JPS6236051Y2 - - Google Patents

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Publication number
JPS6236051Y2
JPS6236051Y2 JP6100183U JP6100183U JPS6236051Y2 JP S6236051 Y2 JPS6236051 Y2 JP S6236051Y2 JP 6100183 U JP6100183 U JP 6100183U JP 6100183 U JP6100183 U JP 6100183U JP S6236051 Y2 JPS6236051 Y2 JP S6236051Y2
Authority
JP
Japan
Prior art keywords
sludge
heating chamber
gelled
longitudinal direction
dryer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP6100183U
Other languages
Japanese (ja)
Other versions
JPS59167393U (en
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 filed Critical
Priority to JP6100183U priority Critical patent/JPS59167393U/en
Publication of JPS59167393U publication Critical patent/JPS59167393U/en
Application granted granted Critical
Publication of JPS6236051Y2 publication Critical patent/JPS6236051Y2/ja
Granted legal-status Critical Current

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

Description

【考案の詳細な説明】 本考案は、横型ドラム状加熱室内に、その長手
方向に汚泥を移送する回転羽根を、駆動装置によ
り前記長手方向に向かう軸芯周りで回転自在に設
け、ゾル状汚泥を供給する供給路、及び、ゲル状
汚泥を排出する排出路を、前記加熱室に連通して
形成し、下水汚泥等の水処理汚泥や産業廃棄物汚
泥などの各種汚泥を連続的に処理する乾燥機に関
する。
[Detailed description of the invention] The present invention provides rotating blades for transferring sludge in the longitudinal direction of the horizontal drum-shaped heating chamber, which are rotatable around an axis in the longitudinal direction by a drive device. A supply channel for supplying sludge and a discharge channel for discharging gel-like sludge are formed in communication with the heating chamber, and various sludges such as water treatment sludge such as sewage sludge and industrial waste sludge are continuously treated. Regarding dryers.

上記乾燥機により汚泥を乾燥する場合、乾燥機
の能力を十分に発揮させると共に、適度に乾燥さ
れかつ細分化されたゲル状汚泥を得るためには、
第3図イに示すように、加熱室の排出路側に適切
な範囲にわたつてゲル状汚泥の堰を形成させる必
要がある。
When drying sludge using the dryer described above, in order to fully utilize the dryer's ability and obtain appropriately dried and finely divided gel-like sludge,
As shown in FIG. 3A, it is necessary to form a weir of gel-like sludge over an appropriate area on the discharge path side of the heating chamber.

他方、従来の乾燥機においては、内部を目視し
ない限り、加熱室内のゲル状汚泥分布状態を検出
することが不可能であり、排出路から回収される
ゲル状汚泥の状態で見当を付けるしかなかつた。
しかし、実際上、加熱室に供給されるゲル状汚泥
の量や含水率が増大して、第3図ロに示すよう
に、ゲル状汚泥Gの堰が排出路7側に移動して、
十分に乾燥されていない汚泥や大き過ぎる塊りの
汚泥が排出されると共に、加熱室3内汚泥量が少
くなつて処理能力が低下したり、あるいは、第3
図ハに示すように、ゲル状汚泥Gの堰が供給路5
側に移動して、ゲル状汚泥Gが過乾燥と回転羽根
8による過度の細分化で微粉化する等のトラブル
を生じやすく、また、そのようなトラブルを生じ
ると、適正なゲル状汚泥分布状態への復元に長時
間を要し、かつ、その間乾燥処理量が大巾に低下
する欠点があつた。
On the other hand, in conventional dryers, it is impossible to detect the distribution of gelled sludge inside the heating chamber without visually inspecting the interior, and the only way to get an idea is by looking at the state of the gelled sludge collected from the discharge channel. Ta.
However, in reality, as the amount and moisture content of the gelled sludge supplied to the heating chamber increase, the weir of the gelled sludge G moves toward the discharge path 7, as shown in FIG.
Sludge that has not been dried sufficiently or sludge that is too large is discharged, and the amount of sludge in the heating chamber 3 decreases, reducing the processing capacity.
As shown in Figure C, the weir of gelled sludge G is connected to the supply channel 5.
If the gelled sludge G moves to the side, it is easy to cause problems such as overdrying and excessive fragmentation by the rotating blades 8, such as pulverization. The disadvantage was that it took a long time to restore the drying process, and the amount of drying was significantly reduced during that time.

