JPS61268976A - Flow regulating plate - Google Patents
Flow regulating plateInfo
- Publication number
- JPS61268976A JPS61268976A JP10985685A JP10985685A JPS61268976A JP S61268976 A JPS61268976 A JP S61268976A JP 10985685 A JP10985685 A JP 10985685A JP 10985685 A JP10985685 A JP 10985685A JP S61268976 A JPS61268976 A JP S61268976A
- Authority
- JP
- Japan
- Prior art keywords
- plate
- powder
- hot air
- flow regulating
- regulating plate
- 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
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明に例えば粉状又に粒状材料t−窒気流により乾燥
又は冷却するのに用いて最適な整流板に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a rectifier plate suitable for use in drying or cooling powdered or granular materials by nitrogen flow.
第5図〜第7図は従来の整流板5Iを示すものであるが
、図において多数の千板圓が平行iC並んでおり、これ
らの間に通孔としてのスリット旧全形成させている。多
数の平板4υの長手方向と直角に延びる複数のリプ14
IJによって平板(4υは補強されている。FIGS. 5 to 7 show a conventional rectifying plate 5I, in which a large number of semicircular circles are lined up in parallel iC, and slits serving as through holes are completely formed between them. A plurality of lips 14 extending perpendicularly to the longitudinal direction of a large number of flat plates 4υ
A flat plate (4υ is reinforced by IJ).
平板(4υの巾は例えば約25mm K対しスリット(
6)の巾は約0.8〜1.0mm″′Cあるが(図をわ
かりやすくするために寸法比に無視している)、下方か
ら熱風が吹き込まれ、スリット(6)により整流して上
方へと導かれる。図示せずとも整流板T0n上には粉粒
状の材料かの任っており整流板6Iの斜方向aの撮動に
より右方へと移送されているのであるが、この移送途上
で整流された熱風により流動化されて乾燥される。A flat plate (the width of 4υ is about 25mm, for example, a slit for K) (
6) has a width of approximately 0.8 to 1.0 mm''C (ignored to the size ratio to make the diagram easier to understand), hot air is blown from below and rectified by the slit (6). Even though it is not shown in the figure, there is a powder-like material on the current plate T0n, and it is transported to the right by the movement of the current plate 6I in the diagonal direction a. During transportation, it is fluidized and dried by rectified hot air.
然るにスリット(社)の巾より小さい粒度の粉は吹き上
げる熱風により流動化され、直接にセ、スリン) t4
3 を通って整流版図の下方に落下しないもの\、結局
は下方に落下してこの処理に困ることがある。However, powder with a particle size smaller than the width of the slit is fluidized by the hot air that blows up, and is directly blown away.
3. Items that do not fall below the rectifier map may end up falling downwards, causing problems with this process.
本発8Aは上述の問題Kgfiみてなされ、スリットの
巾より小さい粒度の粉又μ粒でも下方に落下しない整流
板を提供することを目的とする。The present invention 8A was developed in view of the above-mentioned problem Kgfi, and its purpose is to provide a rectifier plate that does not fall downward even when powder or micro-particles having a particle size smaller than the width of the slits.
上記目的は、多数の通孔を有し、下方からの空ツg f
i i前記通孔(より整流して上方に導くよりにしたv
5.面板において、前記]内7(1に屈曲して形成させ
たことを特徴とする整流板、によって達成される。The above purpose has a large number of through holes, and the holes g f from below.
i iThe through hole (v which was made to rectify the flow and guide it upward)
5. This is achieved by a rectifying plate characterized in that the face plate is bent in the above-mentioned inner part 7 (1).
整流板上の材料は下方からの空気流により流動化される
が、通孔の巾より小さい粒又は粉は通孔の屈曲部に堆積
して整流板の下方に落下することはない。あるいは屈曲
部に堆積している粉又は粒は下方からの空気流により整
流板の上方に吹き上げられる。Although the material on the baffle plate is fluidized by the airflow from below, particles or powder smaller than the width of the through hole are deposited at the bends of the through hole and do not fall below the baffle plate. Alternatively, powder or grains deposited on the bending portion are blown up above the current plate by an air flow from below.
以下、本発明の実施例の整流板が適用される撮動乾燥機
について第11J〜第4図を参照して説明する。Hereinafter, a photographic dryer to which the current plate according to the embodiment of the present invention is applied will be described with reference to FIGS. 11J to 4.
