JPH0565220B2 - - Google Patents
Info
- Publication number
- JPH0565220B2 JPH0565220B2 JP27186588A JP27186588A JPH0565220B2 JP H0565220 B2 JPH0565220 B2 JP H0565220B2 JP 27186588 A JP27186588 A JP 27186588A JP 27186588 A JP27186588 A JP 27186588A JP H0565220 B2 JPH0565220 B2 JP H0565220B2
- Authority
- JP
- Japan
- Prior art keywords
- drum
- pellets
- raw materials
- upper drum
- lower 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 - Fee Related
Links
- 239000008188 pellet Substances 0.000 claims description 36
- 239000002245 particle Substances 0.000 claims description 20
- 239000002994 raw material Substances 0.000 claims description 20
- 238000004519 manufacturing process Methods 0.000 claims description 12
- 239000000654 additive Substances 0.000 claims description 8
- 238000002156 mixing Methods 0.000 claims description 5
- 238000004898 kneading Methods 0.000 claims description 4
- 238000010298 pulverizing process Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 235000013339 cereals Nutrition 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000005453 pelletization Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 1
- 239000002802 bituminous coal Substances 0.000 description 1
- 235000008429 bread Nutrition 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Landscapes
- Glanulating (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
この発明はペレツト製造装置に関し、特に、大
気汚染防止装置ならびに水処理などによつて捕集
されたダスト、汚泥、スラリーなどを取扱いやす
いペレツト化するようなペレツト製造装置に関す
る。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a pellet manufacturing device, and in particular, to pelletizing which makes it easy to handle dust, sludge, slurry, etc. collected by air pollution control devices and water treatment. The present invention relates to a pellet manufacturing apparatus.
[従来の技術]
第3図は従来のペレツトを製造する方法を説明
するための図である。第3図において、原料と添
加剤がバツクミル1に投入され、注水しながら混
合され、回転式ミル2によつて混練され、パン造
粒機3によつてペレツト化される。[Prior Art] FIG. 3 is a diagram for explaining a conventional method for producing pellets. In FIG. 3, raw materials and additives are put into a bag mill 1, mixed while pouring water, kneaded by a rotary mill 2, and pelletized by a bread granulator 3.
ペレツト化の技術としては、第3図に示した例
以外に、原料と添加剤をバツクミルで注水しなが
ら混練し、押出成形機で粒状化する方法がある。 As a pelletizing technique, in addition to the example shown in FIG. 3, there is a method in which raw materials and additives are kneaded in a back mill while pouring water, and then granulated by an extrusion molding machine.
[発明が解決しようとする課題]
しかしながら、上述のいずれの方法において
も、混合、混練時に水分調整剤が注水部で撹拌翼
あるいは器械の内壁に付着し、運転時間とともに
だんだん成長して能率が悪くなるため、適正水分
以下で混合し、パン造粒機で注水しながら造粒す
る方法をとらざるを得ない。このため、粉塵の発
生が多く、注水を誤ると装置内で付着物が多くな
り、遂には運転不能になつてしまう。これらの付
着物を全部排出しなければ正常な運転ができない
ため、普及に長時間を要するという欠点があつ
た。[Problems to be Solved by the Invention] However, in any of the above-mentioned methods, the water conditioner adheres to the stirring blades or the inner wall of the device at the water injection part during mixing and kneading, and gradually grows over time, resulting in poor efficiency. Therefore, it is necessary to mix the ingredients below the appropriate moisture content and granulate them using a pan granulator while pouring water. For this reason, a lot of dust is generated, and if water is poured incorrectly, a lot of deposits will build up inside the device, eventually making it impossible to operate. Normal operation cannot be performed unless all of these deposits are removed, so the drawback is that it takes a long time to become popular.
それゆえに、この発明の主たる目的は、ペレツ
ト化を極めて能率的に行なうことができ、しかも
無人運転が可能なペレツト製造装置を提供するこ
とである。 Therefore, the main object of the present invention is to provide a pellet manufacturing apparatus that can perform pelletization extremely efficiently and can be operated unmanned.
