JPH08126900A - Sludge dryer - Google Patents
Sludge dryerInfo
- Publication number
- JPH08126900A JPH08126900A JP6266798A JP26679894A JPH08126900A JP H08126900 A JPH08126900 A JP H08126900A JP 6266798 A JP6266798 A JP 6266798A JP 26679894 A JP26679894 A JP 26679894A JP H08126900 A JPH08126900 A JP H08126900A
- Authority
- JP
- Japan
- Prior art keywords
- blower
- thin film
- centrifugal thin
- extraction
- 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.)
- Pending
Links
Landscapes
- Treatment Of Sludge (AREA)
Abstract
(57)【要約】
【構成】 本発明の汚泥乾燥装置は、互いに並列に設置
されて流入された汚泥10を熱風乾燥して排出する複数
の遠心薄膜乾燥機1A,1Bと、遠心薄膜乾燥機1A,
1Bの抽気出口2A,2Bに接続されて汚泥10を乾燥
した後の処理空気を排気する抽気ブロワ7と、抽気ブロ
ワ7と遠心薄膜乾燥機1A,1Bとの間に設置されて処
理空気の排出能力を予め設定する手動ダンパ3A,3B
と、手動ダンパ3A,3Bに直列に接続されて外部から
の開閉制御信号によって遠心薄膜乾燥機1A,1Bの立
ち上げ時には半開とし、その後には全開とする自動ダン
パ4A,4Bとを備えたことを特徴とする。
【効果】 本発明によって遠心薄膜乾燥機の運転を安定
化することが可能である。
(57) [Summary] [Structure] The sludge drying device of the present invention comprises a plurality of centrifugal thin film dryers 1A and 1B which are installed in parallel with each other to dry the inflowing sludge 10 by hot air and to discharge the sludge, 1A,
A bleed air blower 7 connected to the bleed air outlets 2A, 2B of 1B for exhausting the treated air after drying the sludge 10, and a bleed air blower 7 and the centrifugal thin film dryers 1A, 1B installed to discharge the treated air. Manual dampers 3A and 3B for presetting capacity
And automatic dampers 4A, 4B which are connected in series to the manual dampers 3A, 3B and are opened halfway when the centrifugal thin film dryers 1A, 1B are started up by an open / close control signal from the outside and then fully opened thereafter. Is characterized by. According to the present invention, the operation of the centrifugal thin film dryer can be stabilized.
Description
【0001】[0001]
【産業上の利用分野】本発明は下水処理場や一般の排水
処理場において発生する汚泥の汚泥乾燥装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sludge drying device for sludge generated in a sewage treatment plant or a general wastewater treatment plant.
【0002】[0002]
【従来の技術】従来は、2台以上の遠心薄膜乾燥機を有
する汚泥乾燥装置においては、遠心薄膜乾燥機に汚泥が
供給されているときと、そうでないときでは抽気系に生
じる圧力損失が異なるため、遠心薄膜乾燥機の運転台数
を変える必要がある場合は、各々の遠心薄膜乾燥機の抽
気風量を安定させるために、各々に抽気ブロワを設けて
いた。2. Description of the Related Art Conventionally, in a sludge dryer having two or more centrifugal thin film dryers, the pressure loss generated in the extraction system is different when sludge is being supplied to the centrifugal thin film dryer and when it is not. Therefore, when it is necessary to change the number of operating centrifugal thin film dryers, an extraction blower is provided for each centrifugal thin film dryer in order to stabilize the extraction air amount.
【0003】[0003]
【発明が解決しようとする課題】従って遠心薄膜乾燥機
の設置台数が多い場合は、抽気ブロワもその台数分設置
しなければならないという問題点があった。Therefore, when a large number of centrifugal thin film dryers are installed, there is a problem in that the extraction blowers must be installed for that number.
【0004】そこで本発明では、2台以上の遠心薄膜乾
燥機に対して1台の抽気ブロワでの抽気でできる汚泥乾
燥装置を提供する。Therefore, the present invention provides a sludge drying device capable of extracting air with two extraction blowers for two or more centrifugal thin film dryers.
