JPS614553A - Apparatus for dehydrating wet powder and wet granule having abrasive property - Google Patents

Apparatus for dehydrating wet powder and wet granule having abrasive property

Info

Publication number
JPS614553A
JPS614553A JP12432984A JP12432984A JPS614553A JP S614553 A JPS614553 A JP S614553A JP 12432984 A JP12432984 A JP 12432984A JP 12432984 A JP12432984 A JP 12432984A JP S614553 A JPS614553 A JP S614553A
Authority
JP
Japan
Prior art keywords
suction
fan
water
casing
wet
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
JP12432984A
Other languages
Japanese (ja)
Other versions
JPH0536082B2 (en
Inventor
Shujiro Takada
高田 修二郎
Tsukasa Oshita
大下 司
Kazuaki Fujii
藤井 和秋
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.)
NAKAYAMA SEIKOSHO KK
Nakayama Steel Works Ltd
Original Assignee
NAKAYAMA SEIKOSHO KK
Nakayama Steel Works 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 NAKAYAMA SEIKOSHO KK, Nakayama Steel Works Ltd filed Critical NAKAYAMA SEIKOSHO KK
Priority to JP12432984A priority Critical patent/JPS614553A/en
Publication of JPS614553A publication Critical patent/JPS614553A/en
Publication of JPH0536082B2 publication Critical patent/JPH0536082B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To reduce the cost by providing a fan in the middle of a system wherein dehydration is carried out by the synergetic effect of the sucking force of a suction rotor and the sucking force of the fan in the titled apparatus for dehydrating wet granules having an abrasive property. CONSTITUTION:Wet powder and wet granules to be dehydrated are successively charged from a chute 1b, and discharged into a suction rotor 2 by the operation of a fan 1a along with an air current through a gas supply pipe 1. The material is blown against the revolving blade 2a of a suction fan, the water is aspirated by a casing 4 from a slit 2b along with the air current, and the material is dehydrated. The material with reduced water content is slid along the front surface by the revolution of the fan blade, and dropped into a material recovery chute 3a. The water and the air current in the casing are separated by the difference in weight, and the water is dropped into a water recovery chute 4b. The air contg. mist is sucked into a main suction duct 5, and the mist is separated by a separator 6. The air freed of the mist is sent into the suction port of the fan.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は摩耗性を有する湿粉体および湿粉体等、高水分
原料の含水分を低減させる機械的脱水装置に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a mechanical dewatering device for reducing the moisture content of high-moisture raw materials, such as abrasive wet powders and wet powders.

従来の技術 湿粉体および湿粉体の含水分を低減し、低水分の粉1粒
体を得る機械的処理(以下脱水操作と略称する)の際、
■摩耗、破孔のための長時間連続運転の不能、Q高エネ
ルギー原皐位による非経済性、■一部微細粉体の飛散に
よる環境悪化、鼻の欠点があった。
Conventional technology During wet powder and mechanical treatment (hereinafter abbreviated as dehydration operation) to reduce the moisture content of the wet powder and obtain a single grain of low moisture powder,
■Unable to operate continuously for long periods of time due to wear and holes; Uneconomical due to high-energy raw material; ■Environmental deterioration due to scattering of some fine powder; disadvantages of the nose.

その−例として1例えば水砕スラグ類は製鉄所の尚炉に
於て溶融金属種錬滓(溶融スラグ)を高圧水により急冷
し、ガラス質若しくは結晶質の固形粉体、並びに粒体(
いわゆる水砕スラグ)を製造し、セメント原料、その他
に供してめるが、此の水砕スラグはその製造過程により
多孔質で摩耗性が極めて高く、又多孔質であることと高
圧水を噴射して製造されるため、その含有水分は70〜
75%と高くて、各顧客にて原料として使用する場合、
そのハンドリングやエネルギーコストの点で支障となっ
ている。
For example, granulated slag is produced by quenching molten metal seed slag (molten slag) with high-pressure water in a furnace at a steelworks, and producing glassy or crystalline solid powders and granules (
Granulated slag (so-called granulated slag) is manufactured and used as raw material for cement and other uses.Due to the manufacturing process, this granulated slag is porous and extremely abrasive. Since the water content is 70~
If it is as high as 75% and used as raw material by each customer,
This poses problems in terms of handling and energy costs.

従って此の水分を除去するために熱風炉、加熱炉、均熱
炉等の高温廃熱を利用して乾燥している例が多い。
Therefore, in order to remove this moisture, high-temperature waste heat from hot air ovens, heating furnaces, soaking ovens, etc. is often used for drying.