本考案の目的は、上記実情に鑑みて、加熱室内
のゲル状汚泥分布状態を確実に検出できるように
する点にある。
In view of the above-mentioned circumstances, an object of the present invention is to enable reliable detection of the gelled sludge distribution state within the heating chamber.

本考案による乾燥機の特徴構成は、横型ドラム
状加熱室内の汚泥の上面レベルを検出する接触式
あるいは無接触式センサーを、加熱室長手方向に
並設し、センサーからの情報に基いて加熱室内の
ゲル状汚泥分布状態を判定する装置を設けたこと
にあり、その作用効果は次の通りである。
The characteristic structure of the dryer according to the present invention is that contact or non-contact sensors are arranged in parallel in the longitudinal direction of the heating chamber to detect the upper surface level of sludge in the horizontal drum-shaped heating chamber. The purpose of this invention is to provide a device for determining the distribution state of gel-like sludge, and its effects are as follows.

つまり、加熱室内の汚泥は、第3図イないしハ
に示すように、ゲル状汚泥Gのゾル状汚泥S側部
分が高くなるのであり、センサーのいずれが高い
汚泥上面を検出しているかによつて、ゲル状汚泥
Gの存在範囲がいずれであるかが判明するのであ
り、このような判断を判定用装置により自動的に
行わせることにより、加熱室3内のゲル状汚泥分
布状態が適正であるか否かが確実に判るのであ
る。
In other words, as shown in Figure 3 A to C, the sludge in the heating chamber is higher on the sol-like sludge S side of the gel-like sludge G, and it depends on which sensor detects the higher sludge top surface. Therefore, it becomes clear which range the gelled sludge G exists in. By automatically making such a judgment using the determination device, it is possible to determine whether the gelled sludge distribution state in the heating chamber 3 is appropriate. It is possible to know for sure whether it is there or not.

したがつて、例えば、判定用装置によつて操作
されるゲル状汚泥分布表示装置に基いて人為的
に、あるいは、判定用装置に連係した制御器によ
つて自動的に、ゲル状汚泥分布状態を適正な状態
に復元させるための操作、つまりゾル状汚泥投入
量の増減、汚泥移送用回転羽根の変速や逆転、加
熱室を形成するケーシングの傾斜角変更、あるい
は、ゾル状汚泥の供給位置変更等を適切に行つ
て、適正なゲル状汚泥分布状態を容易かつ確実に
維持させることができるようになり、乾燥機の能
力を十分に発揮させながら、適度に乾燥されかつ
細分化されたゲル状汚泥が得られる良好な運転
を、長期にわたつて確実に、かつ、容易に継続で
きるようになつた。
Therefore, for example, the gelled sludge distribution state can be determined manually based on a gelled sludge distribution display device operated by a determination device, or automatically by a controller linked to the determination device. operations to restore the sludge to its proper state, such as increasing or decreasing the amount of sol-like sludge input, changing or reversing the speed of the rotary blade for sludge transfer, changing the inclination angle of the casing that forms the heating chamber, or changing the supply position of the sol-like sludge. By doing the following, it is now possible to easily and reliably maintain an appropriate gel-like sludge distribution state, and while making full use of the dryer's ability, the gel-like sludge is properly dried and finely divided. It has become possible to reliably and easily continue good operation that yields sludge over a long period of time.

次に、実施例を示す。 Next, examples will be shown.