【0005】[0005]
【課題を解決するための手段】本発明の汚泥乾燥装置
は、互いに並列に設置されて流入された汚泥を熱風乾燥
して排出する複数の遠心薄膜乾燥機と、遠心薄膜乾燥機
の熱風出口側に接続されて汚泥を乾燥した後の処理空気
を排気する抽気ブロワと、抽気ブロワと遠心薄膜乾燥機
との間に設置されて処理空気の排出能力を予め設定する
手動ダンパと、手動ダンパに直列に接続されて外部から
の開閉制御信号によって遠心薄膜乾燥機の立ち上げ時に
は半開とし、その後には全開とする自動ダンパとを備え
たことを特徴とする。また、請求項2に記載した汚泥乾
燥装置は、抽気ブロワの運転を回転速度調整式と、抽気
ブロワの後段に抽気ブロワ出口圧力検出器を設け、抽気
ブロワ出口圧力検出器の検出する抽気ブロワ出口圧力検
出値が予め定めた抽気ブロワ出口圧力設定値内になるよ
うに抽気ブロワの回転速度を調整することを特徴として
いる。そして、請求項3に記載した汚泥乾燥装置は、遠
心薄膜乾燥機の熱風出口側に乾燥機出口圧力検出器を設
け、乾燥機出口圧力検出器の検出する乾燥機出口圧力検
出値が予め定めた乾燥機出口圧力設定値内になるように
自動ダンパの開閉度を調整することを特徴としている。
更に、請求項4に記載した汚泥乾燥装置は、抽気ブロワ
の前段に抽気ブロワ入口圧力検出器を設け、抽気ブロワ
入口圧力検出器の検出する抽気ブロワ入口圧力検出値が
予め定めた抽気ブロワ入口圧力設定値内になるように抽
気ブロワの回転速度を調整することを特徴としている。The sludge drying apparatus of the present invention comprises a plurality of centrifugal thin film dryers which are installed in parallel with each other and dry the inflowing sludge by hot air drying, and a hot air outlet side of the centrifugal thin film dryer. Connected to the air extraction blower that exhausts the treated air after drying the sludge, a manual damper installed between the extraction blower and the centrifugal thin film dryer to preset the discharge capacity of the treated air, and in series with the manual damper. It is characterized in that it is provided with an automatic damper which is connected to the semi-open type and is opened halfway when the centrifugal thin-film dryer is started up by an open / close control signal from the outside and then fully opened. Further, in the sludge drying device according to claim 2, the operation of the extraction blower is of a rotation speed adjusting type, and an extraction blower outlet pressure detector is provided at a stage subsequent to the extraction blower, and the extraction blower outlet detected by the extraction blower outlet pressure detector is provided. It is characterized in that the rotation speed of the extraction blower is adjusted so that the detected pressure value is within a predetermined extraction blower outlet pressure set value. In the sludge drying device according to claim 3, a dryer outlet pressure detector is provided on the hot air outlet side of the centrifugal thin film dryer, and the dryer outlet pressure detection value detected by the dryer outlet pressure detector is predetermined. The feature is that the opening / closing degree of the automatic damper is adjusted so that it is within the dryer outlet pressure set value.
Further, in the sludge drying device according to claim 4, a bleed air blower inlet pressure detector is provided in front of the bleed air blower, and the bleed air blower inlet pressure detection value detected by the bleed air blower inlet pressure detector is a predetermined bleed air blower inlet pressure. The feature is that the rotation speed of the extraction blower is adjusted so as to be within the set value.