図において振動乾燥機に全体として(IIで示され、ト
ラフ(2)μフード(3)によって密閉されている。フ
ード(3)にμ開口(4m)(4h)が形成され、これ
らKは図示せずともダクトや吸引機などが接続されてい
るものとする。フード(3)には更に材料供給口(5ン
が形成され、こ\から粉粒状材料が併給される。トラフ
(2)の右端部には材料排出口(6)が形成されている
。In the figure, the vibratory dryer is shown as a whole (II) and is sealed by a trough (2) μ hood (3). μ openings (4m) (4h) are formed in the hood (3), these K are It is assumed that a duct, a suction machine, etc. are connected even if not shown.A material supply port (5) is also formed in the hood (3), from which powder and granular materials are simultaneously fed. A material discharge port (6) is formed at the right end.
トラフ(2)の両側壁部には熱風導入口(7a)(7b
)が形成され、これらには簡略化して示す配管(8a)
(8b)及び熱風供給管(9)が接続される。またトッ
プ(2]の両側壁部には取付板OQを介して衝げき緩和
用ゴムブツシュ(11)が取り付けられているが、これ
は平板041 CLI(13及びこれらに保持されたゴ
ム板(15a)(15h)から成り、平板(6)03は
取付板QOに固定されるが、内側の平板a<は駆動ロッ
ド(4)に固定される。Hot air inlets (7a) (7b) are provided on both side walls of the trough (2).
) are formed, and these include piping (8a) shown in simplified form.
(8b) and the hot air supply pipe (9) are connected. Rubber bushings (11) for shock mitigation are attached to both side walls of the top (2) via mounting plates OQ, but these are attached to the flat plate 041 CLI (13 and the rubber plate (15a) held by these). (15h), the flat plate (6) 03 is fixed to the mounting plate QO, while the inner flat plate a< is fixed to the drive rod (4).
駆動ロッド(6)はクランク部σ7)K枢着され、クラ
ンク部α7)はベル)Qllk介してモータQ!19に
よって回転駆動される。トラフ(2)にカウンターウェ
イトのトレi−(イ)及びコイルばね(211により結
合される。The drive rod (6) is pivotally connected to the crank part σ7)K, and the crank part α7) is connected to the motor Q! through the bell)Qllk. Rotationally driven by 19. It is connected to the trough (2) by a counterweight tray i-(A) and a coil spring (211).
すなわちトラフ(2)は矢印a方向に振動可能に支持さ
れる。カウンターウェイトノは防振用コイルばねムにL
り地上に支持される。That is, the trough (2) is supported so as to be able to vibrate in the direction of arrow a. The counterweight is attached to the anti-vibration coil spring.
supported on the ground.
トラフ(2)内には第2図〜第4図に明示されろ整直板
■が取付部材(ロ)を介して取り付けられている。Inside the trough (2), a straightening plate (2), clearly shown in FIGS. 2 to 4, is attached via a mounting member (B).
この整流板■によりトラフ(2)内は熱風導入側空間Q
4Iと熱風導出側空間5とに画成される。整流板C3[
Jは多数の平行に並ぶ断面が第4図に示す形状の部材C
31]から構成され、これらの間Kiミスリットして通
孔C3が形成されている。多数の部材(311は材料の
移送方向に延びる複数のリブ(至)によって補強される
、
通孔(33は第4図に示すようにクランク状に形成され
、上側垂1部(32a)、水平部(32b)及び下側垂
直部(32りから成っており矢印で示すように下方から
吹き上げられる熱風は通孔G3によp整流されて上万全
関6に導かれる。整流板叩は図示せずとも第1図におい
て右端部で逆り字形状に屈曲しており、その土の材料は
上述の材料排出口(6)へと導かれる。This rectifying plate ■ creates a space Q on the hot air introduction side inside the trough (2).
4I and a hot air outlet space 5. Current plate C3 [
J is a member C whose cross sections are arranged in parallel and have the shape shown in Fig. 4.
31], and a through hole C3 is formed by mislit Ki between these. A large number of members (311 are reinforced with a plurality of ribs extending in the material transfer direction), through holes (33 are formed in a crank shape as shown in Fig. 4, upper vertical part (32a), horizontal It consists of a part (32b) and a lower vertical part (32), and the hot air blown up from below as shown by the arrow is rectified by the through hole G3 and guided to the upper part 6.The rectifier plate is not shown. It is always bent in an inverted shape at the right end in FIG. 1, and the soil material is guided to the above-mentioned material discharge port (6).
