチした空気量を送入できる弁開度
に自動的に調節させることにより、炉内ガス成分
を爆発限界外に保つようにしたものであり、その
要旨は、乾留ガス化燃焼装置の発生ガス燃焼炉に
燃焼ガスの温度を測定する温度計を設置し、一方
乾留ガス化炉への空気供給管(またはダクト)中
にアクチユエータ付の弁を設置し、さらに自動調
節計を設けて前記燃焼ガス温度を一定とするよう
に前記弁を開閉するため、前記温度計、前記自動
調節計及び前記弁にて調節ループを構成すると共
に、乾留ガス化燃焼装置の起動時及び停止時の低
温の過度状態においては前記弁が自動調節計の働
きによつて開き過ぎぬよう前記のあるいは別の燃
焼ガス温度計よりの信号に基づいて前記弁の開度
を定常運転状態の開度の近傍の狭い開度に自動設
定するよう構成した乾留ガス化燃焼装置の自動制
御方法である。
In view of the above, the present invention provides air introduction at the beginning, end, or stop of carbonization gasification of waste.
During or after reaching the lower limit temperature of 800°C on the temperature indicating controller, or during the period when the lower limit temperature drops from 800°C to room temperature, the opening degree of the air adjustment valve due to excessive opening according to the temperature indicating controller is changed. The device automatically adjusts the valve opening to allow the flow of air that matches the temperature inside the furnace, thereby keeping the gas components inside the furnace outside the explosion limit. A thermometer to measure the temperature of the combustion gas is installed in the gas combustion furnace of the gasification combustion equipment, and a valve with an actuator is installed in the air supply pipe (or duct) to the carbonization gasification furnace, and automatic adjustment is also performed. In order to open and close the valve so as to keep the temperature of the combustion gas constant, the thermometer, the automatic controller, and the valve constitute a control loop, and when the carbonization gasification and combustion apparatus is started up and In order to prevent the valve from opening too much in the low-temperature transient state at the time of shutdown, the valve opening is adjusted to the normal operating state based on the signal from the combustion gas thermometer or another combustion gas thermometer. This is an automatic control method for a carbonization gasification/combustion apparatus configured to automatically set a narrow opening degree in the vicinity of 100 degrees.

〔作用〕[Effect]

上記の構成によれば本発明は、乾留ガス化炉起
動時、あるいは終期あるいは停止時の低温の過度
状態においては、空気調整弁が温度指示調節計の
働きによつて開き過ぎぬよう、該温度指示調節計
は遮断し燃焼ガスを測定する温度計、あるいは別
の燃焼ガス温度計よりの信号に基づいて、空気調
整弁開度を定常運転状態の開度の近傍の狭い開度
になるように例えば電圧発生器により一定の電圧
を温度指示調節計に印加し、アクチユエータ付空
気調整弁を開閉させるものである。
According to the above configuration, the present invention can prevent the air regulating valve from opening too much due to the action of the temperature indicating controller in the low-temperature transient state at the time of startup, final stage, or shutdown of the carbonization gasifier. The indicating controller is shut off, and based on the signal from the thermometer that measures combustion gas or another combustion gas thermometer, the air adjustment valve opening is set to a narrow opening close to the opening under steady-state operation. For example, a voltage generator applies a constant voltage to a temperature indicating controller to open and close an air regulating valve with an actuator.

〔実施例〕〔Example〕

図は本発明の一実施例における説明図である。 The figure is an explanatory diagram of an embodiment of the present invention.

乾留ガス化炉1は下方に送風機2、アクチユエ
ータ3付き空気調整弁4を有する空気供給管5
と、上方に可燃物投入口6を備え、側方に乾留ガ
ス取出管路7が開口し、該管路7に連絡して燃焼
炉8が設けられていて、高温燃焼ガスが出口9よ
り廃熱ボイラ等の熱回収装置(図示せず)に導入
され熱エネルギーが有効に利用される。
The carbonization gasification furnace 1 has an air supply pipe 5 having a blower 2 and an air regulating valve 4 with an actuator 3 below.
A combustible material inlet 6 is provided at the top, and a carbonization gas take-off pipe 7 opens on the side. A combustion furnace 8 is provided in communication with the pipe 7, and high-temperature combustion gas is disposed of through an outlet 9. The heat energy is introduced into a heat recovery device (not shown) such as a heat boiler, and the heat energy is effectively used.