【0006】[0006]
【作用】本発明の汚泥乾燥装置においては、複数の遠心
薄膜乾燥機を互いに並列に設置して流入された汚泥を熱
風乾燥して排出し、遠心薄膜乾燥機の汚泥出口側に抽気
ブロワを接続して汚泥を乾燥した後の処理空気を排気
し、抽気ブロワと遠心薄膜乾燥機との間に手動ダンパを
設置して処理空気の排出能力を予め設定し、手動ダンパ
に直列に自動ダンパを接続して外部からの開閉制御信号
によって遠心薄膜乾燥機の立ち上げ時には半開とし、そ
の後には全開とすることを特徴とする。また、請求項2
に記載した汚泥乾燥装置は、抽気ブロワの運転を回転速
度調整式とし、抽気ブロワの後段に抽気ブロワ出口圧力
検出器を設け、抽気ブロワ出口圧力検出器の検出する抽
気ブロワ出口圧力検出値が予め定めた抽気ブロワ出口圧
力設定値内になるように抽気ブロワの回転速度を調整す
ることを特徴としている。そして、請求項3に記載した
汚泥乾燥装置は、遠心薄膜乾燥機の熱風出口側に乾燥機
出口圧力検出器を設け、乾燥機出口圧力検出器の検出す
る乾燥機出口圧力検出値が予め定めた乾燥機出口圧力設
定値内になるように自動ダンパの開閉度を調整すること
を特徴としている。更に、請求項4に記載した汚泥乾燥
装置は、抽気ブロワの前段に抽気ブロワ入口圧力検出器
を設け、抽気ブロワ入口圧力検出器の検出する抽気ブロ
ワ入口圧力検出値が予め定めた抽気ブロワ入口圧力設定
値内になるように抽気ブロワの回転速度を調整すること
を特徴としている。In the sludge drying apparatus of the present invention, a plurality of centrifugal thin film dryers are installed in parallel with each other, the inflowing sludge is dried by hot air and discharged, and an extraction blower is connected to the sludge outlet side of the centrifugal thin film dryer. Exhaust the treated air after drying the sludge and set a manual damper between the extraction blower and the centrifugal thin film dryer to set the discharge capacity of the treated air in advance and connect the automatic damper in series with the manual damper. It is characterized in that the centrifugal thin film dryer is half-opened when it is started up by an open / close control signal from the outside and then fully opened. In addition, claim 2
In the sludge drying device described in, the operation of the extraction blower is a rotation speed adjustment type, the extraction blower outlet pressure detector is provided in the subsequent stage of the extraction blower, and the extraction blower outlet pressure detection value detected by the extraction blower outlet pressure detector is set in advance. It is characterized in that the rotation speed of the extraction blower is adjusted so as to be within the set extraction air blower outlet pressure setting value. In the sludge drying device according to claim 3, a dryer outlet pressure detector is provided on the hot air outlet side of the centrifugal thin film dryer, and the dryer outlet pressure detection value detected by the dryer outlet pressure detector is predetermined. The feature is that the opening / closing degree of the automatic damper is adjusted so that it is within the dryer outlet pressure set value. Further, in the sludge drying device according to claim 4, a bleed air blower inlet pressure detector is provided in front of the bleed air blower, and the bleed air blower inlet pressure detection value detected by the bleed air blower inlet pressure detector is a predetermined bleed air blower inlet pressure. The feature is that the rotation speed of the extraction blower is adjusted so as to be within the set value.
【0007】[0007]
【実施例】次に本発明の汚泥乾燥装置の実施例を説明す
る。図1において、遠心薄膜乾燥機1A,1Bは互いに
並列に設置されて流入された汚泥10を熱風乾燥して排
出する。抽気ブロワ7は遠心薄膜乾燥機1A,1Bの熱
風出口側の抽気出口2A,2Bに接続されて汚泥10を
乾燥した後の処理空気を排気する。手動ダンパ3A,3
Bはそれぞれ抽気ブロワ7と遠心薄膜乾燥機1A,1B
との間に設置されて処理空気の排出能力を予め設定す
る。自動ダンパ4A,4Bはそれぞれ手動ダンパ3A,
3Bに直列に接続され、遠心薄膜乾燥機1A,1Bの立
ち上げ時には半開としその後には全開とし、遠心薄膜乾
燥機1A,1Bを使用しない時には全開とする。そし
て、自動ダンパ4A,4Bは抽気配管5に接続され、こ
の抽気配管5にはスクラバ6が抽気ブロワ7の前段に接
続され、排出された空気を冷却すると共に排気する空気
を洗浄する。EXAMPLES Next, examples of the sludge drying apparatus of the present invention will be described. In FIG. 1, centrifugal thin film dryers 1A and 1B are installed in parallel with each other and dry the inflowing sludge 10 and discharge it. The extraction blower 7 is connected to the extraction outlets 2A, 2B on the hot air outlet side of the centrifugal thin film dryers 1A, 1B and discharges the treated air after drying the sludge 10. Manual damper 3A, 3
B is the extraction blower 7 and the centrifugal thin film dryers 1A and 1B, respectively.
