JP2000042396A - Granulating and drying device - Google Patents

Granulating and drying device

Info

Publication number
JP2000042396A
JP2000042396A JP10217661A JP21766198A JP2000042396A JP 2000042396 A JP2000042396 A JP 2000042396A JP 10217661 A JP10217661 A JP 10217661A JP 21766198 A JP21766198 A JP 21766198A JP 2000042396 A JP2000042396 A JP 2000042396A
Authority
JP
Japan
Prior art keywords
chamber
soil
granulating
drying
granulation
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
JP10217661A
Other languages
Japanese (ja)
Other versions
JP3569131B2 (en
Inventor
Shigeru Sano
滋 佐野
Masatoshi Nishida
正俊 西田
Yoshihide Takemoto
嘉秀 竹本
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.)
Kurimoto Ltd
Shinko Pantec Co Ltd
Original Assignee
Kurimoto Ltd
Shinko Pantec 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 Kurimoto Ltd, Shinko Pantec Co Ltd filed Critical Kurimoto Ltd
Priority to JP21766198A priority Critical patent/JP3569131B2/en
Publication of JP2000042396A publication Critical patent/JP2000042396A/en
Application granted granted Critical
Publication of JP3569131B2 publication Critical patent/JP3569131B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To provide a granulating and drying device capable of supplying dried granular soil whose grain sizes are less than a prescribed size and is uniform. SOLUTION: A partition plate 8 is provided at the boundary between a granulating chamber 2 and a drying chamber 1 in a rotary drum, and a rotary blade 3 is disposed at the lower part of the granulating chamber 2. The kneaded soil charged from a hopper 4 is rolled while crushing the soil by the rotary blade 3, and the roundish granular soil whose grain sizes are less than a prescribed size is allowed to overflow the partition plate 8, is fed to the drying chamber 1, and is dried by indirection heating in a heating tube 17, then the dried granular soil is discharged from an outlet hood 6 provided at an outlet end 5 of the drying chamber 1.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、スラッジ等の造
粒乾燥装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for granulating and drying sludge and the like.

【0002】[0002]

【従来の技術】多量に排出される上水スラッジ等の各種
スラッジは、乾燥されて廃棄処理されるものの他に、造
粒乾燥されて農園芸用土等に再利用されるものがある。
これらの再利用されるスラッジは、まず天日等で乾燥さ
れたのち、混練工程、造粒工程および乾燥工程を経て粒
状の農園芸用土等になる。
2. Description of the Related Art Various types of sludge such as water sludge discharged in large quantities are dried and discarded, and others are granulated and dried and reused for agricultural and horticultural soil.
These sludges to be reused are first dried in the sun or the like, and then subjected to a kneading step, a granulating step, and a drying step to become granular agricultural and horticultural soil.

【0003】上述した農園芸用土等の製造工程では、設
備費用の低減や原料搬送の合理化を目的として、前記造
粒と乾燥の両工程を一体の装置で行う場合があり、この
種の装置としては、実開平6−56693号公報に開示
された造粒乾燥装置がある。この造粒乾燥装置は、図6
に示すように、ホッパ41から投入されるスラッジを供
給するスクリューフィーダ42と、円筒状の回転ドライ
ヤ43と、この回転ドライヤ43の入口端に継足された
造粒筒44と、回転ドライヤ43の出口端に設けられた
乾燥粒状土の取出室45と、スラッジから蒸発した蒸気
を排気する排気室46とで構成されている。
[0003] In the above-mentioned production process of agricultural and horticultural soil, for the purpose of reducing equipment costs and rationalizing the transport of raw materials, there are cases where both the granulation and drying processes are performed by an integrated apparatus. Is a granulation drying apparatus disclosed in Japanese Utility Model Laid-Open No. 6-56693. This granulating and drying apparatus is shown in FIG.
As shown in FIG. 5, a screw feeder 42 for supplying sludge supplied from a hopper 41, a cylindrical rotary dryer 43, a granulating cylinder 44 added to an inlet end of the rotary dryer 43, and a rotary dryer 43. It is provided with a chamber 45 for removing dried granular soil provided at the outlet end, and an exhaust chamber 46 for exhausting steam evaporated from sludge.