[課題を解決するための手段]
この発明は乾原料、湿原料、添加剤、水分調整
剤などを粉砕、混合、混練してペレツト化するペ
レツト製造装置であつて、その内部に媒体が内蔵
され、乾原料、湿原料、添加剤、水分調整剤など
が投入され、全体に振動が加えられることによつ
て粉砕、混合、混練が行なわれ、凝集粒を生成す
るための上部ドラムと、上部ドラムで生成された
凝集粒を落下させるための落下部と、全体が振動
することによつて落下部から落下した凝集粒同士
を付着転動させてペレツトを生成する下部ドラム
と、上部ドラムと下部ドラム全体を振動させるた
めの加振手段とを備えて構成される。[Means for Solving the Problems] The present invention is a pellet manufacturing device that crushes, mixes, and kneads dry raw materials, wet raw materials, additives, moisture regulators, etc. to form pellets, and has a medium built therein. , dry raw materials, wet raw materials, additives, moisture regulators, etc. are input, and vibration is applied to the whole to crush, mix, and knead. a lower drum that generates pellets by adhering and rolling the agglomerated particles that have fallen from the falling section by vibrating the whole, an upper drum, and a lower drum. It is configured to include a vibrating means for vibrating the entire body.
[作用]
この発明に係るペレツト製造装置は、上部ドラ
ムに原料、添加剤などを投入して上部ドラムを振
動させ、媒体によつて粉砕、混合、混練が行なわ
れて凝集粒が生成され、この凝集粒が下部ドラム
に落下し、下部ドラムの振動に応じて凝集粒同士
が付着転動してペレツトが生成される。[Function] In the pellet manufacturing apparatus according to the present invention, raw materials, additives, etc. are charged into the upper drum, the upper drum is vibrated, and the medium performs pulverization, mixing, and kneading to generate aggregate particles. The aggregated particles fall onto the lower drum, and in response to the vibrations of the lower drum, the aggregated particles adhere to each other and roll to form pellets.
[発明の実施例]
第1図はこの発明の一実施例を示す外観図であ
り、特に、第1図aは正面図であり、第1図bは
側面図である。[Embodiment of the Invention] Fig. 1 is an external view showing an embodiment of the present invention, in particular, Fig. 1a is a front view, and Fig. 1b is a side view.
まず、第1図を参照して、この発明の一実施例
の構成について説明する。ペレツト製造装置は、
主として上部ドラム5と下部ドラム6と加振機9
とから構成された複胴式振動ミルである。上部ド
ラム5には原料を投入するための投入口4が形成
されており、上部ドラム5の内部には媒体として
ロツドが収納されている。上部ドラム5と下部ド
ラム6と加振機9はスプリング7によつて基台8
から浮いていて、振動しやすくなるように構成さ
れている。加振機9は上部ドラム5、下部ドラム
6の左右に設けられたモータによつて発生する円
運動をタイミングベルトにより同期回転させ、上
部ドラム5、下部ドラム6に円振動を起こさせる
ものである。 First, the configuration of an embodiment of the present invention will be described with reference to FIG. The pellet manufacturing equipment is
Mainly the upper drum 5, lower drum 6 and vibrator 9
This is a double-barrel vibratory mill consisting of: An input port 4 for inputting raw materials is formed in the upper drum 5, and a rod is housed inside the upper drum 5 as a medium. The upper drum 5, the lower drum 6, and the vibrator 9 are mounted on a base 8 by a spring 7.
It is structured so that it floats from the ground and vibrates easily. The vibrator 9 causes the upper drum 5 and the lower drum 6 to generate circular vibrations by synchronizing the circular motion generated by motors provided on the left and right sides of the upper drum 5 and the lower drum 6 with a timing belt. .
今、乾原料、湿原料添加剤、水分調整剤などを
適正配合割合に従つて投入口4から上部ドラム5
に投入すると、加振機9から発生する円振動によ
り、上部ドラム5内の原料と媒体はシエイカーを
振るような激しい躍動をしながら、上部ドラム5
内を回転する現象を起こす。それによつて、原料
と媒体、原料とドラム壁、媒体とドラム壁、媒体
と媒体などの間で衝撃、剪断、摩擦などが生じ、
極めて短時間で混合、混練され、粒子内の余分の
水分は粒子表面に出て凝集力として作用し粒の成
長が起こる。このようにして、上部ドラム5内に
て凝集粒が生成され、生成された凝集粒は落下部
10を介して下部ドラム6に落下する。 Now, add the dry raw materials, wet raw material additives, moisture regulator, etc. according to the proper mixing ratio from the input port 4 to the upper drum 5.