It is installed between and to preset the discharge capacity of the processing air. The automatic dampers 4A and 4B are the manual dampers 3A and 4A, respectively.
The centrifugal thin film dryers 1A and 1B are connected to each other in series and half opened when the centrifugal thin film dryers 1A and 1B are started up, and fully opened after that, and fully opened when the centrifugal thin film dryers 1A and 1B are not used. The automatic dampers 4A and 4B are connected to the extraction pipe 5, and a scrubber 6 is connected to the extraction pipe 5 in front of the extraction blower 7 to cool the discharged air and wash the exhausted air.
【0008】図2は請求項2に記載した汚泥乾燥装置の
構成図を示し、抽気ブロワ7の運転を回転速度調整式と
し、抽気ブロワ7の後段に抽気ブロワ出口圧力検出器1
1を設け、抽気ブロワ出口圧力検出器11の検出する抽
気ブロワ出口圧力検出値が予め定めた抽気ブロワ出口圧
力設定値内になるように制御装置8によって抽気ブロワ
7の回転速度を調整する。FIG. 2 is a block diagram of the sludge drying device according to the second aspect of the present invention, in which the operation of the extraction blower 7 is a rotation speed adjustment type, and the extraction blower outlet pressure detector 1 is provided at the subsequent stage of the extraction blower 7.
1 is provided, and the rotation speed of the extraction blower 7 is adjusted by the control device 8 so that the detected value of the extraction blower outlet pressure detected by the extraction blower outlet pressure detector 11 is within the predetermined extraction blower outlet pressure set value.
【0009】図3は、請求項3に記載した汚泥乾燥装置
の構成図を示し、遠心薄膜乾燥機1Aの熱風出口側に乾
燥機出口圧力検出器9を設け、乾燥機出口圧力検出器9
Aの検出する乾燥機出口圧力検出値が予め定めた乾燥機
出口圧力設定値内になるよう制御装置8によって自動ダ
ンパ4Aの開閉度を調整している。FIG. 3 is a block diagram of a sludge drying device according to a third aspect of the present invention, in which a dryer outlet pressure detector 9 is provided on the hot air outlet side of the centrifugal thin film dryer 1A, and the dryer outlet pressure detector 9 is provided.
The opening / closing degree of the automatic damper 4A is adjusted by the control device 8 so that the dryer outlet pressure detection value detected by A is within a predetermined dryer outlet pressure set value.
【0010】図4は請求項4に記載した汚泥乾燥装置の
構成図を示し、抽気ブロワ7の前段に抽気ブロワ入口圧
力検出器9を設け、抽気ブロワ入口圧力検出器9の検出
する抽気ブロワ入口圧力検出値が予め定めた抽気ブロワ
入口圧力設定値内になるように制御装置8によって抽気
ブロワ7の回転速度を調整する。FIG. 4 is a block diagram of the sludge dryer according to the fourth aspect of the present invention, in which a bleeder blower inlet pressure detector 9 is provided in front of the bleeder blower 7, and a bleeder blower inlet detected by the bleeder blower inlet pressure detector 9 is detected. The rotation speed of the extraction blower 7 is adjusted by the control device 8 so that the detected pressure value is within the predetermined extraction blower inlet pressure setting value.
【0011】即ち、図1において説明する、遠心薄膜乾
燥機1A,1Bの抽気出口2A,2Bに手動ダンパ3を
設け、その下流側に中間開度可能な自動ダンパ4A,4
Bを設け、合流した抽気配管5にスクラバ6と抽気ブロ
ク7を設けたことを特徴とする。That is, as shown in FIG. 1, a manual damper 3 is provided at each of the extraction outlets 2A and 2B of the centrifugal thin film dryers 1A and 1B, and automatic dampers 4A and 4 capable of intermediate opening are provided on the downstream side thereof.
