JPH03195888A - Method and apparatus for drying particulate material - Google Patents
Method and apparatus for drying particulate materialInfo
- Publication number
- JPH03195888A JPH03195888A JP33749089A JP33749089A JPH03195888A JP H03195888 A JPH03195888 A JP H03195888A JP 33749089 A JP33749089 A JP 33749089A JP 33749089 A JP33749089 A JP 33749089A JP H03195888 A JPH03195888 A JP H03195888A
- Authority
- JP
- Japan
- Prior art keywords
- drying
- drying cylinder
- dried
- substance
- powder
- 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.)
- Pending
Links
- 238000001035 drying Methods 0.000 title claims abstract description 68
- 239000011236 particulate material Substances 0.000 title abstract 2
- 238000000034 method Methods 0.000 title description 8
- 239000000126 substance Substances 0.000 claims abstract description 20
- 238000007599 discharging Methods 0.000 claims abstract description 4
- 239000000463 material Substances 0.000 claims description 18
- 239000008187 granular material Substances 0.000 claims description 14
- 238000010438 heat treatment Methods 0.000 claims description 14
- 239000000843 powder Substances 0.000 claims description 13
- 230000005484 gravity Effects 0.000 claims description 10
- 238000003780 insertion Methods 0.000 claims description 8
- 230000037431 insertion Effects 0.000 claims description 8
- 238000007664 blowing Methods 0.000 claims description 7
- 239000002245 particle Substances 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 3
- 230000007423 decrease Effects 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 14
- 230000004888 barrier function Effects 0.000 abstract 2
- 230000000630 rising effect Effects 0.000 abstract 1
- 239000002994 raw material Substances 0.000 description 5
- 235000013305 food Nutrition 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000002440 industrial waste Substances 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、特に含水率の高い粉粒体の乾燥方法ならび
にその装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention particularly relates to a method for drying powder and granular material having a high moisture content and an apparatus therefor.
この発明の方法ならびに装置によ−1て乾燥される含水
粉粒体は、主に設定した低含水率に乾燥された後、食品
の原材料となることを主目的とするものであるが、高含
水率の粉粒体を設定する低含水率まで高速で乾燥するに
は高カロリーを必要とし、nつ、該乾燥過程で用いる高
熱により品質に変化を来したもので、本発明で用いる物
質は食品の原材料でありながら本発明を用いて産出しよ
うとする物質は考えられてはいたものの、適当な方法、
1段、装置等がなく、実施を試みれば、変質などによる
歩留まりがおもわしくなか−・たり、また、大量の熱漬
の使用で採算面で6商品化はむづかしい課題が山積した
ものであるから、これら産出する所望物質の生産開発を
手掛ける考も少ないのが現状である。The water-containing powder and granules dried by the method and apparatus of the present invention (1) are mainly intended to be used as raw materials for foods after being dried to a predetermined low moisture content. Drying powder and granules with a moisture content at high speed to a low moisture content requires high calories, and the high heat used in the drying process causes changes in quality.The material used in the present invention is Although the substance to be produced using the present invention, which is a raw material for food, has been considered, it has not been possible to produce it using an appropriate method.
There was no first-stage equipment, and if we tried to implement it, the yield would be poor due to deterioration, etc. Also, the use of a large amount of hot soaking made commercialization difficult from a profitability standpoint.There were many problems. Therefore, at present, there is little thought to engage in the production and development of these desired substances.
本発明の方法ならびに装置を用いようと°4°る原材料
の高含水物質は、食品製造時に排出されろ残滓で、僅か
一部は再利用されるが現在ではその殆どが廃棄処分され
るものである。しかしながら、本物質は前述の通り高含
水率物質であるから産業廃棄物として取り扱われ、公害
物質視されている。The highly water-containing raw materials that are used in the method and apparatus of the present invention are residues that are discharged during food manufacturing, and although a small portion is recycled, most of them are currently disposed of. be. However, as mentioned above, this substance has a high water content, so it is treated as industrial waste and considered a polluting substance.
