JPH04157000A - Drying method for slurry by rotary drier - Google Patents

Drying method for slurry by rotary drier

Info

Publication number
JPH04157000A
JPH04157000A JP2280306A JP28030690A JPH04157000A JP H04157000 A JPH04157000 A JP H04157000A JP 2280306 A JP2280306 A JP 2280306A JP 28030690 A JP28030690 A JP 28030690A JP H04157000 A JPH04157000 A JP H04157000A
Authority
JP
Japan
Prior art keywords
dryer
detected
crushing
rotating
driving power
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.)
Granted
Application number
JP2280306A
Other languages
Japanese (ja)
Other versions
JP2981271B2 (en
Inventor
Hideo Yamazaki
日出夫 山崎
Hideo Omura
大村 秀夫
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.)
Okawara Mfg Co Ltd
Original Assignee
Okawara Mfg 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 Okawara Mfg Co Ltd filed Critical Okawara Mfg Co Ltd
Priority to JP2280306A priority Critical patent/JP2981271B2/en
Publication of JPH04157000A publication Critical patent/JPH04157000A/en
Application granted granted Critical
Publication of JP2981271B2 publication Critical patent/JP2981271B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Drying Of Solid Materials (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To allow stable drying of even a slurry, such as sludge, by controlling the discharge temp. from the drier together with the required driving power for rotating a drum or the required driving power for rotating crushing and dgitating vanes or the detected value from torque. CONSTITUTION:The temp. of an exhaust gas is detected by a temp. detector 12 mounted at a proper point of a discharge duct 11 and the driving power required for rotating the drum 2 or the driving power or the torque required for rotating the crushing and agitating vanes 4 is detected by meter relays 15, 16 and the detected values are inputted to a computer. The computer controls a motor 8 of a screw conveyor 7 in a charging hopper 6 and a hot stove 9 in accordance with these inputted values. If the detected value from the temp. detector 12 and the detected value of the driving power required for rotating the drum 2 or the driving power or torque required for rotating the crushing and agitating vanes 4 both exceed reference values, the rotation of the motor 8 is controlled according to the ratio thereof to decrease the charge of the slurry or to increase the heat quantity from the hot stove 9.

Description

【発明の詳細な説明】 イ、&″業上の利用分野 本発明は、破砕攪拌翼を有する回転乾燥を用いて汚泥等
の泥状物を乾燥する方法の改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION A. Field of Industrial Application The present invention relates to an improvement in a method for drying muddy substances such as sludge using rotary drying having a crushing stirring blade.

口、従来の技術 従来、汚泥等の泥状物を破砕攪拌翼を有する回転乾燥機
を用いて乾燥するには、次のような方法がとられていた
BACKGROUND OF THE INVENTION Conventionally, the following method has been used to dry muddy substances such as sludge using a rotary dryer having crushing and stirring blades.

すなわち、乾燥機からの排気ガスの温度を検出し、これ
が所定温度より上昇する場合には。
That is, the temperature of the exhaust gas from the dryer is detected and if this rises above a predetermined temperature.

乾燥機への泥状物の投入量を増加するか、あるいは供給
熱量を減少し、排気温度が所定温度より低下する場合は
、乾燥機への泥状物の投入量を減少するか、あるいは供
給熱量を増加する方法である。
Increase the amount of sludge input into the dryer or reduce the amount of heat supplied. If the exhaust temperature drops below the specified temperature, reduce the amount of sludge input into the dryer or reduce the amount of heat supplied. This is a method to increase the amount of heat.

これは、熱風乾燥においては、一般に乾燥機からの排気
温度が上昇することは、乾燥機に供給された熱量に対し
て被乾燥物の量が少なすぎるからであり、排気温度が低
下することはこの逆の現象がみられるからである。
This is because in hot air drying, the exhaust temperature from the dryer generally increases because the amount of material to be dried is too small relative to the amount of heat supplied to the dryer, and the exhaust temperature does not decrease. This is because the opposite phenomenon is observed.

