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JPS5945414B2 - Granular fertilizer manufacturing equipment - Google Patents
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JPS5945414B2 - Granular fertilizer manufacturing equipment - Google Patents

Granular fertilizer manufacturing equipment

Info

Publication number
JPS5945414B2
JPS5945414B2 JP10598680A JP10598680A JPS5945414B2 JP S5945414 B2 JPS5945414 B2 JP S5945414B2 JP 10598680 A JP10598680 A JP 10598680A JP 10598680 A JP10598680 A JP 10598680A JP S5945414 B2 JPS5945414 B2 JP S5945414B2
Authority
JP
Japan
Prior art keywords
particles
zone
outlet
granulation
granular fertilizer
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
JP10598680A
Other languages
Japanese (ja)
Other versions
JPS5730537A (en
Inventor
喜八 松下
勝之 江川
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.)
Kanadevia Corp
Original Assignee
Hitachi Shipbuilding and Engineering 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 Hitachi Shipbuilding and Engineering Co Ltd filed Critical Hitachi Shipbuilding and Engineering Co Ltd
Priority to JP10598680A priority Critical patent/JPS5945414B2/en
Publication of JPS5730537A publication Critical patent/JPS5730537A/en
Publication of JPS5945414B2 publication Critical patent/JPS5945414B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は回転ドラムを用いた粒状肥料の製造装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for producing granular fertilizer using a rotating drum.

従来の粒状肥料の製造工程は第1図に示す通りである。The conventional manufacturing process of granular fertilizer is as shown in FIG.

造粒機1には後工程の篩分機4で分級された製品規格外
の粒子、即ち小粒および粉砕機で粉砕された粉砕粒なら
びに肥料銘柄によっては製品の一部が循環籾としてパケ
ットエレベータTにより持ち上げられて供給されている
In the granulator 1, non-standard particles classified by the sieve 4 in the subsequent process, such as small particles and crushed granules crushed by the crusher, and depending on the fertilizer brand, a part of the product is transferred to the packet elevator T as circulating paddy. Lifted and supplied.

一方これらの循環籾の造粒バインダーとして水または製
品のスラリー溶液が定量的に供給されている。
On the other hand, water or a slurry solution of the product is quantitatively supplied as a granulation binder for these recycled paddy grains.

肥料造粒用には一般に回転ドラム式又はディスク式造粒
機が使用されており、機内では上記循環籾と水またはス
ラリーが混合されて適切な水分含有率下で造粒されてい
る。
A rotating drum type or disk type granulator is generally used for fertilizer granulation, and inside the machine, the above-mentioned circulating rice and water or slurry are mixed and granulated at an appropriate moisture content.

造粒機1の造粒物は次の乾燥機2に供給される。The granulated material from the granulator 1 is supplied to the next dryer 2.

乾燥機2はほとんどの場合回転ドラム式乾燥機が使用さ
れており、造粒物はここで熱風または乾燥空気により規
定の製品含有率まで乾燥される。
As the dryer 2, a rotating drum dryer is used in most cases, and the granulated material is dried here with hot air or dry air to a specified product content.

乾燥機2の造粒乾燥物はパケットエレベータ3により篩
分機4に供給される。
The granulated dried material from the dryer 2 is supplied to a sieving machine 4 by a packet elevator 3.

粒状肥料製造用の篩分機4はほとんどの場合、電磁また
はモータ式の振動篩が使用されており、造粒物はここで
製品サイズのものが分級され、大粒のものは粉砕機5で
粉砕の後に、小粒のものは直接循環籾としてコンベヤ6
、パケットエレベータ7を通して造粒機1に循環されて
いる。
In most cases, the sieving machine 4 for producing granular fertilizer uses an electromagnetic or motor-type vibrating sieve, and the granules are classified into product sizes here, and large particles are crushed in the crusher 5. Later, small grains are directly transferred to conveyor 6 as circulating paddy.
, and is circulated to the granulator 1 through the packet elevator 7.

なお、8はサイクロンである。Note that 8 is a cyclone.

しかし上記のような製造装置では次のような問題点があ
る。
However, the above manufacturing apparatus has the following problems.

(1)造粒、乾燥および篩分工程が各々の専用機械で行
なわれるため、接続用コンベヤ、パケットコンベヤなど
が必要となり、製造主要工程は複雑になっている。
(1) Since the granulation, drying, and sieving processes are each carried out using dedicated machines, connecting conveyors, packet conveyors, etc. are required, making the main manufacturing process complicated.

(2)これら主要工程の機器は粉体な取扱うため事故が
生じ易く、年間の稼動率はガスや流体を取扱うプラント
に比して相対的に低い。
(2) Accidents are likely to occur because the equipment used in these main processes handles powder, and the annual operating rate is relatively low compared to plants that handle gas and fluids.