本発明では前記した産業廃棄物視されている物質を再利
用して原材料ととすることができる方法ならびにその装
置を開発したものである。The present invention has developed a method and an apparatus for reusing the above-mentioned materials considered to be industrial waste as raw materials.
特に含水率が高い粉粒体を設定した低含水率まで乾燥さ
せる手段としてバーナー装置と送風装置とを組み合わせ
た乾燥機構は数多の種類と多数の形態ならびに構成のも
のがある。In particular, there are many types, forms, and configurations of drying mechanisms that combine a burner device and a blower device as a means for drying a powder or granular material with a high moisture content to a predetermined low moisture content.
しかしながら、高含水物質の乾燥手段は加熱乾燥をはじ
めとして古来から用いられている自然乾燥、また、現在
では急速極冷却手段等がある。However, methods for drying highly water-containing substances include heat drying, natural drying that has been used since ancient times, and rapid polar cooling methods that are currently available.
これら、複数の乾燥方法の種類および経時的な乾燥手段
があるが、被乾燥体によ−)では用いる方法の種類なら
びに手段によ−)ては所望乾燥度合いに達する時点では
経時的、あるいは被乾燥体固有の温度と極度に異なる温
度によって材質的変化を来し、所望する低含水率に到達
はするものの異質に変化してしまうことも希ではない。There are multiple types of drying methods and drying methods that dry over time, but depending on the type of method and means used for the object to be dried, the desired degree of drying may be achieved over time or over time. It is not uncommon for material changes to occur due to temperatures extremely different from those inherent to the dried material, and although the desired low moisture content may be achieved, the material changes to a different quality.
そこでこの発明は、乾燥手段として加熱手段と」−昇風
向雰囲気を形成し、この雰囲気内に挿入した高含水の粉
粒体に対し乾燥作用と同時に上方向への吹ト作用を付与
することによりト、方向に飛散し、該飛散した上位によ
−、て弱ま−、た風力と個々の含水粉粒中休の比重との
相関的現象とにより風圧の低い箇所では落下現象を呈し
、ここで−・つの対流循環形態が形成されることを目的
とするものである。Therefore, the present invention uses a heating means as a drying means to form an atmosphere in an upward direction, and to apply an upward blowing action to the highly water-containing powder and granules inserted into this atmosphere. Due to the correlation between the wind force and the specific gravity of individual water-containing powder grains, a falling phenomenon occurs in places where the wind pressure is low. The purpose is to form two convective circulation forms.
本発明は上記した目的を達成させるための手段として、
加熱装置と、上方を指向する風向を生じさせる送風装置
を備えた乾燥筒内に下方より含水被乾燥物質を挿入し、
吹上作用で上方に飛散させて乾燥しつつ、吹−ヒ風力と
単位粒子との相対的比重関係によりL下方向の対流循環
を生じせしめ、乾燥度合いの進行に伴い軽減されていく
比重に比例して前記の対流循環位置を逐次上方に移行さ
せ、これら対流循環作用を重複り昇している間?こ設定
した低含水率に到達した被乾燥物質のみが乾燥筒の最上
部より外部には排出できるようにしたものであろへ
また、乾燥筒内の内壁に設けた邪魔板によって、吹上げ
られた被乾燥物質に対し強制対流循環を促進オろことが
できるようにしたものである。The present invention, as a means to achieve the above-mentioned objects,
A water-containing substance to be dried is inserted from below into a drying cylinder equipped with a heating device and a blower device that generates an upwardly directed wind direction.
While the particles are scattered upward by the blow-up action and dried, a downward convection circulation occurs due to the relationship between the blowing force and the relative specific gravity of the unit particles, and as the degree of drying progresses, the particles decrease in proportion to the specific gravity. The above convective circulation position is successively shifted upward, and while these convective circulation actions are being repeated and ascending? Only the material to be dried that has reached the set low moisture content can be discharged from the top of the drying cylinder to the outside. It is designed to promote forced convection circulation of the material to be dried.