第1図及び第2図に示すように、ジヤケツト1
を備えたケーシング2によつて横型ドラム状加熱
室3を形成し、ポンプ流路4からのゾル状汚泥を
加熱室3にその長手方向一端側から供給する供給
路5を形成し、加熱室3の長手方向他端側からゲ
ル状汚泥を高さ変更可能な堰板19に対してオー
バーフローさせて回収コンベア6に排出する排出
路7を形成し、多数の回転羽根8を並設した回転
軸9a,9bの2本を、左右に並べて加熱室3内
に架設し、回転羽根8夫々に流体室10を形成す
ると共に、それら流体室10夫々に接続した加熱
流体供給路11及び排出路12を回転軸9a,9
b夫々に形成し、電動モータ13a及び正逆転切
換操作自在な変速機13b等から成る駆動装置1
3を、2本の回転軸9a,9bにそれらが逆回転
になるように連動させ、ボイラー等の高温流体供
給装置14を、ケーシング2のジヤケツト1に供
給管15aにより接続すると共に両回転軸9a,
9bの供給路11に供給管15bにより接続し、
もつて、供給路5から連続的に投入されるゾル状
汚泥を、正転する両回転軸9a,9bの回転羽根
8によつて攪拌しながら排出路7側に移送すると
共に、ジヤケツト1及び流体室10に供給される
高温流体によつて加熱乾燥し、ゲル状に乾燥され
た汚泥を排出路7から連続的に回収するように構
成してある。尚、16はジヤケツト1及び流体室
10からの流体排出路である。
As shown in FIGS. 1 and 2, the jacket 1
A horizontal drum-shaped heating chamber 3 is formed by a casing 2 provided with A rotating shaft 9a is formed with a discharge path 7 through which the gelled sludge overflows from the other end in the longitudinal direction against a weir plate 19 whose height can be changed and is discharged to a collection conveyor 6, and a rotating shaft 9a has a large number of rotating blades 8 arranged in parallel. . Axis 9a, 9
A drive device 1 is formed in each of b and includes an electric motor 13a, a transmission 13b that can be freely switched between forward and reverse directions, and the like.
3 is interlocked with two rotating shafts 9a and 9b so that they rotate in opposite directions, and a high-temperature fluid supply device 14 such as a boiler is connected to the jacket 1 of the casing 2 through a supply pipe 15a, and both rotating shafts 9a ,
Connected to the supply path 11 of 9b by a supply pipe 15b,
As a result, the sol-like sludge continuously introduced from the supply path 5 is transferred to the discharge path 7 side while being stirred by the rotating blades 8 of the rotating shafts 9a and 9b that rotate normally, and the jacket 1 and the fluid are The sludge is heated and dried by the high-temperature fluid supplied to the chamber 10 and dried into a gel-like state, and the sludge is continuously collected from the discharge path 7. Note that 16 is a fluid discharge path from the jacket 1 and the fluid chamber 10.

加熱室3内の汚泥の上面レベルを検出する多数
の接触式センサー17を、加熱室長手方向に並設
し、それらセンサー17からの情報に基いて、加
熱室3内ゲル状汚泥分布状態が、第3図イに示す
適正状態であるか、あるいは、第3図ロ又はハに
示す不良状態であるかを判定する装置25を設
け、その判定用装置25からの情報により、第3
図ロのようにゲル状汚泥Gの堰が排出路7側に移
動すると、回転羽根8を逆転するように変速機1
3bを自動操作し、かつ、第3図ハに示すように
ゲル状汚泥Gの堰が供給路5側に移動すると、回
転羽根8の正転速度を増大するように変速機13
bを自動操作する制御器18を設けて、第3図イ
に示す適正なゲル状汚泥分布状態が自動的に維持
されるように構成してある。また、判定用装置2
5によつて操作される適宜型式の表示装置26を
設けて、加熱室3内のゲル状汚泥分布状態が一目
で判るようにしてある。
A large number of contact sensors 17 for detecting the upper surface level of sludge in the heating chamber 3 are arranged in parallel in the longitudinal direction of the heating chamber, and based on the information from these sensors 17, the distribution state of gelled sludge in the heating chamber 3 is determined as follows: A device 25 is provided for determining whether the state is proper as shown in FIG. 3A or is in a defective state as shown in FIG.
When the weir of gelatinous sludge G moves toward the discharge path 7 as shown in Figure B, the transmission 1 rotates the rotary blades 8 in the opposite direction.
3b is automatically operated, and when the weir of gelatinous sludge G moves toward the supply path 5 side as shown in FIG.
A controller 18 is provided to automatically operate the controller 18, so that the proper gelled sludge distribution state shown in FIG. 3A is automatically maintained. In addition, the determination device 2
A suitable type of display device 26 operated by the heating chamber 3 is provided so that the state of gel sludge distribution within the heating chamber 3 can be seen at a glance.