然し、この方法では設備費が嵩み、広大な敷地を要する
と共に、エネルギーコストやハント11ング費用が巨額
となる欠点がある。
However, this method has the drawbacks of high equipment costs, requiring a vast site, and high energy costs and hunting costs.

発明が解決しようとする問題点 本発明は上記の欠点の解消と水砕スラグの性質に適合し
たものとしての機械的脱水装j4を提供せんとするもの
である。
Problems to be Solved by the Invention The present invention aims to eliminate the above-mentioned drawbacks and to provide a mechanical dewatering device j4 that is compatible with the properties of granulated slag.

問題点を解決するための手段 本発明を図面に基づ論て説明する。Means to solve problems The present invention will be explained based on the drawings.

本発明装置は第1図に示す構成からなるもので、(1)
は湿粉体および湿粉体等の高水分原料を脱水装置内に供
給する気流供給管、(1a)は気流を送るだめのファン
、(lb)は高水分原料を気流供給管(1)へ投入する
シュートで、気流供給管(1)に連結されている。(2
)は気流供給管(1)の放出口と対向する位置に設けら
れた吸引ローターで、その周囲には放射方向に特殊なス
リット(2b)を有し、かつ気流供給管側に向って凹形
の円錐面に構成された直接脱水操作を担当する吸引ファ
ンプレート(2a)が設けられている。この吸引ファン
プレート(2a)は等分した複数枚の分割板で構成され
ている。
The device of the present invention has the configuration shown in FIG. 1, (1)
is an air flow supply pipe that supplies high moisture raw materials such as wet powder and wet powder into the dehydrator, (1a) is a fan that sends air flow, and (lb) is an air flow supply pipe that supplies high moisture raw materials to (1). The chute is connected to the airflow supply pipe (1). (2
) is a suction rotor installed at a position facing the outlet of the airflow supply pipe (1), and has special slits (2b) in the radial direction around it, and is concave toward the airflow supply pipe side. A suction fan plate (2a) configured on a conical surface and responsible for direct dewatering operation is provided. This suction fan plate (2a) is composed of a plurality of equally divided plates.

(2C)は吸引脱水操作中に上記吸引ファンブレート(
2a)が摩耗してローター全体がアンバランスになり、
振動を発生し出した際、短時間に容易に調整可能なバラ
ンサーで、ローター軸に取付けられている。(2e)は
吸引ローター(2)を支える防振ゴム付軸受。(2d)
は吸引ローター(2)の回転駆動装置である。
(2C) The above suction fan blade (
2a) is worn out and the entire rotor becomes unbalanced,
This is a balancer that can be easily adjusted in a short time when vibrations start to occur, and is attached to the rotor shaft. (2e) is a bearing with anti-vibration rubber that supports the suction rotor (2). (2d)
is a rotational drive device for the suction rotor (2).

(3)は気流供給管(1)を中心に前記吸引ローター(
2)及び吸引ファンプレート(2a)の前面を包むケー
ジ   叶y、7−(3a3.iいゆ3.アア、え。オ
ウや、6  グ工程へ送る原料回収シュートである。
(3) The suction rotor (
2) and the cage surrounding the front surface of the suction fan plate (2a) 7-(3a3.iiii3.aa,e.oh, 6) This is a raw material recovery chute for sending to the g process.

(4)は吸引ローター+21及び吸引ファンプレート(
2a)の後面を包み吸引された排気を確保するケーシン
グ、 (4a)は吸引ローター(2)Kより吸引された
空気の飛散を防止する排気ケーシング、 (4b)は排
気と共に吸引された水分を分離して次工程へ送るダンバ
ー (7)甘木回収シュニドである。
(4) is the suction rotor +21 and the suction fan plate (
2a) A casing that wraps around the rear surface and secures the suctioned exhaust air, (4a) is an exhaust casing that prevents the air sucked from the suction rotor (2) K from scattering, and (4b) separates the moisture sucked in with the exhaust air. (7) Amagi recovered schnide.