【0004】前記造粒筒44には、その内周面に近接し
てスクレーパ47が設けられ、造粒筒44の内周面に付
着するスラッジを掻き落とすようになっている。前記ス
クリューフィーダ42から供給されるスラッジは、造粒
筒44内を転動する間に角がとれて丸みを帯び、粒状土
となって前記回転ドライヤ43に送り込まれる。
The granulating cylinder 44 is provided with a scraper 47 close to the inner peripheral surface of the granulating cylinder 44 so that sludge adhering to the inner peripheral surface of the granulating cylinder 44 is scraped off. The sludge supplied from the screw feeder 42 is rounded and rounded while rolling in the granulating cylinder 44, and is sent to the rotary dryer 43 as granular soil.

【0005】前記回転ドライヤ43の外周部には、加熱
ガス用のジャケット48が設けられ、前記造粒筒44か
ら送り込まれる粒状土が乾燥される。この乾燥された粒
状土は、前記取出室45の下端に設けられた取出口49
から排出される。
[0005] A jacket 48 for heating gas is provided on the outer periphery of the rotary dryer 43, and the granular soil fed from the granulating cylinder 44 is dried. The dried granular soil is supplied to an outlet 49 provided at the lower end of the outlet chamber 45.
Is discharged from

【0006】なお、この装置では、前記取出室45に設
けられた供給口50からガスを供給し、粒状土が乾燥す
る際に発生する蒸気を造粒筒44内へ導き、冷たいスラ
ッジとの接触で結露させることにより、バインダとして
作用させたり、スラッジの水分を調整したりすることが
できるとしている。供給されたガスは前記排気室46の
排出口51から装置外に排出される。
In this apparatus, a gas is supplied from a supply port 50 provided in the take-out chamber 45, and steam generated when the granular soil is dried is guided into the granulating cylinder 44, so as to come into contact with cold sludge. It is stated that the dew condensation can function as a binder or adjust the moisture of the sludge. The supplied gas is discharged out of the device from the discharge port 51 of the exhaust chamber 46.

【0007】[0007]

【発明が解決しようとする課題】上述した従来の造粒乾
燥装置は、造粒筒内での転動のみでスラッジを粒状化し
ているため、粒状土の大きさがまちまちとなり、極端に
大きな粒状土が混じる問題がある。例えば、農園芸用の
乾燥粒状土は、大きくても10mm以下の直径のものが
要求され、この寸法を大幅に越える乾燥粒状土は、出荷
前に除去する必要がある。
In the conventional granulating and drying apparatus described above, the sludge is granulated only by rolling in the granulating cylinder, so that the size of the granular soil varies and extremely large granular There is a problem of soil mixing. For example, dry granular soil for agricultural and horticultural use is required to have a diameter of at most 10 mm or less, and dry granular soil greatly exceeding this size must be removed before shipment.

【0008】そこで、この発明の課題は、所定の寸法以
下で丸みを帯びた乾燥粒状土を供給できる造粒乾燥装置
を提供することである。
Accordingly, an object of the present invention is to provide a granulating and drying apparatus capable of supplying a rounded dry granular soil having a predetermined size or less.

【0009】[0009]

【課題を解決するための手段】上記の課題を解決するた
めに、この発明は、概ね水平に配置され、回転駆動され
る円筒状の乾燥室の原料供給端側に、同じく円筒状の造
粒室が継足され、この造粒室に供給された原料を造粒乾
燥して、前記乾燥室の排出端から排出する造粒乾燥装置
において、前記造粒室に、原料を攪拌する回転羽根を設
け、前記乾燥室と造粒室との境界に環状の仕切板を設け
た構成を採用したのである。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides a cylindrical drying chamber which is disposed substantially horizontally and is rotatably driven at the raw material supply end side. A granulating and drying apparatus for granulating and drying the raw material supplied to the granulating chamber and discharging the raw material from the discharge end of the drying chamber includes rotating blades for stirring the raw material in the granulating chamber. Thus, a configuration was adopted in which an annular partition plate was provided at the boundary between the drying chamber and the granulation chamber.