温度調節ループ10は、前記出口9に設けられ
た熱電対による温度センサA,B、可変電圧発生
器11、切替接点12が附属した温度指示計1
3、温度指示調節計14及び前記アクチユエータ
3付き空気調整弁4より構成されており、以下に
その作動を述べる。
The temperature control loop 10 includes a temperature indicator 1 equipped with thermocouple temperature sensors A and B provided at the outlet 9, a variable voltage generator 11, and a switching contact 12.
3. It is composed of a temperature indicating controller 14 and an air regulating valve 4 with the actuator 3, and its operation will be described below.

乾留ガス化炉運転開始に当つて先ず温度指示計
13及び温度指示調節計14を希望する燃焼出力
に相当する設定値、例えば1200℃に設定する。次
に可変電圧発生器11を操作して温度指示調節計
14に空気調整弁開度を定常運転状態の開度の近
傍の狭い開度になるような任意に適切な電圧出力
を印加する。温度指示調節計14は印加電圧値に
相当するパルス信号をアクチユエータ付き空気調
整弁4に送信して該弁4の開閉度が決められる。
このようにして予め決めた弁開度となるように可
変電圧発生器11の出力を調整しておく。
When starting the operation of the carbonization gasifier, first, the temperature indicator 13 and temperature indicator controller 14 are set to a set value corresponding to the desired combustion output, for example, 1200°C. Next, the variable voltage generator 11 is operated to apply an arbitrarily appropriate voltage output to the temperature indicating controller 14 so that the air adjustment valve opening becomes a narrow opening close to the opening in the steady operating state. The temperature indicating controller 14 transmits a pulse signal corresponding to the applied voltage value to the air regulating valve 4 with an actuator, and the degree of opening and closing of the valve 4 is determined.
In this way, the output of the variable voltage generator 11 is adjusted so that the valve opening degree is determined in advance.

次に乾留ガス化炉1内の可燃物15に点火口1
6より点火し、送風機2の運転を開始する。上記
のとおり可変電圧発生器11の設定電圧出力によ
り空気調整弁4は定常の開度より狭い設定開度に
固定されており空気量は制限され、燃焼乾留は緩
かに進行し、発生乾留ガス中の酸素濃度も低く、
1.0〜2.6%程度となり、爆発限界外となつて安全
に運転できる。このようにして乾留は進行し、発
生ガス量は増大する。乾留ガスは燃焼炉8に至
り、着火バーナで点火され空気の供給を受けて燃
焼は旺盛となり、燃焼ガスの温度は上昇する。
Next, the ignition port 1 is placed in the combustible material 15 in the carbonization gasification furnace 1.
6, and the blower 2 starts operating. As mentioned above, the air regulating valve 4 is fixed at a set opening narrower than the normal opening due to the set voltage output of the variable voltage generator 11, the amount of air is limited, combustion carbonization proceeds slowly, and the generated carbonized gas The oxygen concentration inside is also low,
The amount is about 1.0 to 2.6%, which is outside the explosive limit and can be operated safely. Carbonization progresses in this manner, and the amount of gas generated increases. The carbonized gas reaches the combustion furnace 8, where it is ignited by an ignition burner, and with the supply of air, combustion becomes active and the temperature of the combustion gas rises.

この燃焼ガス温度が最初に設定した温度1200℃
に達すると、温度センサAの発生電圧によつて温
度指示計13に内蔵されている切替接点12は自
動的に作動して切り替わり、可変電圧発生器11
の電圧出力は断たれ、温度センサBの出力が温度
指示調節計14に自動的に入力される。この切り
替えによつて温度指示調節計14の発する信号に
よつてアクチユエータ付き空気調整弁4の開度を
調節し、導入空気量が調節され、発生ガス温度が
一定に保たれる。
This combustion gas temperature is the initially set temperature 1200℃
When the voltage generated by the temperature sensor A automatically operates and switches the switching contact 12 built in the temperature indicator 13, the variable voltage generator 11
The voltage output of the temperature sensor B is cut off, and the output of the temperature sensor B is automatically input to the temperature indicating controller 14. By this switching, the opening degree of the actuator-equipped air regulating valve 4 is adjusted based on the signal issued by the temperature indicating controller 14, the amount of introduced air is adjusted, and the generated gas temperature is kept constant.

その後は炉内に可燃物15が存在する限り温度
センサBの発生電圧変化に応じて温度指示調節計
14、アクチユエータ付き空気調整弁4によつて
自動制御される。
Thereafter, as long as there is combustible material 15 in the furnace, the temperature is automatically controlled by the temperature indicating controller 14 and the actuator-equipped air regulating valve 4 according to the change in the voltage generated by the temperature sensor B.