When the material and medium in the upper drum 5 are thrown into the shaker, due to the circular vibration generated by the vibrator 9, the raw materials and the medium in the upper drum 5 move violently as if shaking a shaker.
Causes the phenomenon of internal rotation. As a result, impact, shear, friction, etc. occur between the raw material and the medium, the raw material and the drum wall, the medium and the drum wall, the medium and the medium, etc.
They are mixed and kneaded in an extremely short period of time, and excess water within the particles comes out to the surface of the particles and acts as a cohesive force, causing grain growth. In this way, aggregated particles are generated within the upper drum 5, and the generated aggregated particles fall into the lower drum 6 via the falling section 10.
下部ドラム6内には媒体が収納されていないた
め、下部ドラム6の円振動により水分を加えなく
ても振動回転力により凝集粒表面に水分が浮かび
出し、凝集粒同士が付着転動して成長する。但
し、凝集粒子表面の水分が少ないと小粒となり、
多いと大粒になるので、粒度を一定範囲内に揃え
るためには、排出粒を赤外線水分計で瞬時測定
し、標準水とのずれに従つて水分調整剤を調整す
れば、常に一定範囲の粒を製造することができ
る。このようにして、下部ドラム6内で生成され
たペレツトは排出口11から外部に排出される。 Since no medium is stored in the lower drum 6, the circular vibration of the lower drum 6 causes water to float on the surface of the agglomerated grains due to the rotational force of the vibration, causing the agglomerated grains to stick to each other and roll and grow. do. However, if there is little moisture on the surface of the aggregated particles, the particles will become small.
If there is too much, the particles will become large, so in order to keep the particle size within a certain range, measure the discharged particles instantaneously with an infrared moisture meter and adjust the moisture conditioner according to the deviation from the standard water. can be manufactured. In this way, the pellets produced within the lower drum 6 are discharged to the outside through the discharge port 11.
第2図はこの発明の他の実施例を示す図であつ
て、特に第2図aは正面図を示し、第2図bは側
面図を示す。この第2図に示した例は、上部ドラ
ム13と下部ドラム14の間に加振機17を設
け、モータ18の駆動力によつて加振機17が上
部ドラム13と下部ドラム14とを円振動させる
ものである。そして、この実施例においても、ス
プリング15によつて上部ドラム13と下部ドラ
ム14と加振機17が基台16から浮かされてお
り、上部ドラム13には投入口12が設けられ、
上部ドラム13で生成された凝集粒は落下部19
を介して下部ドラム14に落下し、下部ドラム1
4内で生成されたペレツトは排出口20から外部
に排出される。 FIG. 2 is a diagram showing another embodiment of the present invention, in particular, FIG. 2a shows a front view, and FIG. 2b shows a side view. In the example shown in FIG. 2, a vibrator 17 is provided between the upper drum 13 and the lower drum 14, and the vibrator 17 moves the upper drum 13 and the lower drum 14 in a circular motion by the driving force of a motor 18. It vibrates. Also in this embodiment, the upper drum 13, the lower drum 14, and the vibrator 17 are suspended from the base 16 by the spring 15, and the upper drum 13 is provided with the input port 12.
The aggregated particles generated in the upper drum 13 are transferred to the falling part 19.
and falls to the lower drum 14 through the lower drum 1.
The pellets produced within the chamber 4 are discharged to the outside from the discharge port 20.
次に、第1図に示した実施例において、実際の
ペレツトの製造例について説明する。各ホツパよ
り、定量供給器により電気炉集塵ダスト100Kg/
H、泥状瀝青炭20Kg/H、パルプ排液タンクより
定量供給ポンプによりパルプ排液15/Hを投入
口4から15の容量を有する上部ドラム5に投入
し、加振機9による円振動により混練し、その混
練物を容量25の下部ドラム6で加振機9の円振
動を利用してペレツトを造粒した。製造されたペ
レツトは水分が9.8%であり、4m/mφ〜8
m/mφのサイズのものが90%で圧縮強度は1.5
Kg/生ペレツト6m/mφのものが得られ、乾燥
強度14Kg/乾ペレツトで精練用として再利用でき
る良好なものを得ることができた。 Next, in the embodiment shown in FIG. 1, an example of actual pellet production will be explained. From each hopper, 100 kg of electric furnace dust is collected using a quantitative feeder.