【0010】すなわち、造粒室と乾燥室との境界に環状
の仕切板を設けて、混練工程から供給される塊状土を造
粒室内に一定時間溜め、造粒室に設けた回転羽根で前記
塊状土を所定の寸法以下の塊に細かく解砕し、これらの
解砕された塊を転動させて角をとり、丸みを帯びた粒状
土を前記仕切板からオーバーフローさせて乾燥室に送り
込むようにしたのである。また、前記回転羽根は、塊状
土を練り込んで柔らかくするため、滑らかな丸みを持っ
た粒状土を形成できる効果も有する。
That is, an annular partition plate is provided at the boundary between the granulation chamber and the drying chamber, and the massive soil supplied from the kneading step is stored in the granulation chamber for a certain period of time. The massive soil is finely crushed into lumps of a predetermined size or less, these crushed masses are rolled to take corners, and the rounded granular soil overflows from the partition plate and is sent to the drying chamber. It was. Further, since the rotating blades knead and soften the massive soil, it has an effect of forming a granular soil having a smooth roundness.

【0011】[0011]

【発明の実施の形態】以下、図1乃至図5に基づき、こ
の発明の実施形態を説明する。図1乃至図3は、造粒乾
燥装置の全体図を示す。図1は正面図、図2は平面図、
図3は側面図である。この造粒乾燥装置は、回転駆動さ
れる円筒状の乾燥室1と、この乾燥室1の入口端に継足
された同じく円筒状の造粒室2と、この造粒室2に設け
られた回転羽根3と、造粒室2に塊状の混練土を供給す
るホッパ4と、前記乾燥室1の出口端5に設けられた乾
燥粒状土を排出する出口フード6とで基本的に構成され
ている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIGS. 1 to 3 show an overall view of a granulating and drying apparatus. 1 is a front view, FIG. 2 is a plan view,
FIG. 3 is a side view. This granulation drying apparatus is provided in a cylindrical drying chamber 1 that is driven to rotate, a cylindrical granulation chamber 2 that is also connected to the inlet end of the drying chamber 1, and a granulation chamber 2. It is basically composed of a rotary blade 3, a hopper 4 for supplying a mass of kneaded soil to the granulation chamber 2, and an outlet hood 6 provided at an outlet end 5 of the drying chamber 1 for discharging dry granular soil. I have.

【0012】前記乾燥室1と造粒室2は両端が開口する
一体の回転胴7で形成され、回転胴7の内周の乾燥室1
と造粒室2の境界には環状の仕切板8が設けられ、回転
胴7の外周にはスプロケット9と2つのタイヤ10が取
り付けられている。回転胴7は、架台11上に軸受12
を介して取り付けられた2対のローラ13で、前記各タ
イヤ10部を支持され、減速機付きモータ14の回転軸
に取り付けられたスプロケット15と前記スプロケット
9に巻き掛けられたチェーン16で回転駆動されるよう
になっている。
The drying chamber 1 and the granulation chamber 2 are formed by an integral rotating cylinder 7 having both ends opened.
An annular partition plate 8 is provided at the boundary between the and the granulation chamber 2, and a sprocket 9 and two tires 10 are attached to the outer periphery of the rotating drum 7. The rotating drum 7 has a bearing 12 on a gantry 11.
The tire 10 is supported by two pairs of rollers 13 which are mounted via a sprocket. The sprocket 15 is mounted on a rotating shaft of a motor 14 equipped with a speed reducer, and the chain 16 is wound around the sprocket 9. It is supposed to be.

