JPH0351038Y2 - - Google Patents
Info
- Publication number
- JPH0351038Y2 JPH0351038Y2 JP20272285U JP20272285U JPH0351038Y2 JP H0351038 Y2 JPH0351038 Y2 JP H0351038Y2 JP 20272285 U JP20272285 U JP 20272285U JP 20272285 U JP20272285 U JP 20272285U JP H0351038 Y2 JPH0351038 Y2 JP H0351038Y2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- sol
- heating chamber
- movable weir
- level
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000010802 sludge Substances 0.000 claims description 50
- 238000010438 heat treatment Methods 0.000 claims description 22
- 238000007599 discharging Methods 0.000 claims description 2
- 239000012530 fluid Substances 0.000 description 8
- 230000007423 decrease Effects 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 230000002411 adverse Effects 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Treatment Of Sludge (AREA)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
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と共に加熱する回転羽根
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た汚泥用乾燥機に関す
る。[Detailed description of the invention] [Industrial application field] The present invention is a horizontal drum-shaped heating chamber, in which rotating blades that transfer and heat sludge in the longitudinal direction of the heating chamber are moved by a drive device to rotate the rotary blades, which are axially directed in the longitudinal direction. The present invention relates to a sludge dryer that is rotatably provided around the heating chamber and has a supply path for supplying sol-like sludge and a discharge path for discharging gel-like sludge, which are connected to the heating chamber.
従来、第4図イに示すように、加熱室3内のゾ
ル状汚泥Sを排出路7側に正常域で堆積するゲル
状汚泥Gの作用により十分な厚さで貯留するよう
に構成し、回転羽根8等でゾル状汚泥Sを接触加
熱するように構成していた。
Conventionally, as shown in FIG. 4A, the sol-like sludge S in the heating chamber 3 is stored in a sufficient thickness by the action of the gel-like sludge G that normally accumulates on the discharge path 7 side, It was configured to contact and heat the sol-like sludge S with the rotating blades 8 and the like.
しかし、例えば供給路5からのゾル状汚泥の含
水率が増大する等が原因で、ゲル状汚泥Gの堆積
範囲が正常域から排出路7側に狭くなると、加熱
室3内のゾル状汚泥Sの上面レベルが、第4図ロ
のようにかなり低下し、回転羽根8とゾル状汚泥
Sの接触面積が大巾に減少して、加熱能力低下が
顕著になる危険性があり、一層の改良の余地があ
つた。
However, if the accumulation range of the gelled sludge G narrows from the normal range toward the discharge channel 7 side due to an increase in the water content of the sol-like sludge from the supply channel 5, for example, the sol-like sludge S in the heating chamber 3 becomes There is a risk that the upper surface level will drop considerably as shown in Figure 4 (b), and the contact area between the rotating blade 8 and the sol-like sludge S will decrease significantly, leading to a noticeable decrease in heating capacity. There was room for.
本考案の目的は、たとえゲル状汚泥の堆積範囲
が正常域から排出路側に狭くなつても、ゾル状汚
泥と回転羽根との接触面積を大に維持できるよう
に、しかも、そのための構成を、ゲル状汚泥の堆
積範囲が正常域である時に乾燥に悪影響を及ぼさ
ないものにする点にある。 The purpose of the present invention is to maintain a large contact area between the sol sludge and the rotating blades even if the range of gel sludge accumulation narrows from the normal area to the discharge path side, and to create a configuration for this purpose. The purpose is to make it so that it does not adversely affect drying when the gel sludge is deposited in a normal range.
〔問題を解決するための手段)
本考案の特徴構成は、汚泥の移送と加熱のため
の回転羽根を内装した加熱室内のうちゾル状汚泥
を収容する部分に、ゾル状汚泥を設定レベル以上
でオーバーフローさせる可動堰を、作用位置と非
作用位置とに移動操作自在に設けた事にあり、そ
の作用効果は次の通りである。[Means for solving the problem] The characteristic configuration of the present invention is that sol-like sludge is stored at a level higher than a set level in a heating chamber equipped with rotating blades for transferring and heating sludge. The movable weir for causing overflow is provided so as to be freely movable between an active position and a non-active position, and its effects are as follows.