ハ9発明が解決しようとする課題 通常の場合は、上記の方法は妥当なものであるが、汚泥
等の泥状物は含水率が高いと粘性も高く、乾燥機内での
分散性も悪化するから、このような場合は上記の方法で
は乾燥不可能な場合が生ずる。すなわち、乾燥機に投入
された泥状物の量が多過ぎると、乾燥が不十分になり泥
状物は十分に分散されなくなって、乾燥機内壁や破砕攪
拌翼などに付着したり、大きな塊を生じて、熱風との有
効接触面積は減少し、伝熱特性は悪化して乾燥能率は極
端に低下する。すると乾燥機に吹き込まれた熱風は泥状
物と十分接触しないで、乾燥機内を吹き抜けてしまうの
で。
C.9 Problems to be Solved by the Invention In normal cases, the above method is appropriate, but when muddy substances such as sludge have a high water content, they have high viscosity and their dispersibility in the dryer deteriorates. Therefore, in such cases, drying may not be possible using the above method. In other words, if too much sludge is put into the dryer, drying will be insufficient and the sludge will not be sufficiently dispersed, causing it to stick to the inside wall of the dryer, crushing stirring blades, etc., or form large lumps. As a result, the effective contact area with hot air decreases, heat transfer characteristics deteriorate, and drying efficiency extremely decreases. The hot air blown into the dryer then blows through the dryer without making sufficient contact with the mud.

排気温度は上昇する。従来の方法では、排気温度を設定
値に保つべく、乾燥機への泥状物の投入量を増加させる
か、あるいは供給熱量を減少させるようになっているの
で、乾燥機内での泥状物の付着はますます増加し、−層
未乾燥の方向に進み最悪乾燥不能に陥ってしまう。
Exhaust temperature increases. In conventional methods, in order to maintain the exhaust temperature at the set value, the amount of sludge added to the dryer is increased or the amount of heat supplied is decreased. The adhesion increases more and more, and progresses toward a layer that is not dry, and in the worst case, it becomes impossible to dry the layer.

本発明が解決しようとする課題は、乾燥機の排気温度の
上昇が上記のような未乾燥に基因するものかどうかを判
別して、それに相応しい対に策を示すことによって、回
転乾燥機による泥状物の乾燥を、安定して連続的に行え
る方法を提供するものである。
The problem to be solved by the present invention is to determine whether or not the increase in the exhaust gas temperature of the dryer is due to non-drying as described above, and to take appropriate countermeasures to reduce the amount of dirt caused by the rotary dryer. The purpose of the present invention is to provide a method that allows stable and continuous drying of objects.

二 課題を解決するための手段 上記課題を解決するため、本発明は。2. Means to solve the problem In order to solve the above problems, the present invention has the following features.

汚泥等の泥状物を破砕攪拌翼を有する回転乾燥機を用い
て乾燥する方法において、 乾燥機からの排気ガス温度を検出し、この検出値と 乾燥機のドラムの回転にかかる所要動力または破砕攪拌
翼の回転にかかる所要動力もしくはトルクを検比し、こ
の検出値との 2つの検出値の関係から乾燥機に投入する泥状物の量ま
たは乾燥機に供給する熱量を11+整するものである。
In a method of drying muddy materials such as sludge using a rotary dryer equipped with crushing and stirring blades, the temperature of the exhaust gas from the dryer is detected, and this detected value is combined with the power required to rotate the drum of the dryer or crushing. The power or torque required to rotate the stirring blades is compared, and the amount of slurry to be thrown into the dryer or the amount of heat to be supplied to the dryer is adjusted by 11+ based on the relationship between this detected value and the two detected values. be.

ホ1作用 前述のように1例えば投入過多等による乾燥不十分の状
態では、乾燥機に投入された泥状物は、乾燥機内壁や破
砕攪拌翼に付着したり、大きな塊を生ずるようになる。
1. Effect As mentioned above, 1. If drying is insufficient due to overloading, for example, muddy materials put into the dryer will adhere to the inner wall of the dryer or crushing stirring blades, or form large lumps. .