【0013】前記乾燥室1には、内周壁に近接して複数
の加熱チューブ17が軸方向に通されている。これらの
加熱チューブ17は、前記出口フード6に取り付けられ
たロータリージョイント18を介して蒸気配管19に接
続され、蒸気配管19から供給される蒸気で乾燥室1を
加熱するものであり、間接加熱方式のため高い熱効率を
確保することができる。なお、蒸気配管19にはドレン
管20も取り付けられている。
A plurality of heating tubes 17 are passed through the drying chamber 1 in the axial direction near the inner peripheral wall. These heating tubes 17 are connected to a steam pipe 19 via a rotary joint 18 attached to the outlet hood 6 and heat the drying chamber 1 with steam supplied from the steam pipe 19. Therefore, high thermal efficiency can be secured. In addition, a drain pipe 20 is also attached to the steam pipe 19.

【0014】前記回転胴7の造粒室2側には入口フード
21が設けられ、回転胴7の両端はこの入口フード21
と前記出口フード6の中に開口している。入口フード2
1には、後述するガス供給口22と掃除用の原料取出口
23も設けられている。
An entrance hood 21 is provided on the side of the granulation chamber 2 of the rotary drum 7, and both ends of the rotary drum 7 are
And the outlet hood 6. Entrance hood 2
1, a gas supply port 22 and a raw material outlet 23 for cleaning are also provided.

【0015】前記回転羽根3は、フランジ24と締付け
ボルトナット25で回転軸26に接続され、他の形態の
回転羽根と交換できるようになっている。回転軸26は
前記入口フード21を通して外部に取り出され、架台1
1上に取り付けられた2つの軸受27に支持されて、カ
ップリング28でモータ29の回転軸に接続されてい
る。
The rotary blade 3 is connected to a rotary shaft 26 by a flange 24 and a tightening bolt / nut 25 so that the rotary blade 3 can be replaced with another type of rotary blade. The rotating shaft 26 is taken out to the outside through the entrance hood 21 and
It is supported by two bearings 27 mounted on the motor 1, and is connected to a rotating shaft of a motor 29 by a coupling 28.

【0016】前記回転羽根3は、図4(a)、(b)に
示すように、回転胴7の下部に配置され、軸方向に一定
間隔で、回転方向と垂直なパドル状の翼体30が4枚ず
つ放射状に設けられている。これらの回転羽根3は、回
転胴7の回転方向と逆方向に回転され、造粒室2の下部
で転動する塊状の混練土31を解砕する。回転羽根3を
回転胴7と逆方向に回転することにより、回転胴7と一
緒に移動してくる混練土31を、その反対方向から効率
よく解砕することができる。
As shown in FIGS. 4 (a) and 4 (b), the rotating blades 3 are arranged at a lower portion of the rotating drum 7, and are arranged at regular intervals in an axial direction at a paddle-shaped wing body 30 perpendicular to the rotating direction. Are provided radially every four sheets. These rotary blades 3 are rotated in a direction opposite to the rotation direction of the rotary drum 7, and crush the massive kneaded soil 31 rolling at the lower part of the granulation chamber 2. By rotating the rotating blades 3 in the direction opposite to the rotating drum 7, the kneaded soil 31 moving together with the rotating drum 7 can be efficiently crushed from the opposite direction.