〔作用〕
つまり、第3図イに示すように、ゲル状汚泥G
が正常域で堆積して、ゾル状汚泥Sが十分な厚さ
で貯留されている時には、可動堰16を十分に低
い非作用位置に配置して、ゾル状汚泥Sの移送が
可動堰16により悪影響を受けないようにし、効
率良く汚泥を乾燥できる。[Effect] In other words, as shown in Figure 3A, gel sludge G
When the sol-like sludge S is accumulated in a normal range and the sol-like sludge S is stored in a sufficient thickness, the movable weir 16 is placed at a sufficiently low non-working position so that the transfer of the sol-like sludge S is carried out by the movable weir 16. Sludge can be dried efficiently without any negative effects.
第3図ロに示すように、ゲル状汚泥Gの堆積範
囲が正常域から排出路7側に狭くなつて、ゾル状
汚泥Sの上面レベルが異常低下する危険性がある
場合、ゾル状汚泥Sを設定レベルL以上でオーバ
ーフローさせる作用位置に可動堰16を配置し
て、ゾル状汚泥Sを加熱用回転羽根8と十分に接
触する厚さに維持して、汚泥乾燥能力を十分に発
揮させることができる。 As shown in Figure 3B, when the accumulation range of gel sludge G narrows from the normal area toward the discharge channel 7 side and there is a risk that the upper surface level of sol sludge S decreases abnormally, sol sludge A movable weir 16 is arranged at a position where the sludge sludge S overflows at a set level L or above, and the thickness of the sol-form sludge S is maintained to be sufficient to contact the rotating heating blade 8, thereby fully demonstrating the sludge drying ability. I can do it.
その結果、汚泥の性状等による悪影響を受ける
ことなく、常に十分に大きい乾燥能力を確実に発
揮して、汚泥乾燥処理を能率良くかつ熱効率良く
行えるようになつた。
As a result, the sludge drying process can now be carried out efficiently and thermally efficiently by always reliably exhibiting a sufficiently large drying capacity without being adversely affected by the properties of the sludge.
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
に架設してある。そして、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,9b夫々に形成し、電動モータ13
a及び変速機13b等から成る駆動装置13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1
5a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により接続してある。
もつて、供給路5から連続的に投入されるゾル状
汚泥Sを、両回転軸9a,9bの回転羽根8によ
つて撹拌しながら排出路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、15c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. , 9b are installed side by side in the heating chamber 3. A fluid chamber 10 is formed in each of the rotating blades 8, and a heated fluid supply path 11 and a discharge path 12 connected to each of the fluid chambers 10 are formed in each of the rotating shafts 9a and 9b.
A drive device 13 consisting of a transmission 13b, etc.
The two rotating shafts 9a and 9b are interlocked 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 the supply pipe 1.
5a, and is also connected to the supply path 11 of both rotating shafts 9a, 9b by a supply pipe 15b.
At the same time, the sol-like sludge S continuously introduced from the supply channel 5 is transferred to the discharge channel 7 side while being stirred by the rotating blades 8 of both rotating shafts 9a and 9b.
The sludge is heated and dried by the high-temperature fluid supplied to the jacket 1 and the fluid chamber 10 and dried into a gel-like state, and the sludge is continuously collected from the discharge path 7. In addition, 15c is the jacket 1 and the fluid chamber 10.
It is a fluid discharge path from.
加熱室3のうちゾル状汚泥Sを収容する部分
に、可動堰16を駆動装置17で上下摺動操作自
在に設けて、ゾル状汚泥Sを回転羽根8との接触
が十分な設定レベルL以上でオーバーフローさせ
る作用位置と、加熱室3の内底面より以下の非作
用位置にわたつて可動堰16を移動操作自在に構
成してある。18は、非作用位置の可動堰16を
収容するケースである。 A movable weir 16 is provided in a portion of the heating chamber 3 that accommodates the sol-like sludge S so that it can be slid up and down by a drive device 17, so that the sol-like sludge S is brought into sufficient contact with the rotary blades 8 at a setting level L or higher. The movable weir 16 is configured to be movable between an active position for causing overflow and a non-active position below from the inner bottom surface of the heating chamber 3. 18 is a case that accommodates the movable weir 16 in a non-operating position.
