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JPH0746008B2 - Rotating drum cooling device - Google Patents
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JPH0746008B2 - Rotating drum cooling device - Google Patents

Rotating drum cooling device

Info

Publication number
JPH0746008B2
JPH0746008B2 JP60071863A JP7186385A JPH0746008B2 JP H0746008 B2 JPH0746008 B2 JP H0746008B2 JP 60071863 A JP60071863 A JP 60071863A JP 7186385 A JP7186385 A JP 7186385A JP H0746008 B2 JPH0746008 B2 JP H0746008B2
Authority
JP
Japan
Prior art keywords
drum
cooling
heat
cooling device
rotating drum
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
JP60071863A
Other languages
Japanese (ja)
Other versions
JPS61231372A (en
Inventor
章造 林
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.)
Chuetsu Pulp and Paper Co Ltd
Original Assignee
Chuetsu Pulp and Paper 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 Chuetsu Pulp and Paper Co Ltd filed Critical Chuetsu Pulp and Paper Co Ltd
Priority to JP60071863A priority Critical patent/JPH0746008B2/en
Publication of JPS61231372A publication Critical patent/JPS61231372A/en
Publication of JPH0746008B2 publication Critical patent/JPH0746008B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野) 本発明は、加熱高温下に処理された物質を可及的速やか
に冷却する装置に関し、詳しくは回転ドラムを用い、内
容物を掻揚げ撒布する機構と内容物を冷水及び強制空気
により、冷却するための二重ジャケツト機構とを備えた
回転ドラム式冷却装置に関する。
Description: TECHNICAL FIELD The present invention relates to an apparatus for cooling a substance treated under heating and high temperature as quickly as possible, and more specifically, a rotary drum is used to scatter the contents. And a double-jacket mechanism for cooling the contents with cold water and forced air.

(従来技術におけるその問題点) パルプ・製紙工場では製造工程で大量の用水を使用し、
最終工程で排水される水量は製品の数十倍以上にも達す
る。
(Problems with the prior art) Pulp and paper mills use a large amount of water in the manufacturing process,
The amount of water drained in the final process is more than tens of times that of the product.

この排水は環境保全上、クラリファイアー等の沈澱槽に
より浮遊物質を沈降除去し、同時に酸性度を一定範囲内
に調整して後、排出される方式が多く行われている。
From the viewpoint of environmental protection, this waste water is often discharged by suspending and removing suspended solids in a settling tank such as a clarifier and adjusting the acidity within a certain range at the same time.

この場合、沈澱物は更に遠心式濃縮機等により水分を除
去されロータリキルン等の焼却設備により焼却される。
上記焼却設備で焼却された汚泥焼却灰はそのまゝ廃棄さ
れる場合もあるが、焼却灰中に有用な成分が含有される
場合にはこれを更に利用することも又広く行われてい
る。上記の焼却灰中の有用成分利用の場合には、運搬、
使用に便利である様にクラフト紙袋等に袋詰めを行う必
要があるが、例えばロータリキルン出口では焼却灰の温
度は900℃にも達する。自動パツカーでクラフト紙袋に
該焼却灰を袋詰めするためには少くとも60℃以下の温度
まで冷却する必要があるが、短時間に大量の高温焼却灰
を袋詰作業可能な温度にまで低下させるには非常に困難
が伴う。
In this case, the precipitate is further dewatered by a centrifugal concentrator or the like and incinerated by an incinerator such as a rotary kiln.
The sludge incineration ash incinerated by the incinerator may be discarded as it is, but if the incinerator ash contains useful components, it is widely used. In the case of using useful components in the above incinerated ash, transportation,
For convenience of use, kraft paper bags need to be packed, but the temperature of incinerated ash reaches 900 ° C at the rotary kiln outlet, for example. In order to pack the incinerated ash into a kraft paper bag with an automatic packer, it is necessary to cool it to a temperature of at least 60 ° C or less, but it will reduce a large amount of high-temperature incinerated ash to a temperature at which bagging work is possible in a short time. Is very difficult.

従来、上記冷却装置としては、第4図に示すように振動
式コンベアが主として使用されているが、これらは固定
式であり設備の設置床面積も大きく所要動力大で冷却効
率も低い欠点を有する。
Conventionally, as the cooling device, a vibration type conveyor is mainly used as shown in FIG. 4, but these have a drawback that they are fixed type, the installation floor area of the equipment is large, the required power is large, and the cooling efficiency is low. .