【0017】前記回転羽根3で解砕され、転動しながら
丸みを帯びた粒状土は、仕切板8からオーバーフローし
て乾燥室1に送り込まれる。このとき、充分に造粒され
ていない混練土31は流動性が悪く、細かな混練土31
は大きな混練土31の下にもぐり込むため、仕切板8を
オーバーフローすることができず、充分に造粒された粒
状土だけがオーバーフローする。このため、造粒室2の
長さが短くても充分な造粒作用が行われる。また、回転
羽根3の回転数を変更することにより、解砕の程度を調
節して、製造される粒状土の大きさを変えることもでき
る。供給される混練土31の物性に応じて回転羽根3の
回転数を変更し、混練土31の物性に左右されることな
く一定の大きさの粒状土を得ることもできる。
The rounded granular soil that has been crushed by the rotating blades 3 and tumbled overflows from the partition plate 8 and is sent into the drying chamber 1. At this time, the kneaded soil 31 that is not sufficiently granulated has poor fluidity, and the fine kneaded soil 31
Since the slab penetrates beneath the large kneaded soil 31, the partition plate 8 cannot overflow, and only sufficiently granulated granular soil overflows. For this reason, even if the length of the granulation chamber 2 is short, a sufficient granulation action is performed. Further, by changing the number of rotations of the rotating blades 3, the degree of crushing can be adjusted to change the size of the granular soil to be produced. By changing the number of rotations of the rotary blades 3 according to the physical properties of the kneaded soil 31 to be supplied, a granular soil of a certain size can be obtained without being affected by the physical properties of the kneaded soil 31.

【0018】前記乾燥室1に送り込まれた粒状土は、乾
燥室1内を転動しながら前記加熱チューブ17で加熱乾
燥され、前記出口端5から出口フード6に送り出され
る。この出口フード6には、前記入口フード21のガス
供給口22から供給されたガスを排出するガス排出口3
2が設けられており、このガスで粒状土から発生する蒸
気を装置外へ排出するようになっている。このように乾
燥された粒状土は、出口フード6の下部に設けられた取
出口33より排出される。
The granular soil fed into the drying chamber 1 is heated and dried by the heating tube 17 while rolling in the drying chamber 1 and sent out from the outlet end 5 to the outlet hood 6. The outlet hood 6 has a gas outlet 3 for discharging gas supplied from a gas supply port 22 of the inlet hood 21.
2 is provided, and the vapor generated from the granular soil by this gas is discharged to the outside of the apparatus. The dried granular soil is discharged from an outlet 33 provided below the outlet hood 6.

【0019】図5(a)、(b)は、別の形態の回転羽
根34を示す。この回転羽根34は、軸方向に一定間隔
で、回転方向と平行なブレード状の翼体35が4枚ずつ
放射状に取り付けられている。この回転羽根34は混練
土をシャーリングするため、硬質の混練土を解砕するの
に適している。
FIGS. 5A and 5B show a rotary blade 34 of another form. The rotating blades 34 are provided with four blade-shaped blades 35 radially parallel to the rotating direction at regular intervals in the axial direction. Since the rotating blades 34 shear the kneaded soil, they are suitable for crushing hard kneaded soil.

【0020】上述した実施形態では、塊状の混練土を解
砕する回転羽根として、パドル状とブレード状のものを
示したが、これらの中間的な機能を有するものとして、
回転方向と傾斜する翼体を有するプロペラ状の回転羽根
を採用することもできる。また、前記放射状に配置され
る翼体の枚数も任意に選定できる。
In the above-described embodiment, paddle-shaped blades and blade-shaped blades are shown as rotary blades for crushing massive kneaded soil.
A propeller-like rotating blade having a wing body inclined with respect to the rotation direction may be employed. Also, the number of wings arranged radially can be arbitrarily selected.

【0021】[0021]

【発明の効果】以上のように、この発明の造粒乾燥装置
は、造粒室と乾燥室との境界に環状の仕切板を設けて、
混練工程から供給される塊状土を造粒室内に一定時間溜
め、造粒室に設けた回転羽根で前記塊状土を所定の寸法
以下の塊に細かく解砕し、これらの解砕された塊を転動
させて角をとり、丸みを帯びた粒状土を仕切板からオー
バーフローさせて乾燥室に送り込むようにしたので、所
定の寸法以下に粒を揃えた乾燥粒状土を供給することが
できる。また、前記回転羽根は、塊状土を練り込んで柔
らかくする作用も有するため、より滑らかな丸みを持っ
た乾燥粒状土を供給することができる。
As described above, the granulating and drying apparatus of the present invention is provided with an annular partition plate at the boundary between the granulating chamber and the drying chamber.
The bulk soil supplied from the kneading step is stored in the granulation chamber for a certain period of time, and the bulk soil is finely crushed into lumps having a predetermined size or less by rotating blades provided in the granulation chamber. Since the rolling granularity is rounded, the rounded granular soil overflows from the partition plate and is sent into the drying chamber, the dried granular soil having grains equal to or smaller than a predetermined size can be supplied. Further, since the rotating blades also have a function of kneading and softening the massive soil, it is possible to supply a dry granular soil having a smoother roundness.