本発明の実施例は以上のように構成されるが、次にこの
作用について説明する。The embodiment of the present invention is constructed as described above, and its operation will be explained next.
供給口(5)に投入された粉粒状材料はトラフ(2)内
で整流板q上を振動により右方へと移送される。The particulate material introduced into the supply port (5) is transferred to the right by vibration on the current plate q within the trough (2).
整流板田の下方からは熱哄が吹き上げ、通孔のによp整
流されて移送途上の粉粒状材料ti動化し、熱交換して
加熱乾燥する。Heat is blown up from below the rectifying plate and is rectified through the through holes, where it animates the powder and granular material being transported, heat exchanges it, and heats it to dry it.
流動化し皮粉粒状材料のうち通孔田の巾より小さい粒度
の粉又は粒は通孔国内に落下する。然しなから、これら
は通孔(33の水平部(32b)上に落ちて下側垂直部
(32り側へと落ちない。粉又は粒は水平1(32h)
上に堆積せんとしても下方から吹き上げる熱風により再
び整流根囲上方に吹き上げられろ。Among the fluidized skin powder granular materials, powder or grains having a particle size smaller than the width of the through hole fall into the through hole. However, these particles fall onto the horizontal part (32b) of the through hole (33) and do not fall to the lower vertical part (32h).
Even if it does not accumulate on top, the hot air blowing up from below will blow it up again above the rectified root wall.
加熱乾燥された材料に材料排出口(6)から外部に取り
量される。整流板■の以上のような作用によりこの下方
に粉又は粒が殆んど落下することなく、すべての材料は
材料排出口(6)から外部に排出される。The heated and dried material is taken out from the material outlet (6). Due to the above-mentioned action of the rectifying plate (2), almost no powder or grains fall below this plate, and all the materials are discharged to the outside from the material discharge port (6).
以上、本発明の実施例について説明したが、勿論、本発
明はこれに限定されることなく本発明の技術的思想に基
づいて種々の変形が可能である。Although the embodiments of the present invention have been described above, the present invention is of course not limited thereto, and various modifications can be made based on the technical idea of the present invention.
例えば、以上の実施例では整流根因を構成する長手状の
谷部材CDは単体から成るものとし九が、こnVC限る
ことなく複数の、例えば2つの部材から成るようにして
もよい。また通孔c3zの形状も第4図に図示のものに
限ることなく例えば更に屈曲部全増加させたものであっ
てもよい。For example, in the above embodiment, the longitudinal valley member CD constituting the rectification source is made up of a single member, but the nVC is not limited to this, and may be made up of a plurality of members, for example, two members. Further, the shape of the through hole c3z is not limited to that shown in FIG. 4, and may be, for example, one in which the total number of bent portions is further increased.
ま九以上の実施例では乾燥機が説明され九が、冷風によ
る冷却機に適用してもよい。あるいは単なる流動層に適
用するようにしてもよい。In the above embodiments, a dryer is described, but the present invention may also be applied to a cooler using cold air. Alternatively, it may be applied to a simple fluidized bed.
以上述べたよ5に本発明の整流板によれば、細かい粉や
粒でも下方に落下することなく、その上で空気流により
流動化させることができる。従って、この整流板を用い
る機器や装置の保守が容易となる。As described above, according to the current plate of the present invention, even fine powders and particles can be fluidized by air flow without falling downward. Therefore, maintenance of equipment and equipment using this rectifying plate becomes easy.
第1更は本発明の実施例による整流板を適用した振動7
JorIP4乾燥機の側面図、第2図は第1図における
■−■線方向断面図、第3図は第2図におけるI−1[
1線方向断面囚、第4図は第3図におけるIV−1’V
線方線方向拡大図、第5図は従来の整流板の平面図、第
6図は第5図における■−W線方向断面図及び第7図は
第6図における■−4線方線方向図である。
なお図において、The first example is vibration 7 using a rectifying plate according to an embodiment of the present invention.
A side view of the JorIP4 dryer, Fig. 2 is a sectional view along the line ■-■ in Fig. 1, and Fig. 3 is a cross-sectional view along the line I-1 [in Fig. 2].