又従来において加熱処理物を冷却するため二重壁となっ
ている回転式ドラム装置が使用され、冷却水と冷却空気
を強制的に通気せしめることは公知であった。しかしこ
の従来の装置において、ドラムが回転しても加熱処理物
が常に第5図に示すようにドラムの下部に滞っており、
冷却効果はそれほど大とはならない。
Further, it has been known that a rotary drum device having a double wall is conventionally used to cool a heat-treated product and forcedly ventilates cooling water and cooling air. However, in this conventional apparatus, even if the drum rotates, the heat-treated material always stays in the lower part of the drum as shown in FIG.
The cooling effect is not so great.

(問題点を解決するための手段) 本発明は、加熱処理物を傾斜せる回転ドラムの一側より
導入し、他側より排出せしめ、その間において、上記加
熱処理物を一定温度以下に冷却する回転ドラム式冷却装
置において、該回転ドラム内面の長手方向に複数の掻揚
げ翼を配設してあり、これらの掻揚げ翼の半径方向内方
先端部分が回転ドラムの回転方向に向かって屈曲してお
り、該回転ドラムを構成する円筒部分を二重とし、その
中を冷却水が通過する機構を備え、更に上記加熱処理物
の進行方向の逆方向に冷却空気を強制的に通気させる機
構を有することを特徴とする回転式ドラム冷却装置に関
する。
(Means for Solving Problems) The present invention is a rotation for introducing a heat-treated product from one side of a rotating drum which is inclined and discharging the heat-treated product from the other side, during which the heat-treated product is cooled to a certain temperature or lower. In the drum type cooling device, a plurality of scooping blades are arranged in the longitudinal direction of the inner surface of the rotary drum, and the radially inner tip portions of these scooping blades are bent toward the rotational direction of the rotary drum. In addition, the rotating drum has a double cylindrical portion, and a mechanism is provided for cooling water to pass through the cylindrical portion. Further, there is a mechanism for forcing cooling air to flow in a direction opposite to the traveling direction of the heat-treated product. The present invention relates to a rotary drum cooling device characterized by the above.

図面によって本発明を説明する。The present invention will be described with reference to the drawings.

第1図中、1は入口側を上方へ位置して配設した冷却ド
ラムへ導かれる入口シュートであり、焼却された高温の
スラツジ等は1のシュートを経て二重構造の冷却ドラム
本体2に内筒内に導かれる。外部よりの冷却水は7のロ
ータリジョイントより本体周囲にめぐらされている二重
ジャケツト4より内外筒間に形成された空間3を通り、
ドラム内面を冷却しつつ、ジョイント8より外部に排出
される。ドラム本体2の内面の長手方向に複数の掻揚げ
翼9を配設してあり、これらの掻揚げ翼の半径方向内方
先端部分が回転ドラムの回転方向に向かって屈曲してい
る。そのためドラムの回転に従って該翼は内容物(被冷
却材料)を上部に掻揚げ、更にドラムが回転した場合
は、内容物は翼より外れ、第3図に示すように重力で落
下し、回転ドラム内にて撒布される形となり、空気との
接触を大ならしめる様になる。この場合、翼の半径方向
内方先端部分が回転ドラムの回転方向に向かって屈曲し
ているので、その内容物(被冷却材料)は、ドラムの下
端部を基点としてほぼ60゜〜80゜まで持ち上がり、その
地点から下部に落下するので(図面第3図参照)、非常
に内容物の冷却効果が大となる。もし、掻揚げ翼の先端
が屈曲していないと、図面第6図に示されるように、内
容物はドラムの下端を基点として45゜から少し回転した
ところで、下部に落下し、冷却効果は少なくなる。一方
6のフードよりドラム内部に冷却空気を送りこみドラム
内部にて内容物と接触しつつ5のフードへと導かれ、焼
却アキルン(図示せず)に送り込まれる。ドラム本体2
は焼却物の入口より出口に向って好ましくは約8゜の傾
斜した位置に受ローラ10により支持される。
In FIG. 1, reference numeral 1 denotes an inlet chute which is guided to a cooling drum which is arranged with its inlet side positioned upward, and incinerated high temperature sludge or the like passes through the chute 1 to a cooling drum main body 2 having a double structure. Guided in the inner cylinder. The cooling water from the outside passes through the space 3 formed between the inner and outer cylinders from the double jacket 4 which is swirled around the main body by the rotary joint 7
The inner surface of the drum is cooled and discharged from the joint 8 to the outside. A plurality of scooping blades 9 are arranged in the longitudinal direction of the inner surface of the drum body 2, and the radially inner tip portions of these scooping blades are bent in the rotation direction of the rotary drum. Therefore, according to the rotation of the drum, the blade lifts the contents (material to be cooled) to the upper part, and when the drum further rotates, the contents disengage from the blade and fall by gravity as shown in FIG. It will be sprinkled inside and it will increase the contact with the air. In this case, the radially inner tip of the blade bends in the direction of rotation of the rotating drum, so the content (material to be cooled) is approximately 60 ° to 80 ° with the lower end of the drum as the base point. As it is lifted and falls from that point to the lower part (see Fig. 3 of the drawing), the cooling effect of the contents becomes very large. If the tip of the scooping blade is not bent, as shown in Fig. 6 of the drawings, the contents fall to the lower part when rotated slightly from 45 ° around the lower end of the drum, and the cooling effect is small. Become. On the other hand, cooling air is sent from the hood 6 to the inside of the drum, and while being in contact with the contents inside the drum, the cooling air is guided to the hood 5 and is sent to an incinerator (not shown). Drum body 2
Is supported by the receiving roller 10 at a position inclined from the inlet of the incineration to the outlet, preferably about 8 °.