また史に、被乾燥物質の挿入孔を下部に有し乾燥された
物質を外部に放出する排出孔を有する縦型円筒体を乾燥
筒とし、その底部付近に加熱装置ならびに風向を上方と
する送風装置とを備え、また、前記挿入孔の上方の乾燥
筒の内周に複数段の邪魔板装置を中央部に吹上通路が形
成できるようにしてなるものである。In addition, in history, a drying cylinder is a vertical cylindrical body with an insertion hole for the material to be dried at the bottom and a discharge hole for discharging the dried material to the outside. The apparatus also includes a plurality of baffle plate apparatuses on the inner periphery of the drying tube above the insertion hole so that a blow-up passage can be formed in the center.
更にまた、乾燥筒内に装置する加熱装置を遠赤外線放射
器とするものである。Furthermore, the heating device installed inside the drying cylinder is a far-infrared radiator.
なおまた、中央部に吹上通路を形成できるように設置す
る複数の邪魔板の個々は、斜状となるようにその一側を
乾燥筒内壁に装着して成るものである。Furthermore, each of the plurality of baffle plates installed so as to form a blow-up passage in the center is attached to the inner wall of the drying cylinder with one side thereof obliquely.
この発明は、乾燥筒内の下部に、乾燥手段として加熱手
段と一ヒ昇風向雰囲気を形成し、この雰囲気内に挿入し
た高含水の粉粒体に対し乾燥作用と同時に−L方向への
吹−に作用を付与することにより上方向に飛散し、該飛
散した上方位置によ−)で弱ま−、た風力と個々の含水
粉粒中休の比重との相関的現象とにより風圧の低い箇所
では落下現象を呈し、ここで−・つの対流循環形態が形
成される。また、この対流循環形態を促進するために邪
魔板を設けて該形態を補助してやるものである。このよ
うにして、ある高さ位置で形成された区間の対流循環作
用中にも乾燥作用が進展し個々の中休の比重が軽減され
ることによって対流循環のト限位置ならびに下限位置が
徐々にに1位に移行し、逐次対流循環作用を生じせしめ
乾燥度合いの進行状態に比例して軽減された比重と相ま
−・てその対流循環位置を自然り昇させ最終的には設定
した乾燥度合いに達した時点で外部に放出できるように
したしのである。This invention forms an atmosphere in the lower part of the drying cylinder with a heating means as a drying means, and blows in the -L direction at the same time as drying the highly water-containing powder and granules inserted into this atmosphere. The wind pressure is low due to the correlation phenomenon between the wind force and the specific gravity of the individual water-containing powder grains. At some points, a falling phenomenon occurs, and two convection circulation forms are formed here. Further, in order to promote this convection circulation form, a baffle plate is provided to assist this form. In this way, the drying action progresses even during the convective circulation action in the section formed at a certain height position, and the specific gravity of each middle break is reduced, so that the upper and lower limit positions of the convective circulation gradually shift. The convective circulation position is gradually raised to the first position, and the specific gravity is reduced in proportion to the degree of drying. It was designed so that it could be released to the outside as soon as it reached this point.
)1方を指向する風力は邪魔板設置箇所にも吹き上げら
れ、該邪魔板の設置形態に準じて導かれて螺旋状となり
この風向に準じて被乾燥物質も邪魔板に当接・反射を繰
り返し乾燥作用雰開気内でその含水率を低−トさせると
ともに比重自体をも軽減させて吹き上げ風力と比重との
相関関係により全体的に上位置へと移行していく。) The wind force oriented in one direction is also blown up at the location where the baffle plate is installed, and is guided according to the installation form of the baffle plate to form a spiral shape, and the material to be dried repeatedly comes into contact with the baffle plate and is reflected according to the wind direction. In the drying atmosphere, the moisture content is lowered and the specific gravity itself is also reduced, and the overall position is shifted to the upper position due to the correlation between the blowing wind force and the specific gravity.