したがってこのような状態では、乾燥機のドラムの回転
動力は増大し、または破砕攪拌翼の回転動力あるいはト
ルクも増大するとともに、この状態に特有の動力あるい
はトルク変動を生ずるので、この変化を検出し、この検
出値と排気ガス温度の検出値との関係から、乾燥機へ投
入される汚泥物の量または供給熱量を調整するのである
。すなわち、排気ガス温度が基?!i値を超えて上昇す
る場合には、ドラムまたは破砕攪拌翼の回転動力あるい
はトルクを検出し、この検出値も基準を超え特有の変動
を示す場合は、乾燥機への泥状物投入量を減少するかあ
るいは供給熱量を増加し、検出値が基準値を超えない場
合は乾燥機への泥状物の投入量を増加するか、供給熱量
を減少させるのである。
Therefore, in such a state, the rotational power of the drum of the dryer increases, or the rotational power or torque of the crushing agitation blade also increases, and a power or torque fluctuation peculiar to this state occurs, so this change cannot be detected. Based on the relationship between this detected value and the detected value of exhaust gas temperature, the amount of sludge introduced into the dryer or the amount of heat supplied is adjusted. In other words, is it based on exhaust gas temperature? ! If the value increases beyond the i value, the rotational power or torque of the drum or crushing agitation blade is detected, and if this detected value also exceeds the standard and shows a characteristic fluctuation, the amount of sludge input to the dryer is adjusted. If the detected value does not exceed the standard value, either increase the amount of slurry fed into the dryer or decrease the amount of heat supplied.

上記の基準値をを超える、超えないの判定は、瞬時的な
出力変動を補正するため、検出値が基準値を超える時間
の単位時間当りの割合で判断するとともに、その程度を
判定し、それに応じて乾燥機への泥状物の投入量や供給
熱量を114節するのである。
In order to correct instantaneous output fluctuations, the determination of whether the above reference value is exceeded or not is made based on the percentage of time per unit time during which the detected value exceeds the reference value, and also the degree of Accordingly, the amount of slurry input to the dryer and the amount of heat supplied are adjusted by 114 degrees.

へ 実施例 以下本発明を図示の実施例に基づいて説明する。Example The present invention will be explained below based on illustrated embodiments.

1は破砕攪拌翼付回転乾燥機本体であり、ドラム2はモ
ータ3により2〜8rpmで回転する。
Reference numeral 1 denotes a rotary dryer body with crushing stirring blades, and a drum 2 is rotated by a motor 3 at 2 to 8 rpm.

投入ホッパ6内に収納された泥状物はモータ8で回転す
るスクリューコンベア7により乾燥機内に定量供給され
る。乾燥機に投入された泥状物は、ドラム2の内壁に取
り付けられたりフタ10により上部に持ち上げられ、自
重で落下する時モータ5により200〜400rplN
で回転する破砕攪拌翼4に激しく叩かれ分散される。
The slurry stored in the input hopper 6 is fed in a fixed amount into the dryer by a screw conveyor 7 rotated by a motor 8. The sludge put into the dryer is attached to the inner wall of the drum 2 or lifted to the top by the lid 10, and when it falls under its own weight, it is heated by the motor 5 at 200 to 400 rplN.
The crushed particles are violently beaten and dispersed by the rotating crushing stirring blades 4.

9は熱風炉、17はバーナ、18は油量調節弁である。9 is a hot air stove, 17 is a burner, and 18 is an oil amount control valve.

13は排気ブロア、11は排気ガスダクトで適所に温度
検出器12が取り付けられている。15.16はメータ
リレー、14は製品排出口である。
13 is an exhaust blower, 11 is an exhaust gas duct, and a temperature sensor 12 is attached at a proper position. 15 and 16 are meter relays, and 14 is a product discharge port.

以上の装置を用いた本発明による乾燥方法は。The drying method according to the present invention using the above apparatus is as follows.