(5)は吸引ファンにて吸引された排気を気流供給管(
気流供給器)(1)に再使用するため、排気ケーシング
(4a)とファン(1a)とを接続した主吸引ダクトで
、その主吸引ダクト(5)の中途には再使用される吸引
ファン排気中にミスト状、あるいは微粉状で混在する微
11…水滴並びに微細粉末を除去する分1’flffl
 aW (61と、ファン(1a)の手前において吸引
ファン能力と気流供給能力がアンバランスになった時D
I整するダンバー L81付削吸引孔(5a)が設けら
れている。
(5) is the airflow supply pipe (
A main suction duct connecting an exhaust casing (4a) and a fan (1a) for reuse in the air flow supply device (1), and a suction fan exhaust that is reused in the middle of the main suction duct (5). Fine 11 mixed in the form of mist or fine powder... 1'flffl to remove water droplets and fine powder
aW (61 and D when the suction fan capacity and airflow supply capacity become unbalanced in front of the fan (1a))
A suction hole (5a) is provided for adjusting the damper L81.

この様に構成した本発明装置斤では、湿粉体および湿粉
体、ia水分原料をシュート(lb)より順次投入する
と、該高水分原料はファン(1a)の駆動により気流供
給’!!f ti)内を通り空気流と共に吸引ローター
12)に向って放出され、ここにおいてすでに回転駆動
装置(2d)により回転している吸引ファンプレート(
2a)のスリット(21))を通じて空気流が開側の排
気ケーシング(4]に吸引されるので、原料は吸引ファ
ンプレート(2a)に吸付けられ、その水分は空気流と
共に吸引ファンプレート(2a)の裏側のケーシング(
4)に吸込され原料の水分が吸引脱水されると共に、こ
の水分を除去された低水分の原料は吸引ファンプレート
(2)の回転力により前面を滑り原料回収シュート(3
a)に落下し回収される。一方吸引フアンブレード(2
a)を通過した水分及び空気流はケーシング(4)内に
て厘量差により水と空気に分離され、水は五邪の水回収
シュート(4b)に落下し回収される。此の際水回収シ
ュート (4b)内にあるターンパー(7)にて開度を
加減しケーシング(4)内を最も水分の分離に適した圧
力に調整することにより、水と分離された圧気流は排気
ケーシング(4a)から主吸引ダクト(5)により分離
器(61を経て、こ\で排気中に混在する微細な木簡、
微粉末を除去し。
In the apparatus of the present invention constructed in this way, when wet powder, wet powder, and ia moisture raw material are sequentially introduced from the chute (lb), the high moisture raw material is supplied with an airflow by driving the fan (1a)! ! The suction fan plate (f ti) is discharged together with the air flow towards the suction rotor 12), where it is already rotated by the rotary drive (2d).
As the air flow is sucked into the open side exhaust casing (4) through the slit (21)) of 2a), the raw material is attracted to the suction fan plate (2a), and its moisture is sucked into the suction fan plate (2a) along with the air flow. ) on the back side of the casing (
4), the moisture in the raw material is suctioned and dehydrated, and the low-moisture raw material from which this moisture has been removed slides down the front surface by the rotational force of the suction fan plate (2) and passes through the raw material collection chute (3).
a) and is collected. On the other hand, the suction fan blade (2
The water and air flow that has passed through a) is separated into water and air in the casing (4) due to the difference in volume, and the water falls into the water recovery chute (4b) of the goya and is collected. At this time, the pressure air separated from the water is exhausted by adjusting the opening degree with the turner (7) in the water recovery chute (4b) and adjusting the pressure inside the casing (4) to the most suitable for separating water. From the casing (4a), the main suction duct (5) passes through the separator (61), where the fine wood chips mixed in the exhaust air are removed.
Remove fine powder.

再びファン(1a)の吸込み口に送り込まれ、ファン(
1a)による気流供給の空気量と再使用する空気量とに
アンバランスを生ずる時はダンパー(8)による副吸引
化支% (5a)の一度調整により大気を吸い込んで(
Iff +’A便用でさるようにしたものである。
It is fed into the suction port of the fan (1a) again, and the fan (
If there is an imbalance between the amount of air supplied by 1a) and the amount of air to be reused, the damper (8) can be used to suck in atmospheric air by adjusting the sub-suction rate (5a) once (5a).
It is designed to be used for If +'A flight.

実施例 第2図は本発明装置を水砕スラグ脱水処理場に設置した
実施例を示したもので、その機能を説明する。
Embodiment FIG. 2 shows an embodiment in which the apparatus of the present invention is installed in a granulated slag dewatering treatment plant, and its functions will be explained.