加熱装置が発熱体であれば、吹き上げ風向が届く範囲が
乾燥雰囲気帯となり、又、加熱装置が遠赤外線放射体と
すれば乾燥雰囲気帯が照射区域となり、この場合の乾燥
雰囲気帯の雰囲気は高温化せず、照射された被乾燥体の
みが然エネルギ〜に変換されて乾燥作用を呈す。If the heating device is a heating element, the range that the blowing air can reach becomes the dry atmosphere zone, and if the heating device is a far-infrared radiator, the dry atmosphere zone becomes the irradiation area, and in this case, the atmosphere in the dry atmosphere zone is high temperature. Only the irradiated object to be dried is converted into natural energy and exhibits a drying effect.
遠赤外線とは、赤外線の一種で、波長が5ミクロンから
1ミクロン程度の電磁波を指し、その波長は高分子化合
物などの固有の振動数(波長)に近いもので、物質に対
する透過力が弱く、物質によく吸収される。また、物質
に吸収されても化学変化を起こす程のエネルギーレベル
は高くないのでそのまま熱エネルギーに変換されろもの
で遠赤外線を加熱装置の加熱手段として用いることによ
り乾燥時間を短縮し、且つ、物質変化を及ぼさなく、更
に熱エネルギー単価も安く理想的乾燥手段である、。Far-infrared rays are a type of infrared rays, and refer to electromagnetic waves with a wavelength of about 5 microns to 1 micron.The wavelength is close to the unique frequency (wavelength) of polymer compounds, etc., and has weak penetrating power through materials. Well absorbed by substances. In addition, even if it is absorbed by a material, the energy level is not high enough to cause a chemical change, so it will not be converted directly into thermal energy.By using far infrared rays as a heating means of a heating device, drying time can be shortened and the material can be heated. It is an ideal drying method because it does not cause any change and the unit cost of heat energy is low.
次に、本発明を実施する装置について図面とともに説明
すれば、被乾燥物質の挿入孔(4)を下部にイ丁し乾燥
された物質を外部に放出する排出孔(5)を有する縦型
円筒体を乾燥筒(1)とし、その底部付近に加熱装?!
、(3)ならびに風向を上方とする送風装置(2)とを
備え、また、前記挿入孔(4)の上方の乾燥筒(1)の
内周に複数段の邪魔板(6)装置を中央部に吹−L通路
(8)が形成できるようにしてなることを乾燥筒(1)
の基本形態とするもので、前記邪魔板(6)は複数の各
々が斜状となるようにその一側を乾燥筒(1)の内壁(
7)に装着し、装着された各邪魔板(6)の内側に前記
した吹上通路(8)が形成されるように構成するもので
ある。このようにして、前記邪魔板装置を複数段形成し
て乾燥雰囲気帯囲(9)を設け、そのF方に螺旋環装置
(1o)を形成し、」二端間rlffi付近に前記した
排出孔(5)が開口するように乾燥筒(1)を構成する
。Next, the apparatus for carrying out the present invention will be described with reference to the drawings. It is a vertical cylinder having an insertion hole (4) for the substance to be dried at the bottom and a discharge hole (5) for discharging the dried substance to the outside. The body is a drying cylinder (1), and there is a heating device near the bottom of the drying cylinder (1). !
, (3) and a blower device (2) whose air direction is directed upward, and a plurality of baffle plate (6) devices are arranged in the center on the inner periphery of the drying cylinder (1) above the insertion hole (4). A blow-L passage (8) can be formed in the drying cylinder (1).
The baffle plates (6) have one side connected to the inner wall (1) of the drying cylinder (1) so that each of the baffle plates (6) is obliquely shaped.
7), and is constructed so that the blow-up passage (8) described above is formed inside each of the attached baffle plates (6). In this way, the baffle plate device is formed in multiple stages to provide a dry atmosphere zone (9), and the spiral ring device (1o) is formed in the F direction of the baffle plate device, and the above-mentioned discharge hole is formed near the rlffi between the two ends. The drying cylinder (1) is configured so that (5) is open.