次のようなになされる6投入ホツパ6より定量供給され
る泥状物は、リフタ10.破砕攪拌翼4の作用により分
散されながら、熱風炉9により吹き込まれる熱風により
乾燥される6泥状物は、通常ドラム前部(投入ホッパ6
側)では泥塊状、中央部では小塊状、後部では乾燥粒状
となって製品排出口14から排出される。熱風は、熱風
炉9から通常700〜800℃でドラム2内に吹き込ま
れ、泥状物と並流する間に熱を奪われ、120〜250
℃で排気ダクト11がら排気される。この排気ガスの温
度を排気ダクトの適所に取り付けられた温度検出器12
により検出するとともに、ドラム2の回転に要する動力
または破砕攪拌翼4の回転に要する動力もしくはトルク
をメータリレー15.16で検出して、この検出値をコ
ンピュータに入力する。本実施例ではこの検出にメータ
リレーを用いたが、これに限定されるものではない。コ
ンピュータでは、これらの入力された値に基づいて、投
入ホッパ6内のスクリューコンベア7のモータ8と熱風
炉9を制御するようになっている。すなわち、温度検出
器12からの検出値とドラム2の回転所要動力または破
砕攪拌翼4の回転所要動力もしくはトルクの検出値が共
に基準値を超える場合は、その割合に応じて、モータ8
の回転を制御して泥状物の投入量を減少させるか、ある
いは熱風炉9からの熱量を増加させるのである。熱量を
増加させる方法は、排気温度基準を上げてバーナ7の燃
油量を増して、熱風温度を高めてもよいし、排気ブロア
13を調節して熱風量を増加させてもよい。また排気温
度のみが基準値を超え所要動力等は基準値以下である場
合には泥状物投入量を増すか、供給熱量を減すのである
The slurry that is fed in a fixed amount from the input hopper 6 is fed to the lifter 10. The sludge, which is dispersed by the action of the crushing stirring blades 4 and dried by the hot air blown by the hot blast furnace 9, is usually placed in the front part of the drum (input hopper 6).
The product is discharged from the product discharge port 14 in the form of mud lumps at the sides, small lumps at the center, and dry granules at the rear. The hot air is blown into the drum 2 from the hot blast furnace 9 at a temperature of usually 700 to 800°C, and heat is removed while flowing in parallel with the mud, resulting in a temperature of 120 to 250°C.
The air is exhausted from the exhaust duct 11 at . The temperature of this exhaust gas is measured by a temperature detector 12 installed at a suitable location in the exhaust duct.
At the same time, the power required to rotate the drum 2 or the power or torque required to rotate the crushing stirring blades 4 is detected by meter relays 15 and 16, and this detected value is input into the computer. Although a meter relay is used for this detection in this embodiment, the present invention is not limited to this. The computer controls the motor 8 of the screw conveyor 7 in the input hopper 6 and the hot air stove 9 based on these input values. That is, if both the detected value from the temperature detector 12 and the detected value of the required rotation power of the drum 2 or the detected value of the rotation required power or torque of the crushing stirring blades 4 exceed the reference value, the motor 8 is
The rotation of the hot air stove 9 is controlled to reduce the amount of mud thrown in, or to increase the amount of heat from the hot air stove 9. The amount of heat may be increased by raising the exhaust gas temperature standard and increasing the amount of fuel in the burner 7 to increase the hot air temperature, or by adjusting the exhaust blower 13 to increase the amount of hot air. Furthermore, if only the exhaust gas temperature exceeds the standard value and the required power, etc. is below the standard value, the amount of sludge input is increased or the amount of heat supplied is decreased.

ト、効果 上述のように、本願発明は乾燥機からの排気温度に加え
、ドラムの回転所要動力または破砕攪拌翼の回転所要動
力もしくはトルクを検出し、この検出値とあわせて制御
しているため、排気温度の上昇が、いわゆる乾燥不十分
に基づくものか否かが判定でき、それに相応しい制御が
可能となり、汚泥等の泥状物であっても安定した連続乾
燥ができるのである。
G. Effect As mentioned above, the present invention detects the required rotation power of the drum or the rotation required power or torque of the crushing agitation blade in addition to the exhaust temperature from the dryer, and controls it in conjunction with this detected value. It is possible to determine whether the rise in exhaust gas temperature is due to so-called insufficient drying, and to perform appropriate control, making it possible to perform stable continuous drying even for muddy materials such as sludge.