加熱室3内のゾル状汚泥Sの上面レベルが設定
レベルL以上であるか否かを検出する、例えば静
電容量式等のセンサー20を可動堰16の上流側
に設け、そのセンサー20からの情報に基いて駆
動装置17を自動操作する制御器22を設けて、
第3図イに示すように、センサー20により検出
した汚泥レベルが設定レベルL以上であると可動
堰16を非作用位置に、かつ、第3図ロに示すよ
うに、センサー20により検出した汚泥レベルが
設定レベルL未満であると可動堰16を作用位置
に設定時間だけ、夫々配置して、ゾル状汚泥Sの
厚さ減少による加熱能力低下を防止できるように
構成してある。 A sensor 20, such as a capacitive type, for detecting whether the upper surface level of the sol-form sludge S in the heating chamber 3 is equal to or higher than the set level L is provided on the upstream side of the movable weir 16, and the A controller 22 is provided to automatically operate the drive device 17 based on the information,
As shown in FIG. 3A, when the sludge level detected by the sensor 20 is equal to or higher than the set level L, the movable weir 16 is set to the non-operating position, and as shown in FIG. 3B, the sludge level detected by the sensor 20 is When the level is less than the set level L, the movable weir 16 is placed in the operating position for a set time, so that a reduction in heating capacity due to a decrease in the thickness of the sol-like sludge S can be prevented.
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、例えば連続螺施形状
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。 When forming the rotary vane 8, the shape can be freely changed, for example, by making it into a continuous screw shape, and the specific configuration of the driving device 13 for the rotary vane 8 can be changed in various ways.
可動堰16を移動自在に取付ける構成や移動操
作する構成は適当に変更でき、例えば、人為的に
移動すべく構成したり、センサー20による検出
レベルに見合つて設定レベルに可動堰16を連続
的又は多段に自動レベル調整するように構成して
もよく、また、可動堰16に対する駆動装置17
としてはトルクモータや流体圧シリンダー、その
他適当なものを選択できる。 The configuration in which the movable weir 16 is movably mounted and the configuration in which it is moved can be changed as appropriate. For example, the movable weir 16 may be configured to be moved manually, or the movable weir 16 may be moved continuously or at a set level in accordance with the detection level by the sensor 20. It may be configured to automatically adjust the level in multiple stages, and the drive device 17 for the movable weir 16
For example, a torque motor, a hydraulic cylinder, or any other suitable device can be selected.
第1図ないし第3図は本考案の実施例を示し、
第1図は乾燥機の概略断面図、第2図は第1図の
−線断面図、第3図イ及びロは夫々加熱室内
のゾル状及びゲル状汚泥分布状態の説明図であ
る。第4図イ及びロは従来例の説明図である。
3……加熱室、5……供給路、7……排出路、
8……回転羽根、13……駆動装置、L……設定
レベル、S……ゾル状汚泥、G……ゲル状汚泥。
1 to 3 show embodiments of the present invention,
FIG. 1 is a schematic sectional view of the dryer, FIG. 2 is a sectional view taken along the line -- in FIG. 1, and FIGS. 3A and 3B are explanatory views of the distribution of sol-like and gel-like sludge in the heating chamber, respectively. FIGS. 4A and 4B are explanatory diagrams of a conventional example. 3... Heating chamber, 5... Supply path, 7... Discharge path,
8... Rotating vane, 13... Drive device, L... Setting level, S... Sol sludge, G... Gel sludge.
Claims (1)
泥を移送すると共に加熱する回転羽根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内のうちゾル状汚泥Sを収
容する部分に、ゾル状汚泥Sを設定レベルL以上
でオーバーフローさせる可動堰16を、作用位置
と非作用位置とに移動操作自在に設けてある汚泥
用乾燥機。 A rotary blade 8 that transfers and heats sludge in the longitudinal direction of the horizontal drum-shaped heating chamber 3 is provided rotatably around an axis extending in the longitudinal direction by a drive device 13, and supplies sol-like sludge S. The supply path 5 and the discharge path 7 for discharging the gelled sludge G,
A movable weir 16 that is a sludge dryer formed in communication with the heating chamber 3 and causes the sol-form sludge S to overflow at a set level L or higher in a portion of the heating chamber 3 that accommodates the sol-form sludge S. A sludge dryer that can be moved freely between working and non-working positions.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20272285U JPH0351038Y2 (en) | 1985-12-27 | 1985-12-27 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20272285U JPH0351038Y2 (en) | 1985-12-27 | 1985-12-27 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62109800U JPS62109800U (en) | 1987-07-13 |
| JPH0351038Y2 true JPH0351038Y2 (en) | 1991-10-31 |
Family
ID=31167371
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20272285U Expired JPH0351038Y2 (en) | 1985-12-27 | 1985-12-27 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0351038Y2 (en) |
-
1985
- 1985-12-27 JP JP20272285U patent/JPH0351038Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62109800U (en) | 1987-07-13 |
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