つまり、第3図ロのようになると、ゲル状汚泥
Gが十分乾燥されないで排出されたり、ゾル状汚
泥Sが排出路7に流入したり、あるいは、乾燥不
足のためゲル状汚泥Gが大きな塊りで排出された
りする等のトラブルを生じ、また、第3図ハのよ
うになると、ゲル状汚泥Gが過乾燥になり、回転
羽根8で細断され過ぎて微粉化してしまうのであ
るが、そのような不都合な事態を自動的に防止す
るように構成すると共に、良好な運転になつてい
るか否かを容易確実に判断できるように構成して
ある。
In other words, if the condition shown in Fig. 3B occurs, the gel sludge G may be discharged without being sufficiently dried, the sol sludge S may flow into the discharge channel 7, or the gel sludge G may form large clumps due to insufficient drying. However, if the gelatinous sludge G becomes too dry and is shredded by the rotary blades 8, it becomes fine powder. The system is configured to automatically prevent such inconvenient situations, and is also configured to easily and reliably determine whether or not the vehicle is operating properly.

前記センサー17を構成するに、第2図及び第
4図に示すように、ケーシング2に固定したブラ
ケツト17aに、汚泥に対する受圧板17bを、
回転軸9a,9bとほぼ平行なピン17cにより
揺動自在にかつ自重によりほぼ鉛直な姿勢になる
ように取付け、受圧板17bの下端側を、回転羽
根8により回動する汚泥の押圧力が効率良く作用
するように屈曲形成し、ワイヤー17dにより受
圧板17bに連動された検出部17eを加熱室3
外に設け、もつて、受圧板17bの揺動角に基い
て汚泥上面レベルを検出するように構成してあ
る。
To configure the sensor 17, as shown in FIGS. 2 and 4, a pressure receiving plate 17b for sludge is attached to a bracket 17a fixed to the casing 2.
It is mounted so that it can swing freely using pins 17c that are substantially parallel to the rotating shafts 9a and 9b, and that it assumes a substantially vertical posture due to its own weight. The detection part 17e, which is bent to work well and linked to the pressure receiving plate 17b by a wire 17d, is connected to the heating chamber 3.
It is provided outside the pressure receiving plate 17b and is configured to detect the sludge upper surface level based on the swing angle of the pressure receiving plate 17b.

次に、別の実施例を示す。 Next, another example will be shown.

加熱室3を形成するに、例えば回転羽根8を備
えた回転軸9a,9bが1本の場合にほぼ円筒状
にする等、形状を自由に変更でき、また、その他
の具体構造における各種構成変更が可能である。
To form the heating chamber 3, the shape can be freely changed, such as making it almost cylindrical when there is only one rotating shaft 9a, 9b equipped with the rotating blade 8, and various other configuration changes can be made in the specific structure. is possible.

回転羽根8を形成するに、例えば連続螺旋形状
にする等、形状を自由に変更でき、また、回転羽
根8の駆動装置13の具体的構成は各種変更自在
である。
The shape of the rotary vanes 8 can be freely changed, for example to a continuous spiral shape, and the specific configuration of the drive device 13 for the rotary vanes 8 can be freely changed in various ways.

汚泥上面レベルを検出するセンサー17を構成
するに、例えば、検出部17eをリミツトスイツ
チ式、近接スイツチ式、フイトスイツチ式、可変
抵抗式、誘導電流式等にしたり、あるいは、光投
射方式や超音波投射方式等の無接触式に構成する
等、その他各種の構成変更が可能である。
To configure the sensor 17 for detecting the upper surface level of sludge, for example, the detection section 17e may be of a limit switch type, a proximity switch type, a foot switch type, a variable resistance type, an induced current type, or a light projection type or an ultrasonic projection type. Various other configuration changes are possible, such as a non-contact configuration.