1-line direction cross section, Figure 4 is IV-1'V in Figure 3.
5 is a plan view of a conventional rectifier plate, FIG. 6 is a sectional view in the direction of the ■-W line in FIG. 5, and FIG. 7 is an enlarged view in the direction of the ■-4 line in FIG. 6. It is a diagram. In the figure,
Claims (1)
整流して上方に導くようにした整流板において、前記通
孔を屈曲して形成させたことを特徴とする整流板。1. A current plate having a large number of through holes and configured to rectify airflow from below and guide it upward, characterized in that the through holes are formed in a bent manner.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10985685A JPS61268976A (en) | 1985-05-21 | 1985-05-21 | Flow regulating plate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10985685A JPS61268976A (en) | 1985-05-21 | 1985-05-21 | Flow regulating plate |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61268976A true JPS61268976A (en) | 1986-11-28 |
Family
ID=14520924
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10985685A Pending JPS61268976A (en) | 1985-05-21 | 1985-05-21 | Flow regulating plate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61268976A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003040417A (en) * | 2001-07-25 | 2003-02-13 | Tamagawa Machinery Co Ltd | Vibrating process device |
JP2011001218A (en) * | 2009-06-18 | 2011-01-06 | Denki Glass Fiber Kako Kk | Dryer for glass chopped strand and method for manufacturing the same |
JP2011148170A (en) * | 2010-01-21 | 2011-08-04 | Tanaka:Kk | Pellet cooling device |
JP2012206443A (en) * | 2011-03-30 | 2012-10-25 | Tanaka:Kk | Pellet drying apparatus |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5211642A (en) * | 1975-07-17 | 1977-01-28 | Ito Tekkosho:Kk | Method of excretion and filth separation |
-
1985
- 1985-05-21 JP JP10985685A patent/JPS61268976A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5211642A (en) * | 1975-07-17 | 1977-01-28 | Ito Tekkosho:Kk | Method of excretion and filth separation |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003040417A (en) * | 2001-07-25 | 2003-02-13 | Tamagawa Machinery Co Ltd | Vibrating process device |
JP2011001218A (en) * | 2009-06-18 | 2011-01-06 | Denki Glass Fiber Kako Kk | Dryer for glass chopped strand and method for manufacturing the same |
JP2011148170A (en) * | 2010-01-21 | 2011-08-04 | Tanaka:Kk | Pellet cooling device |
JP2012206443A (en) * | 2011-03-30 | 2012-10-25 | Tanaka:Kk | Pellet drying apparatus |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2983051A (en) | Apparatus for cooling particulate materials | |
JPS6071718A (en) | Apparatus and method for performing opening and dust removal of fiber bale | |
US2501487A (en) | Apparatus for treating soap | |
JPS61268976A (en) | Flow regulating plate | |
JP2006511414A (en) | Vibrating conveyor | |
JPH0815587B2 (en) | Vibrating sieve | |
JP6054650B2 (en) | Vibrating feeder | |
CN109140905A (en) | A kind of drying apparatus of vibrating fluidized bed and drying means | |
CA2310749C (en) | Apparatus and process for cooling and de-steaming calcined stucco | |
JPH01189485A (en) | Vibrating dryer provided with heat transfer pipes | |
US4843732A (en) | Vibratory and gas levitation particle treatment system | |
JPS5818072Y2 (en) | Heat exchange device with fins | |
JP2690172B2 (en) | Heat exchange device for powdery particles | |
JP2927632B2 (en) | Particle flow heat exchanger | |
JPS59142370A (en) | Device for heating and drying powdered and granular body | |
JPS59157482A (en) | Heat exchanger using waste gas | |
JPS58220007A (en) | Method of carrying granular solid between two plate | |
CN211876530U (en) | Clean type vibration fluidized bed | |
SU1460550A1 (en) | Utilizer of heat of loose materials | |
CS220702B1 (en) | Vibrofluidous trough | |
JP2659850B2 (en) | Fine powder cooling device | |
US481687A (en) | Malt-drying kiln | |
JPH065491U (en) | Draining boiled small fish, cooling and drying equipment | |
JPS61101238A (en) | Apparatus for heat exchanging between coarse and fine particles | |
JPS6127484A (en) | Device for removing extraneous matter in indirect heating type drier |