B is provided, and a scrubber 6 and an extraction block 7 are provided in the combined extraction pipe 5.
【0012】次に、図2においては、遠心薄膜乾燥機1
の抽気出口2Aに手動ダンパ3Aを設計、その下流側で
遠心薄膜乾燥機1A,1Bごとに抽気配管を合流させ、
中間開度可能な自動ダンパ4A,4Bを設け合流した抽
気配管5にスクラバ6と抽気ブロク7を設け、かつ、遠
心薄膜乾燥機1A,1Bの運転台数により抽気ブロワ7
の回転数を制御する制御装置8を設けたことを特徴とす
る。Next, referring to FIG. 2, the centrifugal thin film dryer 1
A manual damper 3A is designed at the extraction outlet 2A of, and the extraction pipes are joined to each of the centrifugal thin film dryers 1A and 1B on the downstream side,
A scrubber 6 and a bleed block 7 are provided in the bleed pipe 5 that merges with the automatic dampers 4A and 4B capable of intermediate opening, and the bleed blower 7 depends on the number of operating centrifugal thin film dryers 1A and 1B.
A control device 8 for controlling the number of rotations is provided.
【0013】図3においては、遠心薄膜乾燥機1Aの抽
気出口2Aに手動ダンパ3Aを設け、その下流側に中間
開度可能な自動ダンパ4Aを設け、合流した抽気配管5
にスクラバ6と抽気ブロワ7を設計、かつ、抽気出口2
Aと手動ダンパ3Aの間に圧力計9Aを設置し、また、
その圧力計信号により自動ダンパ4Aの開度を調整する
制御装置8を設けたことを特徴とする。In FIG. 3, a manual damper 3A is provided at the extraction outlet 2A of the centrifugal thin film dryer 1A, an automatic damper 4A capable of intermediate opening is provided at the downstream side thereof, and the combined extraction pipe 5 is joined.
The scrubber 6 and the extraction blower 7 are designed and the extraction outlet 2
A pressure gauge 9A is installed between A and the manual damper 3A, and
A control device 8 for adjusting the opening degree of the automatic damper 4A based on the pressure gauge signal is provided.
【0014】図4においては、遠心薄膜乾燥機1Aの抽
気出口2Aに手動ダンパ3Aを設け、その下流側に中間
開度可能な自動ダンパ4Aを設け、合流した抽気配管5
にスクラバ6と抽気ブロワ7を設け、かつ、抽気ブロワ
7の吸込側に圧力計9を設置し、またその圧力計信号に
より抽気ブロワ7の回転数を調節する制御装置を設けた
ことを特徴とする。In FIG. 4, a manual damper 3A is provided at the extraction outlet 2A of the centrifugal thin film dryer 1A, an automatic damper 4A with an intermediate opening degree is provided at the downstream side thereof, and the combined extraction pipe 5 is joined.
The scrubber 6 and the bleeding blower 7 are provided, the pressure gauge 9 is installed on the suction side of the bleeding blower 7, and a control device for adjusting the rotation speed of the bleeding blower 7 is provided by the pressure gauge signal. To do.
【0015】このように構成したので遠心薄膜乾燥機1
Aによって汚泥10は乾燥され乾燥汚泥となる。一方、
乾燥の際発生する蒸発水分は抽気出口2Aよりスクラバ
6へ送られ、冷却除湿され抽気ブロワ7により脱臭装置
など系外へ送り出される。The centrifugal thin film dryer 1 having the above structure
The sludge 10 is dried by A to be dried sludge. on the other hand,
Evaporated water generated during drying is sent to the scrubber 6 through the extraction outlet 2A, cooled and dehumidified, and sent out of the system such as a deodorizing device by the extraction blower 7.