燃焼終期に近ずけば燃焼炉8のガス出口温度が
低下するから、温度センサAの発生電圧は減少
し、切替接点12が切り替わり、スタート時と逆
の作動により空気調整弁4は再び可変電圧発生量
11によつて作動し空気調整弁4の開度を制限し
空気量は減少する。
As the combustion furnace 8 approaches the end of combustion, the gas outlet temperature of the combustion furnace 8 decreases, so the voltage generated by the temperature sensor A decreases, the switching contact 12 switches, and the air regulating valve 4 returns to the variable voltage due to the reverse operation from the start. It operates according to the generated amount 11, limits the opening degree of the air regulating valve 4, and reduces the amount of air.

温度指示計13と温度センサAは接点付の温度
センサーで代用してもよい。また温度センサA及
びBは上記のように別々のものとしてもよいが、
別の回路を採用して1本のセンサとして信号を分
岐することも可能である。温度センサ、調節計等
の方式については各種のものが市販されておりそ
のいずれを用いるかによつて信号、回路構成等に
上記の実施例と異なる部分が生じるが、本発明の
要旨とするところは特許請求の範囲に記載すると
おりであり上記実施例に限定されるものではい。
The temperature indicator 13 and the temperature sensor A may be replaced by a temperature sensor with a contact point. Also, temperature sensors A and B may be separate as described above, but
It is also possible to use another circuit to branch the signal into one sensor. Various types of temperature sensors, controllers, etc. are commercially available, and depending on which one is used, signals, circuit configurations, etc. may differ from those of the above embodiments, but the gist of the present invention is is as described in the claims and is not limited to the above embodiments.

〔発明の効果〕〔Effect of the invention〕

本発明は乾留ガス化燃焼装置の発生ガス燃焼炉
に燃焼ガスの温度を測定する温度計を設置し、一
方乾留ガス化炉への空気供給管(またはダクト)
中にアクチユエータ付の弁を設置し、さらに自動
調節計を設けて前記燃焼ガス温度を一定とするよ
うに前記弁を開閉するため、前記温度計、前記自
動調節計及び前記弁にて調節ループを構成すると
共に、乾留ガス化燃焼装置の起動時及び停止時の
低温の過度状態においては前記弁が自動調節計の
働きによつて開き過ぎぬよう前記のあるいは別の
燃焼ガス温度計よりの信号に基づいて前記弁の開
度を定常運転状態の開度の近傍の狭い開度に自動
設定するよう構成した乾留ガス化燃焼装置の自動
制御方法を要旨とするものであるから、乾留ガス
化炉の起動時、あるいは終期の低温過度状態にお
いて温度指示調節計の調節制御範囲外であつて
も、可変電圧発生器により出力する電圧値で強制
的に制御範囲を抑制し、空気調整弁の開度を狭い
開度に制限でき、供給空気量を減少して発生乾留
ガス中の酸素濃度も低く爆発限界濃度に達する機
会も減少でき、安全性が一層高まる。
In the present invention, a thermometer for measuring the temperature of combustion gas is installed in the generated gas combustion furnace of a carbonization gasification combustion apparatus, and an air supply pipe (or duct) to the carbonization gasification furnace is installed.
A valve with an actuator is installed inside, and an automatic controller is further installed to open and close the valve so as to keep the combustion gas temperature constant. At the same time, the valve is controlled by the signal from the above or another combustion gas thermometer to prevent the valve from opening too much due to the action of the automatic controller in the low-temperature transient state when starting and stopping the carbonization gasification combustion equipment. The purpose of the present invention is to provide an automatic control method for a carbonization gasification combustion apparatus configured to automatically set the opening degree of the valve to a narrow opening degree close to the opening degree in the steady operation state based on the above-mentioned conditions. Even if it is outside the adjustment control range of the temperature indicating controller during startup or in the final low temperature transient state, the control range is forcibly suppressed by the voltage value output by the variable voltage generator, and the opening degree of the air adjustment valve is controlled. The opening can be restricted to a narrow degree, the amount of air supplied can be reduced, and the oxygen concentration in the generated carbonized gas can be low, reducing the chance of reaching the explosive limit concentration, further increasing safety.

しかも従来制御範囲限界外の制御部分の制御は
手動操作で行つていたので自動化の障害となつて
いたが、この調節ループの採用によつて自動化が
可能となり、しかも可変電圧発生器により温度指
示調節計への電圧の印加は可燃物の種類に合わせ
て予め任意の値に設定できるから、可燃物が雑
芥、木屑、石炭、廃プラスチツク、廃ゴム、タイ
ヤ等多岐にわたつてもその種類に合わせることが
できるので汎用性に富み、しかも可変電圧発生器
は安価で入手し易いので経済的効果も大である。
Moreover, in the past, control of control parts outside the limits of the control range was performed manually, which was an obstacle to automation, but by adopting this control loop, automation is possible, and temperature control is also controlled by a variable voltage generator. The voltage applied to the controller can be set in advance to any value depending on the type of combustible material, so even if the combustible material is diverse, such as trash, wood chips, coal, waste plastics, waste rubber, tires, etc. Since variable voltage generators can be matched, they are highly versatile, and variable voltage generators are inexpensive and easily available, so they have great economic effects.