なお、この乾燥筒(1)に対し、被乾燥物質を供給する
ホッパー(11)を備え、該ホッパー(11)より移送
手段を介して接続した供給管(12)の先端を前記挿入
孔(4)に連結するものであり、また、乾燥n(1)、
1:部に設けた排出孔(5)には送出管(13)を接続
して調整ff!i(+4)に挿入されるように形成し、
ここで設定した減食水率に到達しなのものならびに乾燥
筒(+)からの排出空気とともに再度乾燥筒(1)内に
挿入する還元装置(+5)を介して乾燥筒(1)の底部
付近に接続し、一方、設定した低含水率に到達した粉粒
体は調整筒(14)の上位に設けた出口(16)より外
部に産出させるものである。The drying tube (1) is equipped with a hopper (11) for supplying the substance to be dried, and the tip of the supply pipe (12) connected to the hopper (11) via a transfer means is inserted into the insertion hole (4). ), and also dry n(1),
1: Connect the delivery pipe (13) to the discharge hole (5) provided in the section and adjust ff! formed to be inserted into i(+4),
The water that has not reached the reduced edible water rate set here and the air discharged from the drying cylinder (+) are passed through the reducing device (+5), which is inserted into the drying cylinder (1) again, to the vicinity of the bottom of the drying cylinder (1). On the other hand, the powder and granules that have reached the set low moisture content are outputted to the outside from the outlet (16) provided above the adjustment cylinder (14).
なお図中、符号(17)はモータを示すものである。In addition, in the figure, the code|symbol (17) shows a motor.
更に、前記したシステムにおいて、被乾燥物質で特に含
水率の高い物質の乾燥作業において、前記乾燥筒(+)
の複数を重連して行うことも任意であり、更にまた、前
記作用で説明した高含水物質は、σ腐の生産過程で産す
る残滓、即ち、「オカラ1を対象として説明したもので
、従来その殆どが廃棄処分の対象となった物質を食品あ
るいは飼料または肥料の原材料として再利用するための
乾燥手段を根底にして開示したものである。Furthermore, in the above-mentioned system, when drying a substance to be dried, especially a substance with a high moisture content, the drying tube (+)
It is also optional to carry out multiple combinations of the above.Furthermore, the high water content substance explained in the above action is the residue produced in the production process of sigma rot, that is, the one explained for "Okara 1". Most of these disclosures are based on drying methods for reusing materials that have conventionally been disposed of as raw materials for food, feed, or fertilizer.
本発明は以上のように、高含水率の粉粒体物質を、その
物質を変質させないで、且つ、小規模で、設定する低含
水率に乾燥することができるもので、熱エネルギー中価
がやすく、シかも安定した無変質粉粒物質を得ることが
できる効果あるものである。As described above, the present invention is capable of drying a granular material with a high moisture content to a predetermined low moisture content on a small scale without deteriorating the substance, and with a low median thermal energy cost. It is effective in that it is easy to obtain a stable and unaltered granular material.
第1図は本発明の全体縦断面図、第2図は平面図である
。
(1)・・・乾燥筒、(2)・・・送風装置、(3)・
・・加熱装置、(4)・・・挿入孔、(5)・・・排出
孔、(6)・・・邪魔板、(7)・・・内壁、(8)・
・・吹上通路。FIG. 1 is an overall vertical sectional view of the present invention, and FIG. 2 is a plan view. (1)... Drying tube, (2)... Air blower, (3)...
... heating device, (4) ... insertion hole, (5) ... discharge hole, (6) ... baffle plate, (7) ... inner wall, (8) ...
・Fukiage passage.