【0016】遠心薄膜乾燥機1Aの抽気風量は乾燥機能
に大きく影響するため、各遠心薄膜乾燥機1A,1Bの
抽気風量をバランスさせるため手動ダンパ3A,3Bを
設けている。、また、遠心薄膜乾燥機1A,1Bが複数
台あり、そのいずれかが休止中となる場合、運転中の遠
心薄膜乾燥機より抽気系の圧損が小さくなるため、休止
中の遠心薄膜乾燥機からの抽気風量が多くなり、逆に運
転中の遠心薄膜乾燥機からの抽気風量が減り、乾燥能力
が落ちてしまうため、抽気風量を調節するための自動ダ
ンパ4A,4Bを設け、休止中の遠心薄膜乾燥機の抽気
風量を制御できるようになっている。Since the extraction air volume of the centrifugal thin film dryer 1A greatly affects the drying function, manual dampers 3A and 3B are provided to balance the extraction air volumes of the centrifugal thin film dryers 1A and 1B. In addition, when there are multiple centrifugal thin film dryers 1A and 1B, and any one of them is in suspension, the pressure loss of the extraction system is smaller than that of the centrifugal thin film dryer in operation. However, the amount of air extracted from the centrifugal thin-film dryer during operation decreases, and the drying capacity decreases. Therefore, automatic dampers 4A and 4B for adjusting the amount of air extracted are installed, and the centrifugal force during suspension is reduced. The amount of air extracted from the thin film dryer can be controlled.
【0017】図2においては遠心薄膜乾燥機1A,1B
の2台に対して自動ダンパ4を1台設置し、2台ごとに
運転制御するようになっている。さらに、遠心薄膜乾燥
機1A,1Bの運転台数により全体の抽気風量が変化す
るため、運転台数に応じて抽気ブロワ7の回転数をイン
バータにより制御できるようになっている。In FIG. 2, centrifugal thin film dryers 1A and 1B are provided.
One automatic damper 4 is installed for each of the two units, and the operation is controlled for each of the two units. Furthermore, since the total amount of extracted air changes depending on the operating number of the centrifugal thin film dryers 1A and 1B, the rotation speed of the extracting blower 7 can be controlled by the inverter according to the operating number.
【0018】図3においては、抽気出口2Aに設けた圧
力計9Aにより抽気圧力を検出し、自動ダンパ4Aの開
度を調節することにより抽気圧力を一定に保つように工
夫されている。In FIG. 3, the bleed pressure is detected by a pressure gauge 9A provided at the bleed outlet 2A, and the bleed pressure is kept constant by adjusting the opening of the automatic damper 4A.
【0019】図4においては、抽換ブロワ7の吸込側に
設けた圧力計9により、抽気圧力を検出し、抽気ブロワ
7の回転数を調節し、抽気圧力を一定に保つように工夫
されている。In FIG. 4, the pressure gauge 9 provided on the suction side of the extraction blower 7 detects the extraction pressure, adjusts the number of revolutions of the extraction blower 7, and keeps the extraction pressure constant. There is.
【0020】図2においては、4台の遠心薄膜乾燥機に
各々手動ダンパが設けてあり、また2台で各々自動ダン
パ4Aが設けてある。また、抽気配管5にはスクラバ6
と抽気ブロワ7が1台ずつ設置されている。さらに、抽
気ブロワ7はインバータ駆動となっており、かつ、抽気
ブロワ7の吐出側に流量調節計11が設置されている。In FIG. 2, four centrifugal thin film dryers are each provided with a manual damper, and two are provided with an automatic damper 4A. A scrubber 6 is installed in the extraction pipe 5.
And one bleed blower 7 is installed. Further, the extraction blower 7 is driven by an inverter, and the flow rate controller 11 is installed on the discharge side of the extraction blower 7.