(3)造粒機、篩分機などの重量回転機、振動機類は製
造工程上2階または3階に設置される必要があり、この
ため他のプラントに比して相対的に建家は太き(、土建
費用が高価につく。
(3) Heavy rotating machines such as granulators and sieving machines, and vibrating machines need to be installed on the second or third floor due to the manufacturing process, so the building is relatively small compared to other plants. Thick (and construction costs are high).

(4)製造工程上、乾燥物および循環籾を比較的高所に
運搬処理する必要があるため、他のプラントに比して電
力消費量が大きい。
(4) Due to the manufacturing process, it is necessary to transport and process dried products and recycled paddy to a relatively high place, so power consumption is large compared to other plants.

本発明は上記問題点を解決するためのもので、そのため
、本発明の粒状肥料製造装置は、回転ドラム本体内に造
粒域と乾燥域と粒子な粒径に応じて分級するスクリーン
を本体外周部に有する篩分域とを連続して設け、前記篩
分域を覆い、分級された粒子をそれぞれ少な(とも細粉
と製品と粗粉として取り出す出口を有するカバ一体を設
け、粗粒出口に粉砕機を接続し、前記粉砕機で粉砕され
た粒子と細粉出口から取り出された粒子とを前記ドラム
本体の造粒域に循環供給するように構成したもので、こ
れにより、造粒、乾燥は勿論のこと粒子をその径に応じ
て篩い分ける分級をも単一の回転ドラマで行なえ、設備
を簡略化でき、イニシャルコストおよびランニングコス
トを大巾に削減できる。
The present invention is intended to solve the above-mentioned problems, and therefore, the granular fertilizer manufacturing apparatus of the present invention has a granulation zone, a drying zone, and a screen for classifying particles according to the particle size in the rotating drum body around the outside of the body. A cover is provided in series with a sieve zone in the section, and an integrated cover is provided that covers the sieve zone and has an outlet for taking out the classified particles as fine powder, product, and coarse powder. A pulverizer is connected to the drum, and the particles pulverized by the pulverizer and the particles taken out from the fine powder outlet are circulated and supplied to the granulation area of the drum body. Not only that, but also the classification of particles according to their diameter can be performed with a single rotating drum, simplifying the equipment and greatly reducing initial costs and running costs.

以下本発明の一実施例を図面に基づいて説明する。An embodiment of the present invention will be described below based on the drawings.

第2図において、11は回転ドラム式造粒乾燥篩分装置
で、従来の造粒、乾燥および篩分操作の各々分割されて
いる機能を地上に設置された一台の該装置11により全
て行なうものであり、該装置11のドラム本体12の内
部は造粒域13と乾燥域14と篩分域15とに分割され
ている。
In FIG. 2, reference numeral 11 denotes a rotating drum type granulation, drying, and sieving device, and the functions that are conventionally divided into granulation, drying, and sieving operations are all performed by one device 11 installed on the ground. The inside of the drum body 12 of the apparatus 11 is divided into a granulation zone 13, a drying zone 14, and a sieving zone 15.

乾燥域14はさらに例えば3つの第1〜第3乾燥域16
〜18に分割され、各乾燥域16〜18の内周面には軸
心方向にリフター19〜21が設けられ、各リフター1
9〜21は第3図a”eに示すように各領域16〜18
によって異なった形状をしており、造粒域13と乾燥域
14の境界の本体12内周面には埋板状の堰22が設け
られている。
The drying area 14 further includes, for example, three first to third drying areas 16.
-18, and lifters 19-21 are provided in the axial direction on the inner peripheral surface of each drying zone 16-18, and each lifter 1
9 to 21 are each area 16 to 18 as shown in Figure 3 a"e.
A buried plate-shaped weir 22 is provided on the inner peripheral surface of the main body 12 at the boundary between the granulation zone 13 and the drying zone 14.

篩分域15には、第4図に示すように、周方向に適当間
隔で軸心方向に適当長さのスロット23が軸心方向に対
して例えば2段設けられ、各段のスロット23に対応す
る本体12外周には篩分けるべき粒径に応じてあみ目の
目開きがそれぞれ異なるスクリーン24,25が取付板
26により取付けられており、前記スロット23より後
方には掻上板27とグリッド28が設けられている。
As shown in FIG. 4, the sieving area 15 is provided with slots 23 having appropriate lengths in the axial direction at appropriate intervals in the circumferential direction, for example, in two stages in the axial direction. On the outer periphery of the corresponding main body 12, screens 24 and 25 having different mesh openings depending on the particle size to be sieved are attached by mounting plates 26, and behind the slots 23 are a raking plate 27 and a grid. 28 are provided.