掻げ翼9の長さはドラムの直径の1/5〜1/20が好まし
い。該翼は回転ドラム本体2の内面に数個、好ましくは
4〜12個、ほぼ等間隔で設置されることが好ましい。そ
の翼はドラム本体に固定されていても良いが、翼の根元
がドラム本体の内容に可能自在に設置されていても良
い。
The length of the scraping blade 9 is preferably 1/5 to 1/20 of the diameter of the drum. It is preferable that several blades, preferably 4 to 12 blades are provided on the inner surface of the rotary drum body 2 at substantially equal intervals. The wings may be fixed to the drum body, or the roots of the wings may be freely installed in the contents of the drum body.

(本発明の効果) 本発明によれば焼却後の高温汚泥スラツジ等は、冷却ド
ラム内面の掻揚げ翼により内面全面に撒布され冷却空気
と接触を大にしつつ、ドラム内を下方へ通過するが、そ
の際壁面に接触した場合には、壁面内の冷水二重ジャケ
ツトにより更に冷却を促進させられる。その後このスラ
ツジ等は搬送コンベアへ落下しライトサイロへ集積され
る。
(Effect of the present invention) According to the present invention, the high temperature sludge sludge and the like after incineration are sprinkled on the entire inner surface by the scooping blades on the inner surface of the cooling drum, and pass through the inside of the drum while making large contact with the cooling air. At that time, if the wall surface comes into contact with the wall surface, cooling can be further promoted by the cold water double jacket in the wall surface. After that, the sludge and the like fall onto the conveyor and are accumulated in the light silo.

本発明は上記の様に冷却装置として水・空気の併用冷却
を行うため極めて冷却効率がよく、従来の固定式振動コ
ンベアに比し本体を小型化し設置面積を1/3〜1/4にする
ことができる。
The present invention has extremely good cooling efficiency because it performs combined cooling of water and air as a cooling device as described above, and downsizes the main body as compared with the conventional fixed vibration conveyor to reduce the installation area to 1/3 to 1/4. be able to.

又振動部分がなく、低速回転であり故障が少く、粉塵、
騒音等の作業上の問題点も解消され、運転に伴う環境悪
化も全くない特徴を有している。
In addition, there are no vibration parts, it rotates at low speed and there are few failures, dust,
It has features that work problems such as noise are solved and the environment is not deteriorated during operation.

更に冷却ドラム本体を回転せしめる動力として可変速モ
ータを設置してあるため焼却物処理量の変化に対応して
本体の回転数を変化せしめ運転条件を調節することがで
きる。
Further, since a variable speed motor is installed as power for rotating the cooling drum main body, it is possible to adjust the operating condition by changing the rotational speed of the main body in response to the change in the incinerated material throughput.

上記本体回転用モータの容量は、従来の振動式のモータ
の1/2以下であり、冷却空気の強制通気も焼却設備の吹
込空気の吸気口と該ドラム冷却装置の排気側フードを連
結することにより、特に送風装置を必要とせずかつ熱交
換が行われるためエネルギーの節約にもなり、極めて有
利である。
The capacity of the main body rotation motor is 1/2 or less of that of the conventional vibration type motor, and the forced ventilation of the cooling air is to connect the intake port of the blown air of the incinerator and the exhaust side hood of the drum cooling device. This is very advantageous because it saves energy because heat is exchanged without requiring a blower.

本発明による回転ドラム式冷却装置は前記製紙工場の排
水処理における汚泥スラツジの焼却後処理として利用で
きる外加熱・焼却等における高温処理物例えば化成肥
料、金属の鋳造後の鋳砂、ごみ焼却灰等の処理に広く使
用することができる。
The rotating drum type cooling device according to the present invention can be used as a post-incineration treatment of sludge sludge in the wastewater treatment of the paper mill. A high-temperature treated material in external heating / incineration such as chemical fertilizer, cast sand after metal casting, dust incinerated ash, etc. It can be widely used for the treatment of

比較実施例 製紙工場の排水処理設備としてクラリファイアの汚泥焼
却灰をクラフト紙袋詰めを行う場合。
Comparative Example A case in which slag incineration ash of clarifier is packed in kraft paper as wastewater treatment equipment at a paper mill.