【0021】遠心薄膜乾燥機1Aによって汚泥10は乾
燥され乾燥汚泥となる。一方乾燥の際発生する蒸発水分
は抽換出口2Aよりスクラバ6へ送られ、冷却除湿され
抽気ブロワ7により脱臭装置などの系外装置へ送られ
る。遠心薄膜乾燥機1Aの抽気出口2Aに設けられた手
動ダンパ3Aにより、4台の遠心薄膜乾燥機の抽気風量
が均等になるようにされている。また、この汚泥乾燥装
置は遠心薄膜乾燥機2台を一括して運転制御するように
しているため、自動ダンパ4Aは遠心薄乾燥機2台に1
台の割合で設置されている。The sludge 10 is dried by the centrifugal thin film dryer 1A to be dried sludge. On the other hand, evaporated water generated during drying is sent from the extraction outlet 2A to the scrubber 6, cooled and dehumidified, and sent to an external device such as a deodorizing device by the extraction blower 7. The manual damper 3A provided at the extraction outlet 2A of the centrifugal thin film dryer 1A makes the extraction air amounts of the four centrifugal thin film dryers uniform. In addition, since this sludge drying device is designed to collectively control the operation of two centrifugal thin film dryers, one automatic damper 4A is provided for every two centrifugal thin dryers.
It is installed at the rate of a stand.
【0022】この自動ダンパ4Aにより、汚泥を供給
し、乾燥工程に入っている遠心薄膜乾燥機と汚泥が供給
されず休止中の遠心薄膜乾燥機または立ち上げ中の遠心
薄膜乾燥機に対する抽気風量のバランスをとることがで
きるようになっている。さらに、抽気ブロワ7の回転数
を遠心薄膜乾燥機1Aの運転台数により制御し、遠心薄
膜乾燥機1台当たりの抽気風量が一定となるようにでき
る。このとき、遠心薄膜乾燥機1台当たりの抽気風量が
設定値となっているかどうかをチェックするため、本実
施例では流量調節計11を設置している。The automatic damper 4A supplies the sludge to the centrifugal thin film dryer which is in the drying step and the centrifugal thin film dryer which is not supplied with the sludge and is in the resting state or the centrifugal thin film dryer which is starting up. It's designed to be balanced. Further, the number of revolutions of the extraction blower 7 can be controlled by the number of operating centrifugal thin film dryers 1A so that the extraction air amount per one centrifugal thin film dryer can be kept constant. At this time, a flow rate controller 11 is installed in this embodiment to check whether or not the amount of extracted air per centrifugal thin film dryer is at a set value.
【0023】本実施例により、従来は遠心薄膜乾燥機1
台ごとに抽気ブロワを設置する必要があったが、4台の
遠心薄膜乾燥機に対して1台の抽気ブロワで済み、省ス
ペース化が図れる効率のよい汚泥乾燥装置とすることが
できる。According to this embodiment, the centrifugal thin film dryer 1 is conventionally used.
Although it was necessary to install an extraction blower for each stand, only one extraction blower is required for four centrifugal thin film dryers, and it is possible to provide an efficient sludge drying device that saves space.
【0024】本実施例では、スクラバおよび抽気ブロワ
により抽気系を構成しているか、スクラバではなく復水
器としてもよく、また、ブロワでなく、真空ポンプやエ
ゼクタを用いてもよい。In this embodiment, an extraction system may be constituted by a scrubber and an extraction blower, or a condenser may be used instead of the scrubber, and a vacuum pump or an ejector may be used instead of the blower.
【0025】[0025]
【発明の効果】本発明により、遠心薄膜乾燥機の抽気系
を簡略化することができ、かつ安定した抽気ができ、効
率的な汚泥乾燥装置とすることができる。According to the present invention, the extraction system of a centrifugal thin film dryer can be simplified and stable extraction can be performed, and an efficient sludge drying device can be provided.
【図1】本発明の一実施例を示す汚泥乾燥装置の構成図
である。FIG. 1 is a configuration diagram of a sludge drying device showing an embodiment of the present invention.
【図2】請求項2の実施例を示す汚泥乾燥装置の構成図
であるFIG. 2 is a configuration diagram of a sludge drying device showing an embodiment of claim 2.
【図3】請求項3の実施例を示す汚泥乾燥装置の構成図
であるFIG. 3 is a configuration diagram of a sludge drying device showing an embodiment of claim 3.