ゲル状汚泥分布状態を判定する装置25からの
情報をいかに利用するかは各種変更が可能であ
り、例えば、単に表示装置26を付設するだけに
して、回転羽根用変速機13bの操作、ケーシン
グ2の傾斜角を変更する装置の操作、加熱室3へ
のゾル状汚泥供給位置を変更する装置の操作等の
対処操作を人為的に行わせたり、あるいは、制御
器によつてそれら対処操作を単独であるいは適当
に組合わせて行わせてもよい。
Various changes can be made in how the information from the device 25 for determining the gelled sludge distribution state is used. For example, by simply adding the display device 26, the operation of the rotary vane transmission 13b, the casing 2 Countermeasure operations such as operating a device to change the inclination angle of the heating chamber 3 and operating a device to change the position of supplying sol-form sludge to the heating chamber 3 may be performed manually, or these countermeasure operations may be performed independently using a controller. It may be carried out either by itself or by a suitable combination.

加熱室3内の汚泥を加熱するための方式や具体
的構造は、汚泥の性状や乾燥機設置状況等に見合
つて適宜変更可能である。
The method and specific structure for heating the sludge in the heating chamber 3 can be changed as appropriate depending on the properties of the sludge, the installation status of the dryer, and the like.

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

第1図は乾燥機の概略縦断面図、第2図は第1
図の−線断面図、第3図イないしハは夫々加
熱室内のゲル状汚泥分布状態の説明図、第4図は
第2図の−線矢視図である。 3……加熱室、5……供給路、7……排出路、
8……回転羽根、13……駆動装置、17……セ
ンサー、25……判定用装置、S……ゾル状汚
泥、G……ゲル状汚泥。
Figure 1 is a schematic vertical cross-sectional view of the dryer, Figure 2 is the
3A to 3C are explanatory diagrams of the gelled sludge distribution state in the heating chamber, respectively, and FIG. 4 is a view taken along the - line in FIG. 2. 3... Heating chamber, 5... Supply path, 7... Discharge path,
8... Rotating vane, 13... Drive device, 17... Sensor, 25... Judgment device, S... Sol-like sludge, G... Gel-like sludge.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 横型ドラム状加熱室3内に、その長手方向に汚
泥を移送する回転羽根8を、駆動装置13により
前記長手方向に向かう軸芯周りで回転自在に設
け、ゾル状汚泥Sを供給する供給路5、及び、ゲ
ル状汚泥Gを排出する排出路7を、前記加熱室3
に連通して形成した汚泥用乾燥機であつて、前記
加熱室3内の汚泥S,Gの上面レベルを検出する
センサー17を、前記加熱室長手方向に並設し、
それらセンサー17からの情報に基いて前記加熱
室3内のゲル状汚泥分布状態を判定する装置25
を設けてある汚泥用乾燥機。
In the horizontal drum-shaped heating chamber 3, a rotary blade 8 for transferring sludge in the longitudinal direction is provided rotatably around an axis in the longitudinal direction by a drive device 13, and a supply path 5 for supplying the sol-like sludge S. , and the discharge passage 7 for discharging the gelled sludge G is connected to the heating chamber 3.
A sludge dryer formed in communication with a sludge dryer, in which sensors 17 for detecting the upper surface level of sludge S and G in the heating chamber 3 are arranged in parallel in the longitudinal direction of the heating chamber,
A device 25 that determines the gelled sludge distribution state within the heating chamber 3 based on information from the sensors 17
A sludge dryer equipped with
JP6100183U 1983-04-22 1983-04-22 Sludge dryer Granted JPS59167393U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6100183U JPS59167393U (en) 1983-04-22 1983-04-22 Sludge dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6100183U JPS59167393U (en) 1983-04-22 1983-04-22 Sludge dryer

Publications (2)

Publication Number Publication Date
JPS59167393U JPS59167393U (en) 1984-11-09
JPS6236051Y2 true JPS6236051Y2 (en) 1987-09-12

Family

ID=30191222

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6100183U Granted JPS59167393U (en) 1983-04-22 1983-04-22 Sludge dryer

Country Status (1)

Country Link
JP (1) JPS59167393U (en)

Also Published As

Publication number Publication date
JPS59167393U (en) 1984-11-09

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