0℃は水砕スラグを貯溜する切出部ホッパー、(2)は
その切出口下に設置された大塊状のスラグを分離できる
形式のフィーダー、(社)は本装置の原料投入シュート
(lb)に連絡するよう設けられた可変速供給コンベヤ
ーで、高水分水砕スラグは切出量を調整テきるゲートを
備えた切出部ホッパーODにクレーンcfで投入され、
フィーダー−により切り出されて可変速供給コンベヤー
03に乗せられ5本脱水装置戊系の投入シュート(lb
)を経て気流供給g(1)内に順欠投入される。
0°C is the cutting part hopper that stores granulated slag, (2) is the feeder installed under the cutting port that can separate large lumps of slag, and (2) is the raw material input chute (lb) of this equipment. The high-moisture granulated slag is fed by a crane cf into the cutting section hopper OD, which is equipped with a gate to adjust the cutting amount.
The 5 pieces are cut out by the feeder and placed on the variable speed supply conveyor 03, and then transferred to the input chute (lb) of the dewatering system.
) and are sequentially introduced into the airflow supply g(1).

4     投入された茜水分水砕スラグはファン(υ
の駆動により圧送気流と共に気流供給g(1)を経て脱
水機内に送り込まれる。この時すでに駆動装置(2d)
により回転している吸引ファンプレート(2a)に高水
分水砕スラグは吸いつけられ、その水分は吸引ファンプ
レート(2a)のスリット(2b)を通じて裏側の排気
ケーシング(4)内に吸引され、下方の水回収シュート
(4b)にて回収される。
4 The injected madder water granulated slag is passed through a fan (υ
is sent into the dehydrator together with the pressurized airflow through the airflow supply g(1). At this time, the drive device (2d)
The high-moisture granulated slag is attracted to the rotating suction fan plate (2a), and the moisture is sucked into the exhaust casing (4) on the back side through the slit (2b) of the suction fan plate (2a), and is sucked downward. The water is collected through the water collection chute (4b).

一方水分を除去された低水分水砕スラグは吸引ファンプ
レート(2a)の回転力により前面を滑り下方の原料回
収シュート(3a)により回収されて、その出口に設置
された回収コンベヤーa4により低水分水砕スラグ積出
ホッパーαGに一時貯溜され、トラックOeにて顧客工
場に輸送する。吸引ファンプレート(2a)の裏側に吸
引された空気と水分は排気ケーシング(4)内にて菖量
差により分離され、水は111述の如く下方へ行き、シ
ュート(4b)及び管により適宜に設置近されたタンク
αηに導かれ、ポンプO膀にて再使用先に圧送する。
On the other hand, the low-moisture granulated slag from which water has been removed slides down the front surface by the rotational force of the suction fan plate (2a) and is collected by the raw material collection chute (3a) below, and is transported to a low-moisture granulated slag by the collection conveyor A4 installed at the outlet of the chute (3a). The granulated slag is temporarily stored in the granulated slag shipping hopper αG and transported to the customer's factory by truck Oe. The air and moisture sucked into the back side of the suction fan plate (2a) are separated in the exhaust casing (4) by the difference in irises volume, and the water goes downward as described in 111 and is appropriately removed by the chute (4b) and pipe. It is guided to a nearby tank αη and is pumped to a reuse destination using a pump O bladder.

一方空気は排気ケーシング(4)の下方にある水回収″
′−ト(4b)のダニ/ /< −(7) ttcて該
ケー″グ内     、黛を最も水分の分離に適した圧
力に調整されるので、此の圧気体は排気ケーシング上部
(4a)から主吸引ダクト(5)により消エネルギーの
ため高水分水砕スラグの供給に用Aられるファン(’1
a)の吸′込口に接続し、再使用されて、省エネルギー
が果される。
On the other hand, the air is collected under the exhaust casing (4).
Since the pressure inside the casing is adjusted to the most suitable pressure for moisture separation, this pressurized gas flows into the upper part of the exhaust casing (4a). From the main suction duct (5), a fan ('1
It is connected to the suction port in a) and is reused to save energy.