29は篩分域150本体外周を覆って設けられたカバ一
体で、前記スクリーン24,25およびグリッド28に
対応する位置にそれぞれ細粉出口30、製品出口31お
よび粗粒出口32が形成され、本体後端に対応する位置
に熱風または乾燥空気人口33が設けられている。
Reference numeral 29 denotes a cover integrally provided to cover the outer periphery of the main body of the sieving area 150, and a fine powder outlet 30, a product outlet 31, and a coarse particle outlet 32 are formed at positions corresponding to the screens 24, 25 and the grid 28, respectively. A hot air or dry air outlet 33 is provided at a position corresponding to the rear end.

34は排ガス出口で、サイクロン35に接続される。34 is an exhaust gas outlet connected to a cyclone 35.

ドラム本体12の造粒域13には後工程の篩分域15で
分級された製品規格外の粒子、即ち小粒および粉砕機3
6で粉砕された粉砕粒ならびに肥料銘柄によっては製品
の一部が循環籾としてパケットエレベータ37により持
ち上げられてシュート38を通して供給されている。
In the granulation zone 13 of the drum body 12, there are particles that are classified in the sieve zone 15 in the subsequent process, that is, small particles, and the crusher 3.
The crushed grains crushed in step 6 and a part of the product depending on the brand of fertilizer are lifted up by a packet elevator 37 and supplied through a chute 38 as circulating paddy.

一方これらの循環籾の造粒バインダーとして水または製
品のスラリー溶液が供給パイプ39を通して定量的に供
給される。
On the other hand, water or a slurry solution of the product is quantitatively supplied through the supply pipe 39 as a granulation binder for the recycled paddy.

造粒域13で造粒に適切な含水率、温度下で造粒された
造粒物は堰22を越えて乾燥域14に移動する。
The granulated material, which is granulated in the granulation zone 13 at a moisture content and temperature suitable for granulation, passes over the weir 22 and moves to the drying zone 14.

移動してきた造粒物はリフター19〜21で掻き上げら
れ、乾燥される。
The moving granules are scraped up by lifters 19 to 21 and dried.

乾燥された造粒乾燥物は本体12内面を転動しながら篩
分域15に入ってきて、初段δスロット23で細粉のみ
がスクリーン24を通過し、細粉出口30から取り出さ
れる。
The dried granulated material enters the sieving area 15 while rolling on the inner surface of the main body 12, and only the fine powder passes through the screen 24 at the first stage δ slot 23 and is taken out from the fine powder outlet 30.

次に次段のスロット23で規格サイズの製品がスクリー
ン25を通過し、製品出口31から取り出される。
Next, the standard size product passes through the screen 25 in the next slot 23 and is taken out from the product outlet 31.

最後にスクリーン24゜25を通過しなかった粗大粒お
よび塊は掻上板27により上部へ掻き上げられ、グリッ
ド28上へ落下され、粗粒出口32かも取り出されて粉
砕機36により粉砕される。
Finally, the coarse grains and lumps that did not pass through the screens 24 and 25 are scraped up by the scraping plate 27 and dropped onto the grid 28, and the coarse grain outlet 32 is also taken out and crushed by the crusher 36.

塊の一部はグリッド28上に落下された時に粉砕され、
粗大粒の粉砕機36に対する負荷を低減させている。
A portion of the mass is crushed when it falls onto the grid 28,
The load on the coarse grain crusher 36 is reduced.

前記細粉出口30かも取り出された小粒と、粉砕機36
で粉砕された粉砕粒と、肥料銘柄によっては製品の一部
が循環籾としてコンベヤ40からパケットエレベータ3
7に送られ、造粒域13に供給される。
The small particles taken out from the fine powder outlet 30 and the crusher 36
Depending on the brand of fertilizer, the crushed granules crushed in
7 and supplied to the granulation zone 13.

以上本発明によれば、次のような利点を有する。As described above, the present invention has the following advantages.

(1)プロセスが簡単になる。(1) The process becomes simpler.

従来の造粒機、乾燥機および篩分機が回転ドラム式の造
粒乾燥篩分装置の1台で済み、簡単になるばかりでなく
、これら機器の連絡に必要なコンベヤ、パケットエレベ
ータなどが削減できるため、プロセスが簡単になり、設
備投資を軽減できるとともに、操作が容易になり、年間
稼動率も向上する。
Conventional granulators, dryers, and sieves can be replaced with a single rotary drum type granulation, drying, and sieving device, which not only simplifies the process, but also reduces the need for conveyors, packet elevators, etc. to connect these devices. This simplifies the process, reduces capital investment, and improves operation and annual operating rates.

(2)建家を縮少できる。(2) The size of the building can be reduced.