【図4】請求項4の実施例を示す汚泥乾燥装置の構成図
であるFIG. 4 is a configuration diagram of a sludge drying device showing an embodiment of claim 4;
1A,1B1…遠心薄膜乾燥機 3A,3B…手動ダンパ 4A,4B…自動ダンパ 7…換気ブロワ 8…制御装置 9…圧力計 1A, 1B1 ... Centrifugal thin film dryer 3A, 3B ... Manual damper 4A, 4B ... Automatic damper 7 ... Ventilation blower 8 ... Control device 9 ... Pressure gauge
Claims (4)
を熱風乾燥して排出する複数の遠心薄膜乾燥機と、これ
らの遠心薄膜乾燥機の熱風出口側に接続されて前記汚泥
を乾燥した後の処理空気を排気する抽気ブロワと、この
抽気ブロワと前記遠心薄膜乾燥機との間に設置されて前
記処理空気の排出能力を予め設定する手動ダンパと、こ
の手動ダンパに直列に接続されて外部からの開閉制御信
号によって前記遠心薄膜乾燥機の立ち上げ時には半開と
しその後には全開とする自動ダンパと、を具備してなる
汚泥乾燥装置。1. A plurality of centrifugal thin film dryers which are installed in parallel with each other and dry with hot air of discharged sludge and discharge, and after drying the sludge by being connected to hot air outlets of these centrifugal thin film dryers. A blower for exhausting the treated air, a manual damper installed between the extracted blower and the centrifugal thin film dryer to preset the discharge capacity of the treated air, and connected in series to the manual damper to externally A sludge drying device comprising an automatic damper which is half-opened when the centrifugal thin-film dryer is started up and half-opened thereafter by the opening / closing control signal from
と、前記抽気ブロワの後段に抽気ブロワ出口圧力検出器
を設け、この抽気ブロワ出口圧力検出器の検出する抽気
ブロワ出口圧力検出値が予め定めた抽気ブロワ出口圧力
設定値内になるように前記抽気ブロワの回転速度を調整
することを特徴とした汚泥乾燥装置。2. The operation of the bleed air blower is a rotation speed adjustment type, and a bleed air blower outlet pressure detector is provided at a subsequent stage of the bleed air blower, and a bleed air blower outlet pressure detection value detected by the bleed air blower outlet pressure detector is previously set. A sludge drying device, characterized in that the rotation speed of the extraction blower is adjusted so as to be within a set outlet pressure setting value of the extraction blower.
機出口圧力検出器を設け、この乾燥機出口圧力検出器の
検出する乾燥機出口圧力検出値が予め定めた乾燥機出口
圧力設定値内になるように前記自動ダンパの開閉度を調
整することを特徴とした汚泥乾燥装置。3. The dryer outlet pressure detector is provided on the hot air outlet side of the centrifugal thin film dryer, and the dryer outlet pressure detection value detected by the dryer outlet pressure detector is a predetermined dryer outlet pressure set value. A sludge drying device, characterized in that the opening / closing degree of the automatic damper is adjusted so as to be inside.
圧力検出器を設け、この抽気ブロワ入口圧力検出器の検
出する抽気ブロワ入口圧力検出値が予め定めた抽気ブロ
ワ入口圧力設定値内になるように前記抽気ブロワの回転
速度を調整することを特徴とした汚泥乾燥装置。4. A bleed air blower inlet pressure detector is provided in the preceding stage of the bleed air blower so that the bleed air blower inlet pressure detection value detected by the bleed air blower inlet pressure detector is within a predetermined bleed air blower inlet pressure set value. A sludge drying device, characterized in that the rotation speed of the extraction blower is adjusted.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6266798A JPH08126900A (en) | 1994-10-31 | 1994-10-31 | Sludge dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6266798A JPH08126900A (en) | 1994-10-31 | 1994-10-31 | Sludge dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH08126900A true JPH08126900A (en) | 1996-05-21 |
Family
ID=17435837
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6266798A Pending JPH08126900A (en) | 1994-10-31 | 1994-10-31 | Sludge dryer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH08126900A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011088089A (en) * | 2009-10-23 | 2011-05-06 | Toshiba Corp | Sludge treatment apparatus |
-
1994
- 1994-10-31 JP JP6266798A patent/JPH08126900A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011088089A (en) * | 2009-10-23 | 2011-05-06 | Toshiba Corp | Sludge treatment apparatus |
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