但し主吸引ダクト(5)にて送られる圧力気体の中には
微イ(口なウール質や針状のスラグ並びにペーパー状ミ
ストを含んでいるので、このままでは再使用が出来ない
ので主吸引ダクト(5)の途中には分離器(6)が設け
られ、これらを系外に除去する様にしたものである。又
高水分水砕スラグをファン(1a)によって送り込む空
気量と主吸引タクト(5)を経て再使用する空気量にア
ンバランスが生じた時にはダンパー(8)により副吸引
孔(5a)の一度を加減し大気を吸込ませて気流供給に
適した量に調整するものである。
However, the pressurized gas sent through the main suction duct (5) contains fine wool, needle-like slag, and paper-like mist, so it cannot be reused as it is, so the main suction duct A separator (6) is installed in the middle of (5) to remove these from the system.Also, the amount of air sent into the high moisture granulated slag by the fan (1a) and the main suction tact ( When an imbalance occurs in the amount of air reused through step 5), the damper (8) adjusts the amount of air in the sub suction hole (5a) to suck in atmospheric air and adjust the amount to an amount suitable for supplying airflow.

第5図は晶水分水砕スラグの本発明装置による脱水ii
1と脱水処理後のサンプリング試験結果を示すもので脱
水Oil水分%は平均//7にあったものが、前記の如
く本装置による脱水後水分には平均ムざ%に減少した。
Figure 5 shows dehydration of crystalline water granulated slag using the apparatus of the present invention.
1 shows the results of a sampling test after dehydration treatment, and the dehydrated oil moisture % was on average 7/7, but as mentioned above, after dehydration using this device, the moisture content decreased to an average muzzle %.

発明の詳細 な説明した様に本発明装置4によれば、湿粉体および湿
粉体4漏水分原料を気流供給によってケーシング内で回
転する吸引ローターに放出すると共に、該ローター周囲
の多数のスリットを有するPLII形状吸引ファンプレ
ートの後面への気体の吸引作用によって吸いつけ、かつ
回転力で放出し回収するようにしたものであるから、熱
乾燥でなく吸引脱水によって高水分原料の水分を容易に
除去できると共に、原料が摩耗性を弔し、かつ、多孔質
のものでも摩耗、破孔の虞れや、吸引ファンプレートの
損傷も少なく長時間連続運転が可能であり、又吸引ファ
ンプレートの裏側に吸引された気体及び水分1d M 
貴差により分離され、水が回収されると共に気体は分離
器を経て高水分原料の気流供給に再使用されるので、微
細粉体、水分の飛散による環境悪化も皆無で、省エネル
ギーと環境保全に有効であり、しかも構成も簡単で経済
的な脱水装置を提供し得る。又此の装置により処理した
水砕スラグの水分除去の実績は第S図に示す如く高い脱
水効果を上げ、耐久性、環境保持と低電力にて運転を縦
続してイル。
As described in detail, according to the device 4 of the present invention, the wet powder and the raw material leaking from the wet powder 4 are discharged into the suction rotor rotating within the casing by air flow supply, and a large number of slits around the rotor are discharged. The PLII-shaped suction fan plate has a PLII-shaped suction fan plate that attracts gas by the suction action on the rear surface, and releases and collects it by rotational force, making it easy to remove water from high-moisture raw materials by suction dehydration rather than heat drying. In addition, the material is abrasive, and even if it is porous, there is no risk of abrasion, rupture, or damage to the suction fan plate, and continuous operation for long periods of time is possible. Gas and moisture sucked into 1d M
The water is separated by a pressure difference, and while the water is recovered, the gas is reused for the air flow supply of high-moisture raw materials through a separator, so there is no environmental deterioration due to the scattering of fine powder or water, resulting in energy savings and environmental protection. It is possible to provide an effective, simple and economical dewatering device. In addition, the track record of water removal from granulated slag treated with this equipment is as shown in Figure S, with a high dehydration effect, durability, environmental protection, and low power consumption.

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

第1図は本発明装置の構成を示す断面図、第2図は木装
置火を高炉水砕スラグの脱水装置に適用した実施例を示
す説明図、第3図は本発明装置における吸引ファンプレ
ートを備えた吸引ローターの正面概略図、第9図は吸引
ファンプレートの一部斜面図、第S図は本発明の実施例
におけろ水砕スラグの脱水611と脱水後のサンプリン
グ試験実績を示すグラフである。 (1)・・気流供給管、(1a)・・ファン、(lb)
・・原料投入シュート 、 (21・・吸引ローター、
 (2a)・・吸引ファンプレート、 (2b)・・ス
リット、(31・・ケーシング、(3a)・・低水分原
料回収シュート、(4)・・排気ケーシング、(4a)
・・排気ケーシング上部、(5)・・主吸引ダクト、(
5a)・・副吸引孔、(6)・・分離器、(7)、(8
)・・ダンパー。
Fig. 1 is a sectional view showing the configuration of the device of the present invention, Fig. 2 is an explanatory view showing an embodiment in which a wood device fire is applied to a dehydration device for granulated blast furnace slag, and Fig. 3 is a suction fan plate in the device of the present invention. FIG. 9 is a partial perspective view of the suction fan plate, and FIG. It is a graph. (1)...Airflow supply pipe, (1a)...Fan, (lb)
・・Raw material input chute, (21・・Suction rotor,
(2a)...Suction fan plate, (2b)...Slit, (31...Casing, (3a)...Low moisture raw material recovery chute, (4)...Exhaust casing, (4a)
・・Top of exhaust casing, (5)・・Main suction duct, (
5a)... Sub suction hole, (6)... Separator, (7), (8
)...damper.