従来の製造法によれば、一般に機器名々は建家内の例え
ば造粒機は2階に、乾燥機は地上1階に、篩分機は3階
に設置されていたが、本発明では1台の地上設備で済み
、入口、出口部のみ建家内に、胴体部は屋外設置が可能
となり、建家は低くなるとともに、建物面積を大巾に縮
少できる。
According to conventional manufacturing methods, equipment was generally installed in the building, such as a granulator on the second floor, a dryer on the first floor, and a sieve machine on the third floor, but in the present invention, only one machine is installed. Only the entrance and exit can be installed inside the building, while the body can be installed outdoors.The building can be lowered and the area of the building can be greatly reduced.

さらに従来の造粒機、篩分機のような重量回転機、振動
機が2階、3階に設置されることがないので、土建関係
費用も大巾に軽減できる。
Furthermore, since heavy rotating machines and vibrators such as conventional granulators and sieves are not installed on the second and third floors, construction-related costs can be greatly reduced.

(3)電気消費量を軽減できる。(3) Electricity consumption can be reduced.

従来のように造粒物および循環籾を高所に運搬する必要
がなく、このため電気消費量を軽減でき、省エネルギー
プラントに構成できる。
There is no need to transport the granulated material and circulating paddy to a high place as in the past, so electricity consumption can be reduced and an energy-saving plant can be constructed.

【図面の簡単な説明】 第1図は従来の粒状肥料製造装置の構成図、第2図は本
発明の構成図、第3図a ”’−cは第2図のA−A
、 B−B 、 C−C断面図、第4図は回転ドラムの
一部詳細断面図である。 11・・・・−・回転ドラム式造粒乾燥篩分装置、12
・・・・−・ドラム本体、13・・・・・・造粒域、1
4・・・・・・乾燥域、15・・・・・・篩分域、24
,25・・・・・・スクリーン、26・・・・・・粉砕
機、28・・:・・・グリッド、29・・・・・・カバ
一体、30・・・・・・細粉出口、31・・・・・・製
品出口、32・・・・・・粗粒出口、36・・・・・・
粉砕機、37・・・・−・パケットルベータ、40・・
・・・・コンベヤ。
[BRIEF DESCRIPTION OF THE DRAWINGS] Fig. 1 is a block diagram of a conventional granular fertilizer manufacturing device, Fig. 2 is a block diagram of the present invention, and Fig. 3 a''-c are A-A in Fig. 2.
, BB and CC sectional views, and FIG. 4 is a partially detailed sectional view of the rotating drum. 11... Rotating drum type granulation drying sieving device, 12
......Drum body, 13...Pelletization area, 1
4...Drying area, 15...Sieving area, 24
, 25...Screen, 26...Crusher, 28...Grid, 29...Cover integrated, 30...Fine powder outlet, 31... Product outlet, 32... Coarse particle outlet, 36...
Grinding machine, 37...Packet rubeta, 40...
...conveyor.

Claims (1)

【特許請求の範囲】[Claims] 1 回転ドラム本体内に造粒域と乾燥域と粒子を粒径に
応じて分級するスクリーンを本体外周部に有する篩分域
とを連続して設け、前記篩分域を覆い、分級された粒子
をそれぞれ少なくとも細粉と製品と粗粒として取り出す
出口を有するカバ一体を設け、粗粒出口に粉砕機を接続
し、前記粉砕機で粉砕された粒子と細粉出口から取り出
された粒子とを前記ドラム本体の造粒域に循環供給する
ように構成したことを特徴とする粒状肥料製造装置。
1 A granulation zone, a drying zone, and a sieve zone having a screen on the outer periphery of the main body for classifying particles according to particle size are successively provided in the rotating drum body, and the sieve zone is covered and the classified particles are separated. A cover unit is provided having an outlet for taking out at least fine powder, product, and coarse particles, respectively, and a crusher is connected to the coarse particle outlet, and the particles crushed by the crusher and the particles taken out from the fine powder outlet are A granular fertilizer manufacturing device characterized by being configured to circulate and supply to a granulation area of a drum body.
JP10598680A 1980-07-31 1980-07-31 Granular fertilizer manufacturing equipment Expired JPS5945414B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10598680A JPS5945414B2 (en) 1980-07-31 1980-07-31 Granular fertilizer manufacturing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10598680A JPS5945414B2 (en) 1980-07-31 1980-07-31 Granular fertilizer manufacturing equipment

Publications (2)

Publication Number Publication Date
JPS5730537A JPS5730537A (en) 1982-02-18
JPS5945414B2 true JPS5945414B2 (en) 1984-11-06

Family

ID=14422049

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10598680A Expired JPS5945414B2 (en) 1980-07-31 1980-07-31 Granular fertilizer manufacturing equipment

Country Status (1)

Country Link
JP (1) JPS5945414B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101415177B1 (en) * 2012-01-31 2014-07-04 김미영 Manufacturing device for board materials

Also Published As

Publication number Publication date
JPS5730537A (en) 1982-02-18

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