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

第1図は本発明を実施する乾燥装置の模式図。 第2図は第1図A−Aの断面図である。 1 破砕攪拌翼付回転乾燥機 2 ドラム 3、モータI 4、破砕攪拌翼 5、モータ… 6、投入ホッパ 7、スクリューコンベア 8 モータm 9、熱風炉 10、リフタ 11、排気ダクト 12、温度検出器 13、排気ブロア 14、製品排出口 15.16  メータリレー 17、バーナ 18、油量調節弁 FIG. 1 is a schematic diagram of a drying apparatus for implementing the present invention. FIG. 2 is a sectional view taken along line A-A in FIG. 1 Rotary dryer with crushing stirring blades 2 Drum 3. Motor I 4. Crushing stirring blade 5. Motor... 6. Input hopper 7. Screw conveyor 8 Motor m 9.Hot stove 10, Lifter 11. Exhaust duct 12. Temperature detector 13. Exhaust blower 14. Product outlet 15.16 Meter relay 17, Burna 18, Oil amount control valve

Claims (1)

【特許請求の範囲】 1、汚泥等の泥状物を破砕攪拌翼を有する回転乾燥機を
用いて乾燥する方法において、 乾燥機からの排気ガス温度を検出し、この検出値と 乾燥機のドラムの回転にかかる所要動力または破砕攪拌
翼の回転にかかる所要動力もしくはトルクを検出し、こ
の検出値との 2つの検出値の関係から乾燥機へ投入する泥状物の量を
調整することを特徴とする回転乾燥機による泥状物の乾
燥方法 2、前記2つの検出値の関係から乾燥機へ供給する熱量
を調整することを特徴とする請求項1記載の回転乾燥機
による泥状物の乾燥方法
[Claims] 1. In a method of drying muddy materials such as sludge using a rotary dryer having crushing and stirring blades, the temperature of the exhaust gas from the dryer is detected, and this detected value is combined with the drum of the dryer. It is characterized by detecting the required power required for rotation of the crushing agitation blade or the required power or torque required for rotation of the crushing stirring blade, and adjusting the amount of slurry to be fed into the dryer based on the relationship between this detected value and the two detected values. 2. A method for drying mud by a rotary dryer according to claim 1, wherein the amount of heat supplied to the dryer is adjusted based on the relationship between the two detected values. Method
JP2280306A 1990-10-18 1990-10-18 Continuous drying method of sludge by rotary dryer Expired - Fee Related JP2981271B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2280306A JP2981271B2 (en) 1990-10-18 1990-10-18 Continuous drying method of sludge by rotary dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2280306A JP2981271B2 (en) 1990-10-18 1990-10-18 Continuous drying method of sludge by rotary dryer

Publications (2)

Publication Number Publication Date
JPH04157000A true JPH04157000A (en) 1992-05-29
JP2981271B2 JP2981271B2 (en) 1999-11-22

Family

ID=17623155

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2280306A Expired - Fee Related JP2981271B2 (en) 1990-10-18 1990-10-18 Continuous drying method of sludge by rotary dryer

Country Status (1)

Country Link
JP (1) JP2981271B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5435923A (en) * 1992-03-20 1995-07-25 Bio Gro Systems, Inc. Method for the treatment of sewage sludge and the like
US5679262A (en) * 1995-02-13 1997-10-21 Bio Gro Systems, Inc. Method for alkaline treatment of sewage sludge for beneficial use
JP2008051399A (en) * 2006-08-24 2008-03-06 Takuma Co Ltd Drier, control device for it, and control method for drier
JP2011067787A (en) * 2009-09-28 2011-04-07 Okawara Mfg Co Ltd Method for operating drying equipment
CN104891772A (en) * 2015-06-29 2015-09-09 丁巧娜 Separator of anti-blocking mechanism
CN109928597A (en) * 2019-03-28 2019-06-25 北京科技大学 Excess sludge depth drying equipment system and method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5435923A (en) * 1992-03-20 1995-07-25 Bio Gro Systems, Inc. Method for the treatment of sewage sludge and the like
US5679262A (en) * 1995-02-13 1997-10-21 Bio Gro Systems, Inc. Method for alkaline treatment of sewage sludge for beneficial use
JP2008051399A (en) * 2006-08-24 2008-03-06 Takuma Co Ltd Drier, control device for it, and control method for drier
JP2011067787A (en) * 2009-09-28 2011-04-07 Okawara Mfg Co Ltd Method for operating drying equipment
CN104891772A (en) * 2015-06-29 2015-09-09 丁巧娜 Separator of anti-blocking mechanism
CN109928597A (en) * 2019-03-28 2019-06-25 北京科技大学 Excess sludge depth drying equipment system and method

Also Published As

Publication number Publication date
JP2981271B2 (en) 1999-11-22

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