H, muddy bituminous coal 20Kg/H, pulp waste liquid 15/H from the pulp waste liquid tank is charged from the input port 4 to the upper drum 5 having a capacity of 15, and kneaded by circular vibration by the vibrator 9. Then, the kneaded product was granulated into pellets using the circular vibration of the vibrator 9 in the lower drum 6 having a capacity of 25 mm. The produced pellets have a moisture content of 9.8% and a diameter of 4 m/mφ to 8
90% of the size is m/mφ, and the compressive strength is 1.5
Kg/green pellets of 6 m/mφ were obtained, and the dry pellets had a dry strength of 14 kg/dry pellets and were good enough to be reused for scouring.
次に、第2図に示した実施例における実際のペ
レツトの製造例について説明する。各ホツパより
定量供給機で都市焼却灰300Kg/H、セメント30
Kg/H、水タンクより定量供給ポンプにより水50
/Hを第2図に示した容量25の上部ドラム1
3に投入し、加振機17の円振動により混練し、
その混練物を容量50の下部ドラム14で加振機
17による円振動を利用してペレツト化した。製
造されたペレツトは水分16%で2m/mφ〜6
m/mφのサイズのものが90%で、その圧縮強度
は1Kg/生ペレツト6m/mφのものが得られ、
空気中に一日放置したとき2Kg/ペレツト6m/
mφ、1週間放置で11Kg/ペレツト6m/mφに
なり、砂利と同程度の強さのものを得ることがで
きた。 Next, an example of actual production of pellets in the embodiment shown in FIG. 2 will be explained. Municipal incineration ash 300Kg/H, cement 30Kg/h from each hopper with quantitative feeder
Kg/H, water 50 by metered supply pump from water tank
/H shown in Figure 2. Upper drum 1 with a capacity of 25
3 and kneaded by circular vibration of the vibrator 17,
The kneaded product was pelletized in a lower drum 14 with a capacity of 50 using circular vibration from a vibrator 17. The produced pellets have a moisture content of 16% and a diameter of 2m/mφ~6
90% of the pellets have a size of m/mφ, and the compressive strength is 1Kg/raw pellets of 6m/mφ.
2Kg/6m of pellets when left in the air for a day
After leaving it for one week, the pellet weight became 11 kg/pellet 6 m/mφ, and the strength was comparable to that of gravel.
なお、上述の第1図および第2図に示した実施
例では、下部ドラム6,14を単胴のもので構成
したが、これに限ることなく下部ドラム6,14
をそれぞれ2個平行に設け、復胴構成にして容量
を増すようにしてもよい。 In the embodiments shown in FIGS. 1 and 2, the lower drums 6 and 14 are constructed with a single barrel, but the lower drums 6 and 14 are not limited to this.
It is also possible to increase the capacity by providing two of each in parallel and forming a rectangular configuration.