処理量 粉体50m3/日 内容物温度 冷却装置入口900℃ 出口60℃ Processing amount Powder 50m 3 / day Content temperature Cooling device inlet 900 ℃, outlet 60 ℃

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の回転ドラム式冷却装置の側面図、第2
図は同断面図、第3図は該装置で内容物を冷却する場合
における断面図、第4図は従来の振動コンベア水冷式冷
却装置の側面図、第5図は翼のない装置での冷却の状態
を示す断図面、第6図は先端が屈曲していない翼を有す
るドラムを使用して内容物を冷却する場合における断面
図である。 1……入口シュート、2……ドラム本体、3,4……冷水
ジャケツト、5,6……冷却空気用フード、7,8……冷却水
用ロータリジョイント、9……掻揚げ翼、10……受ロー
ラ。
FIG. 1 is a side view of a rotary drum type cooling device of the present invention, and FIG.
The figure is the same cross-sectional view, FIG. 3 is a cross-sectional view when the contents are cooled by the device, FIG. 4 is a side view of a conventional vibration conveyor water-cooling type cooling device, and FIG. 5 is cooling in a device without blades. FIG. 6 is a cross-sectional view showing the state of FIG. 6 in the case where the contents are cooled using a drum having a wing whose tip is not bent. 1 ... Inlet chute, 2 ... Drum body, 3,4 ... Cold water jacket, 5,6 ... Cooling air hood, 7,8 ... Cooling water rotary joint, 9 ... Scoking blade, 10 ... … Receiving roller.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】加熱処理物を傾斜した回転ドラムの一側よ
り導入し、他側より排出し、その間において上記加熱処
理物を一定温度以下に冷却する回転ドラム式冷却装置に
おいて、 該回転ドラム内面の長手方向に複数の掻揚げ翼を配設し
てあり、これらの掻揚げ翼の半径方向内方先端部分が回
転ドラムの回転方向に向かって屈曲しており、該回転ド
ラムを構成する円筒部分を二重とし、その中を冷却水が
通過する機構を備え、更に上記加熱処理物の進行方向の
逆方向に冷却空気を強制的に通気させる機構を有するこ
とを特徴とする回転式ドラム冷却装置。
1. A rotary drum type cooling device for introducing a heat-treated product from one side of an inclined rotary drum and discharging it from the other side, and cooling the heat-treated substance to a certain temperature or lower during the period, the inner surface of the rotary drum. A plurality of scraping blades are arranged in the longitudinal direction of the rotary blade, and the radially inner tip portions of these scraping blades are bent toward the rotating direction of the rotating drum, and the cylindrical portion that constitutes the rotating drum. And a mechanism for allowing cooling water to pass therethrough, and further having a mechanism for forcibly venting cooling air in a direction opposite to the traveling direction of the heat-treated product. .
JP60071863A 1985-04-04 1985-04-04 Rotating drum cooling device Expired - Lifetime JPH0746008B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60071863A JPH0746008B2 (en) 1985-04-04 1985-04-04 Rotating drum cooling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60071863A JPH0746008B2 (en) 1985-04-04 1985-04-04 Rotating drum cooling device

Publications (2)

Publication Number Publication Date
JPS61231372A JPS61231372A (en) 1986-10-15
JPH0746008B2 true JPH0746008B2 (en) 1995-05-17

Family

ID=13472780

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60071863A Expired - Lifetime JPH0746008B2 (en) 1985-04-04 1985-04-04 Rotating drum cooling device

Country Status (1)

Country Link
JP (1) JPH0746008B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5167100B2 (en) * 2008-12-10 2013-03-21 三菱重工業株式会社 Cooling and conveying device for hot granular fluid
CN102364286A (en) * 2010-11-01 2012-02-29 连云港晶族新材料科技有限公司 Continuous cooling device for high-temperature granules
CN118104854A (en) * 2024-04-03 2024-05-31 云南昆船烟草设备有限公司 Drum-type tobacco shred cooling device and tobacco shred cooling method

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5222700B2 (en) * 1974-04-09 1977-06-18
JPS5298247A (en) * 1976-02-16 1977-08-17 Agency Of Ind Science & Technol Cooling device

Also Published As

Publication number Publication date
JPS61231372A (en) 1986-10-15

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