Claims (1)
送風装置とを備えた乾燥筒内に下方より含水被乾燥物質
を挿入し、吹上作用で上方に飛散させて乾燥しつつ、吹
上風力と単位粒子との相対的比重関係により上下方向の
対流循環を生じせしめ、乾燥度合いの進行に伴い軽減さ
れていく比重に比例して前記の対流循環位置を逐次上方
に移行させ、これら対流循環作用を重複上昇している間
に設定した低含水率に到達した被乾燥物質のみが乾燥筒
の最上部より外部には排出できるようにしたことを特徴
とする粉粒体の乾燥方法。 〔2〕、乾燥筒内の内壁に設けた邪魔板によって、吹上
げられた被乾燥物質に対し強制対流循環を促進すること
ができるようにしたことを特徴とする請求項1記載の粉
粒体の乾燥方法。 〔3〕、被乾燥物質の挿入孔を下部に有し乾燥された物
質を外部に放出する排出孔を有する縦型円筒体を乾燥筒
とし、その底部付近に加熱装置ならびに風向を上方とす
る送風装置とを備え、また、前記挿入孔の上方の乾燥筒
の内周に複数段の邪魔板装置を中央部に吹上通路が形成
できるようにして構成したことを特徴とする粉粒体の乾
燥装置。 〔4〕、乾燥筒内に装置する加熱装置を遠赤外線放射器
とすることを特徴とする請求項3記載の粉粒体の乾燥装
置。 〔5〕、中央部に吹上通路を形成できるように設置する
複数の邪魔板の個々は、斜状となるようにその一側を乾
燥筒内壁に装着して成ることを特徴とする請求項3記載
の粉粒体の乾燥装置。[Claims] [1] A moisture-containing substance to be dried is inserted from below into a drying cylinder equipped with a heating device and a blowing device that generates an upwardly directed wind direction, and is blown upward by an upward blowing action. While drying, vertical convection circulation is generated due to the relative specific gravity relationship between the blowing wind force and the unit particles, and the convection circulation position is sequentially shifted upward in proportion to the specific gravity that decreases as the degree of drying progresses. The powder and granular material is characterized in that only the material to be dried that reaches a preset low moisture content while increasing these convective circulation effects can be discharged from the top of the drying cylinder to the outside. Drying method. [2] The granular material according to claim 1, characterized in that forced convection circulation of the blown up material to be dried can be promoted by a baffle plate provided on the inner wall of the drying cylinder. drying method. [3] A vertical cylindrical body with an insertion hole for the material to be dried at the bottom and a discharge hole for discharging the dried material to the outside is used as a drying cylinder, and a heating device and an air blower with the wind direction upward are installed near the bottom of the drying cylinder. A drying device for powder and granular materials, further comprising a plurality of baffle plate devices on the inner periphery of the drying tube above the insertion hole so that an upflow passage can be formed in the center. . [4] The apparatus for drying powder or granular material according to claim 3, wherein the heating device installed in the drying cylinder is a far-infrared radiator. [5] Claim 3, wherein each of the plurality of baffle plates installed to form a blow-up passage in the center is attached to the inner wall of the drying cylinder on one side in a diagonal manner. The drying device for powder and granular material described above.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33749089A JPH03195888A (en) | 1989-12-26 | 1989-12-26 | Method and apparatus for drying particulate material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33749089A JPH03195888A (en) | 1989-12-26 | 1989-12-26 | Method and apparatus for drying particulate material |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03195888A true JPH03195888A (en) | 1991-08-27 |
Family
ID=18309143
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33749089A Pending JPH03195888A (en) | 1989-12-26 | 1989-12-26 | Method and apparatus for drying particulate material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03195888A (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4828557A (en) * | 1971-08-18 | 1973-04-16 | ||
JPS5129764A (en) * | 1974-07-06 | 1976-03-13 | Hoechst Ag | |
JPS5465875A (en) * | 1977-11-05 | 1979-05-26 | Shinko Electric Co Ltd | Heating and drying device |
JPS5589680A (en) * | 1978-12-25 | 1980-07-07 | Chuo Kakoki | Vertical vibrating dryer |
JPS63161382A (en) * | 1986-12-23 | 1988-07-05 | 昭和飛行機工業株式会社 | Method and device for drying powder |
-
1989
- 1989-12-26 JP JP33749089A patent/JPH03195888A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4828557A (en) * | 1971-08-18 | 1973-04-16 | ||
JPS5129764A (en) * | 1974-07-06 | 1976-03-13 | Hoechst Ag | |
JPS5465875A (en) * | 1977-11-05 | 1979-05-26 | Shinko Electric Co Ltd | Heating and drying device |
JPS5589680A (en) * | 1978-12-25 | 1980-07-07 | Chuo Kakoki | Vertical vibrating dryer |
JPS63161382A (en) * | 1986-12-23 | 1988-07-05 | 昭和飛行機工業株式会社 | Method and device for drying powder |
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