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

【図1】造粒乾燥装置の実施形態を示す一部切欠き正面
FIG. 1 is a partially cutaway front view showing an embodiment of a granulation drying apparatus.

【図2】図1の平面図FIG. 2 is a plan view of FIG. 1;

【図3】図2のIII −III 線に沿った縦断側面図FIG. 3 is a longitudinal sectional side view taken along the line III-III in FIG. 2;

【図4】aは図1の要部拡大断面図、bはaのIV−IV線
に沿った断面図
4A is an enlarged cross-sectional view of a main part of FIG. 1, and FIG. 4B is a cross-sectional view taken along line IV-IV of FIG.

【図5】aは別の態様の回転羽根を示す正面図、bはそ
の縦断側面図
5A is a front view showing a rotating blade of another embodiment, and FIG. 5B is a longitudinal side view thereof.

【図6】従来の造粒乾燥装置を示す縦断面図FIG. 6 is a longitudinal sectional view showing a conventional granulation drying apparatus.

【符号の説明】[Explanation of symbols]

1 乾燥室 2 造粒室 3 回転羽根 4 ホッパ 5 出口端 6 出口フード 7 回転胴 8 仕切板 9 スプロケット 10 タイヤ 11 架台 12 軸受 13 ローラ 14 モータ 15 スプロケット 16 チェーン 17 加熱チューブ 18 ロータリージョイント 19 蒸気配管 20 ドレン管 21 入口フード 22 供給口 23 取出口 24 フランジ 25 ボルトナット 26 回転軸 27 軸受 28 カップリング 29 モータ 30 翼体 31 混練土 32 排出口 33 取出口 34 回転羽根 35 翼体 41 ホッパ 42 スクリューフィーダ 43 回転ドライヤ 44 造粒筒 45 取出室 46 排気室 47 スクレーパ 48 ジャケット 49 取出口 50 供給口 51 排出口 DESCRIPTION OF SYMBOLS 1 Drying room 2 Granulation room 3 Rotating blade 4 Hopper 5 Outlet end 6 Outlet hood 7 Rotating drum 8 Partition plate 9 Sprocket 10 Tire 11 Mount 12 Bearing 13 Roller 14 Motor 15 Sprocket 16 Chain 17 Heating tube 18 Rotary joint 19 Steam pipe 20 Drain pipe 21 Inlet hood 22 Supply port 23 Outlet 24 Flange 25 Bolt nut 26 Rotating shaft 27 Bearing 28 Coupling 29 Motor 30 Blade body 31 Kneaded soil 32 Discharge port 33 Extract port 34 Rotating blade 35 Blade body 41 Hopper 42 Screw feeder 43 Rotary dryer 44 Granulation cylinder 45 Extraction chamber 46 Exhaust chamber 47 Scraper 48 Jacket 49 Outlet 50 Supply port 51 Outlet

───────────────────────────────────────────────────── フロントページの続き (72)発明者 竹本 嘉秀 大阪市西区北堀江1丁目12番19号 株式会 社栗本鐵工所内 Fターム(参考) 3L113 AA06 AB03 AB05 AC05 AC16 AC31 AC40 AC42 AC45 AC46 AC48 AC49 AC57 AC58 AC59 AC63 AC68 AC73 AC76 AC79 BA02 DA24 4G004 HA01 HA02  ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Yoshihide Takemoto 1-12-19 Kitahorie, Nishi-ku, Osaka-shi F-term in Kurimoto Iron Works Co., Ltd. 3L113 AA06 AB03 AB05 AC05 AC16 AC31 AC40 AC42 AC45 AC46 AC48 AC49 AC57 AC58 AC59 AC63 AC68 AC73 AC76 AC79 BA02 DA24 4G004 HA01 HA02