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

図は本発明の一実施例における説明図である。 1……乾留ガス化炉、2……送風機、3……駆
動アクチユエータ、4……空気調整弁、5……空
気供給管、6……可燃物投入口、7……乾留ガス
取出管路、8……燃焼炉、9……出口、10……
温度調節ループ、11……可変電圧発生器、12
……切替接点、13……温度指示計、14……温
度指示調節計、15……可燃物、16……点火
口。
The figure is an explanatory diagram of an embodiment of the present invention. DESCRIPTION OF SYMBOLS 1... Carbonization gasification furnace, 2... Air blower, 3... Drive actuator, 4... Air adjustment valve, 5... Air supply pipe, 6... Combustible material inlet, 7... Carbonization gas extraction pipe, 8... Combustion furnace, 9... Exit, 10...
Temperature control loop, 11... Variable voltage generator, 12
...Switching contact, 13...Temperature indicator, 14...Temperature indicator controller, 15...Combustible material, 16...Ignition port.

Claims (1)

【特許請求の範囲】[Claims] 1 乾留ガス化燃焼装置の発生ガス燃焼炉に燃焼
ガスの温度を測定する温度計を設置し、一方乾留
ガス化炉への空気供給管(またはダクト)中にア
クチユエータ付の弁を設置し、さらに自動調節計
を設けて前記燃焼ガス温度を一定とするように前
記弁を開閉するため、前記温度計、前記自動調節
計及び前記弁にて調節ループを構成すると共に、
乾留ガス化燃焼装置の起動時及び停止時の低温の
過度状態においては前記弁が自動調節計の働きに
よつて開き過ぎぬよう前記のあるいは別の燃焼ガ
ス温度計よりの信号に基づいて前記弁の開度を定
常運転状態の開度の近傍の狭い開度に自動設定す
るよう構成した乾留ガス化燃焼装置の自動制御方
法。
1. A thermometer for measuring the temperature of combustion gas is installed in the generated gas combustion furnace of the carbonization gasification combustion equipment, and a valve with an actuator is installed in the air supply pipe (or duct) to the carbonization gasification furnace, and In order to open and close the valve to keep the temperature of the combustion gas constant by providing an automatic controller, the thermometer, the automatic controller, and the valve constitute a control loop,
In order to prevent the valve from opening too much due to the action of the automatic controller, the valve is adjusted based on the signal from the combustion gas thermometer or another combustion gas thermometer to prevent the valve from opening too much during low temperature transient conditions when starting and stopping the carbonization gasification combustion equipment. An automatic control method for a carbonization gasification combustion equipment configured to automatically set the opening of the engine to a narrow opening close to the opening of a steady operating state.
JP5916585A 1985-03-22 1985-03-22 Automatic control method of dry distillation combustion device Granted JPS61217618A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5916585A JPS61217618A (en) 1985-03-22 1985-03-22 Automatic control method of dry distillation combustion device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5916585A JPS61217618A (en) 1985-03-22 1985-03-22 Automatic control method of dry distillation combustion device

Publications (2)

Publication Number Publication Date
JPS61217618A JPS61217618A (en) 1986-09-27
JPH057605B2 true JPH057605B2 (en) 1993-01-29

Family

ID=13105494

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5916585A Granted JPS61217618A (en) 1985-03-22 1985-03-22 Automatic control method of dry distillation combustion device

Country Status (1)

Country Link
JP (1) JPS61217618A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103797258A (en) * 2011-08-11 2014-05-14 Ntn株式会社 Tapered roller bearing and its installation structure

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0656252B2 (en) * 1988-07-08 1994-07-27 株式会社ササクラ Batch type incinerator of waste
US8006407B2 (en) * 2007-12-12 2011-08-30 Richard Anderson Drying system and method of using same
JP5762713B2 (en) * 2010-10-04 2015-08-12 株式会社キンセイ産業 Dry distillation gasification incineration processing equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103797258A (en) * 2011-08-11 2014-05-14 Ntn株式会社 Tapered roller bearing and its installation structure

Also Published As

Publication number Publication date
JPS61217618A (en) 1986-09-27

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