Claims (1)

【特許請求の範囲】[Claims] 1、吸引ローター(2)の吸引力とファン(1a)の吸
引力の相乗効果による脱水を目的とする系統の中間にフ
ァンを設置し之に接続された湿紛、粒体等の高水分原料
を送り込むシュート(1b)を設けた原料の気流供給管
(1)と、周囲を放射方向に多数穿設し、耐摩耗性を有
する吸引ファンプレート(2a)により円錐状に構成し
た吸引ローター(2)とを設置し、吸引ローター(2)
及び吸引ファンプレート(2a)の前、後面を包むケー
シング(3)と排気ケーシング(4)を設けると共に、
排気ケーシングの上部(4a)と前記ファン(1a)の
吸込口とを途中に分離器(6)及びダンパー(8)付副
吸引孔(5a)を介し主吸引ダクト(5)で接続し、前
記ケーシング(3)の下部に低水分原料回収シュート(
3a)を、また排気ケーシング(4)の下部にダンパー
(7)付の水回収シュート(4b)を設けた脱水系より
なる摩耗性を有する湿粉体および湿粒体の脱水装置。
1. A fan is installed in the middle of the system for the purpose of dehydration by the synergistic effect of the suction force of the suction rotor (2) and the suction force of the fan (1a), and high moisture raw materials such as wet powder and granules are connected to it. A suction rotor (2) configured in a conical shape with a suction fan plate (2a) having abrasion resistance and having many perforations in the radial direction around the periphery. ) and suction rotor (2).
In addition to providing a casing (3) and an exhaust casing (4) that enclose the front and rear surfaces of the suction fan plate (2a),
The upper part (4a) of the exhaust casing and the suction port of the fan (1a) are connected by the main suction duct (5) through a sub-suction hole (5a) with a separator (6) and a damper (8) in the middle. A low moisture material recovery chute (
3a), and a dehydration system for abrasive wet powder and wet granules comprising a dehydration system provided with a water recovery chute (4b) with a damper (7) at the bottom of the exhaust casing (4).
JP12432984A 1984-06-15 1984-06-15 Apparatus for dehydrating wet powder and wet granule having abrasive property Granted JPS614553A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12432984A JPS614553A (en) 1984-06-15 1984-06-15 Apparatus for dehydrating wet powder and wet granule having abrasive property

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12432984A JPS614553A (en) 1984-06-15 1984-06-15 Apparatus for dehydrating wet powder and wet granule having abrasive property

Publications (2)

Publication Number Publication Date
JPS614553A true JPS614553A (en) 1986-01-10
JPH0536082B2 JPH0536082B2 (en) 1993-05-28

Family

ID=14882640

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12432984A Granted JPS614553A (en) 1984-06-15 1984-06-15 Apparatus for dehydrating wet powder and wet granule having abrasive property

Country Status (1)

Country Link
JP (1) JPS614553A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4771714A (en) * 1985-08-16 1988-09-20 Mefina S.A. Electric sewing machine with computerized control
US7651753B2 (en) 2002-07-05 2010-01-26 Emitec Gesellschaft Fuer Emissionstechnologie Mbh Process and apparatus for spatially inhomogeneously coating a honeycomb body and inhomogeneously coated honeycomb body

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4771714A (en) * 1985-08-16 1988-09-20 Mefina S.A. Electric sewing machine with computerized control
US7651753B2 (en) 2002-07-05 2010-01-26 Emitec Gesellschaft Fuer Emissionstechnologie Mbh Process and apparatus for spatially inhomogeneously coating a honeycomb body and inhomogeneously coated honeycomb body

Also Published As

Publication number Publication date
JPH0536082B2 (en) 1993-05-28

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