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 概ね水平に配置され、回転駆動される円
筒状の乾燥室の原料供給端側に、同じく円筒状の造粒室
が継足され、この造粒室に供給された原料を造粒乾燥し
て、前記乾燥室の排出端から排出する造粒乾燥装置にお
いて、前記造粒室に、原料を攪拌する回転羽根を設け、
前記乾燥室と造粒室との境界に環状の仕切板を設けたこ
とを特徴とする造粒乾燥装置。
1. A cylindrical granulating chamber is also added to a raw material supply end side of a cylindrical drying chamber which is arranged substantially horizontally and driven to rotate, and a raw material supplied to the granulating chamber is formed. In the granulation drying apparatus for drying granules and discharging from the discharge end of the drying chamber, the granulation chamber is provided with a rotary blade for stirring the raw material,
A granulation and drying apparatus, wherein an annular partition plate is provided at a boundary between the drying chamber and the granulation chamber.
JP21766198A 1998-07-31 1998-07-31 Granulation drying equipment Expired - Lifetime JP3569131B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21766198A JP3569131B2 (en) 1998-07-31 1998-07-31 Granulation drying equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21766198A JP3569131B2 (en) 1998-07-31 1998-07-31 Granulation drying equipment

Publications (2)

Publication Number Publication Date
JP2000042396A true JP2000042396A (en) 2000-02-15
JP3569131B2 JP3569131B2 (en) 2004-09-22

Family

ID=16707748

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21766198A Expired - Lifetime JP3569131B2 (en) 1998-07-31 1998-07-31 Granulation drying equipment

Country Status (1)

Country Link
JP (1) JP3569131B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002361065A (en) * 2001-06-05 2002-12-17 Taiheiyo Kiko Kk Apparatus for treating powder and granular material or the like
JP2014065761A (en) * 2012-09-24 2014-04-17 Jsr Corp Manufacturing method of solid fuel and manufacturing apparatus of solid fuel
CN108059319A (en) * 2017-12-07 2018-05-22 洪作娟 Bio-fertilizer dewatered drying system
CN108112790A (en) * 2018-02-12 2018-06-05 费军 A kind of automation feed processing granulation device
CN109607724A (en) * 2019-02-21 2019-04-12 新疆德安环保科技股份有限公司 A kind of integration flocculation deposition apparatus
CN113758183A (en) * 2021-09-03 2021-12-07 泉州市交发泓盛材料科技有限责任公司 Aggregate drying roller and drying method for dry-mixed mortar production line

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002361065A (en) * 2001-06-05 2002-12-17 Taiheiyo Kiko Kk Apparatus for treating powder and granular material or the like
JP2014065761A (en) * 2012-09-24 2014-04-17 Jsr Corp Manufacturing method of solid fuel and manufacturing apparatus of solid fuel
CN108059319A (en) * 2017-12-07 2018-05-22 洪作娟 Bio-fertilizer dewatered drying system
CN108112790A (en) * 2018-02-12 2018-06-05 费军 A kind of automation feed processing granulation device
CN109607724A (en) * 2019-02-21 2019-04-12 新疆德安环保科技股份有限公司 A kind of integration flocculation deposition apparatus
CN113758183A (en) * 2021-09-03 2021-12-07 泉州市交发泓盛材料科技有限责任公司 Aggregate drying roller and drying method for dry-mixed mortar production line
CN113758183B (en) * 2021-09-03 2022-12-13 泉州市交发泓盛材料科技有限责任公司 Aggregate drying roller and drying method for dry-mixed mortar production line

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