[発明の効果]
以上のように、この発明によれば、加振機によ
る円振動を利用し、上部ドラムで凝集粒を生成
し、それを下部ドラムで再び円振動を加えてペレ
ツトを製造するようにしたので、性状の極端に異
なる原料(高水分、低水分、泥状、乾粉)を配合
処理する場合でも混合の均質化を図ることができ
る。凝集塊状化した原料が混入している場合でも
微細均一化できる。混練物の水分偏差は極度に低
下し、極めて均一化した水分分布を有するペレツ
トを製造することができる。しかも、処理原料の
粉砕粒子を密充填化し、嵩比重を上げると同時に
粒子表面に均一な水膜を形成することができ、他
のペレツト製造方法に比べて低水分で高強度のペ
レツトを得ることができる。さらに、操業管理は
点検のみでよく、長時間の連続運転が可能とな
り、また停止時の残留物は原料を投入しないでそ
のまま運転すれば残留物を全部排出でき、特に洗
浄する人員を必要としない。さらに、ドラム全体
で混練作用が起こるので、回転ミルのような死ん
だ空間がなく、回転ミルの20倍ないし50倍の能力
があり、今まで不可能であつた超大容量のペレツ
ト生産が可能となる。[Effects of the Invention] As described above, according to the present invention, agglomerated grains are generated in the upper drum using circular vibration by a vibrator, and then circular vibration is applied again to the aggregated particles in the lower drum to produce pellets. This makes it possible to achieve homogeneous mixing even when raw materials with extremely different properties (high moisture, low moisture, muddy, dry powder) are blended. Even if agglomerated raw materials are mixed in, it can be made fine and uniform. The moisture deviation of the kneaded product is extremely reduced, and pellets with extremely uniform moisture distribution can be produced. In addition, it is possible to densely pack the crushed particles of the raw material to be processed and increase the bulk specific gravity, while at the same time forming a uniform water film on the particle surface, making it possible to obtain high-strength pellets with low moisture content compared to other pellet manufacturing methods. I can do it. In addition, operation management requires only inspections, allowing continuous operation for long periods of time, and any residue remaining when stopped can be removed by continuing to operate without adding raw materials, eliminating the need for special cleaning personnel. . Furthermore, since the kneading action occurs throughout the drum, there is no dead space like in rotary mills, and the capacity is 20 to 50 times that of rotary mills, making it possible to produce ultra-large volumes of pellets that were previously impossible. Become.
第1図はこの発明の一実施例の外観図である。
第2図はこの発明の他の実施例の外観図である。
第3図は従来のペレツト製造方法を説明するため
の図である。
図において、4,12は投入口、5,13は上
部ドラム、6,14は下部ドラム、7,15はス
プリング、8,16は基台、9,17は加振機、
10,19は落下部、11,20は排出口を示
す。
FIG. 1 is an external view of one embodiment of the present invention.
FIG. 2 is an external view of another embodiment of the invention.
FIG. 3 is a diagram for explaining a conventional pellet manufacturing method. In the figure, 4 and 12 are input ports, 5 and 13 are upper drums, 6 and 14 are lower drums, 7 and 15 are springs, 8 and 16 are bases, 9 and 17 are vibration exciters,
10 and 19 are falling parts, and 11 and 20 are discharge ports.
Claims (1)
粉砕、混合、混練してペレツト化するペレツト製
造装置であつて、 その内部に媒体が内蔵され、前記乾原料、湿原
料、添加剤、水分調整剤などが投入され、全体に
振動が加えられることによつて粉砕、混合、混練
が行なわれ、凝集粒を生成するための上部ドラ
ム、 前記上部ドラムで生成された凝集粒を落下させ
るための落下部、 全体が振動することによつて、前記落下部から
落下した凝集粒同士を付着転動させてペレツトを
生成する下部ドラム、および 前記上部ドラムと前記下部ドラム全体を振動さ
せるための加振手段を備えた、ペレツト製造装
置。[Scope of Claims] 1. A pellet manufacturing device that crushes, mixes, and kneads dry raw materials, wet raw materials, additives, moisture regulators, etc. to form pellets; Wet raw materials, additives, moisture regulators, etc. are input, and vibration is applied to the whole to perform pulverization, mixing, and kneading, and an upper drum for producing aggregated particles. A falling part for dropping the aggregated particles; a lower drum that vibrates as a whole to cause the aggregated particles that have fallen from the falling part to stick to each other and roll to form pellets; and the upper drum and the lower drum as a whole. A pellet manufacturing device equipped with a vibration means for vibrating pellets.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27186588A JPH02119927A (en) | 1988-10-27 | 1988-10-27 | Device for producing pellet |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27186588A JPH02119927A (en) | 1988-10-27 | 1988-10-27 | Device for producing pellet |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02119927A JPH02119927A (en) | 1990-05-08 |
JPH0565220B2 true JPH0565220B2 (en) | 1993-09-17 |
Family
ID=17505975
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27186588A Granted JPH02119927A (en) | 1988-10-27 | 1988-10-27 | Device for producing pellet |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02119927A (en) |
-
1988
- 1988-10-27 JP JP27186588A patent/JPH02119927A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPH02119927A (en) | 1990-05-08 |
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