JPS59100383A - Drier for superheated steam - Google Patents
Drier for superheated steamInfo
- Publication number
- JPS59100383A JPS59100383A JP21036482A JP21036482A JPS59100383A JP S59100383 A JPS59100383 A JP S59100383A JP 21036482 A JP21036482 A JP 21036482A JP 21036482 A JP21036482 A JP 21036482A JP S59100383 A JPS59100383 A JP S59100383A
- Authority
- JP
- Japan
- Prior art keywords
- drying
- superheated steam
- air
- conveyor
- drying chamber
- 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
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】
本発明は、ネットブンベヤ等の通気性を有する被乾燥物
搬送体が、乾燥室内部を貫通し、又同搬送体に対してL
下方向に過熱水蒸気を吹きつけることにより乾燥を実施
するクイズの過熱水蒸気乾燥装置に於いて、空気混入抑
制装置の設置により乾燥室の搬送休出入口付近より外部
から多量の空気が、同乾燥室内に混入するのを有効に抑
止し得た過熱水蒸気乾燥装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention is characterized in that an air permeable drying object conveyor such as a net bunveyor penetrates the inside of a drying chamber, and
In Quiz's superheated steam drying equipment, which performs drying by blowing superheated steam downward, a large amount of air enters the drying room from the outside near the transportation entrance and exit of the drying room due to the installation of an air mixture suppression device. The present invention relates to a superheated steam drying device that can effectively prevent contamination.
過熱水蒸気乾燥法は、熱風乾燥法等他の乾、操法に比し
、乾燥効率の向上、乾燥品の膨化(多孔質化)聞合の向
上、あるいは均一乾燥が図れる点で大へん有利な乾燥法
であるが、前述した態様の乾燥装置を使用して乾礫を実
施する場合、搬送休出入口付近よυ多量の空気が乾燥室
内に混入し一前記過熱水蒸気乾燥特有の効果を阻害する
ことにも継かった。The superheated steam drying method has great advantages over other drying methods such as hot air drying in that it improves drying efficiency, increases the degree of swelling (porosity) of dried products, and allows for uniform drying. Regarding the drying method, when drying gravel is carried out using the drying apparatus of the above-mentioned aspect, a large amount of air gets mixed into the drying chamber near the transportation entrance and exit, which inhibits the effects peculiar to the superheated steam drying. It was also inherited by
同空気の乾燥室内への混入を抑止する方策としては、搬
送体出入口付近より水蒸気が乾燥室外に噴出する程必要
以上に多量に水蒸気を乾燥室□内に供給することが考え
られるが、これは経済性の面でも問題が有り、加えて乾
燥室外に噴出した水蒸気が、乾燥品表面に結露して乾燥
品の品質低下を招くことにもなる。One possible measure to prevent this air from entering the drying chamber is to supply a larger amount of water vapor than necessary into the drying chamber □, to the extent that the water vapor blows out of the drying chamber near the entrance and exit of the carrier. There is also a problem in terms of economy, and in addition, the water vapor ejected outside the drying chamber condenses on the surface of the dried product, resulting in a deterioration in the quality of the dried product.
又、空気混入抑止手段として、搬送体出入口へのエアー
ロッカーの設置も考えられるが、これは搬送体の運転効
率の而で問題がある。Also, as a means to prevent air from entering the air, it is possible to install an air locker at the entrance and exit of the carrier, but this poses a problem in terms of operating efficiency of the carrier.
このような現状に鑑みて、上記欠陥を有することなく、
しかも乾燥室内への空気の混入を有効に抑制し乍ら過熱
水蒸気乾燥が実施し得る乾燥装置として考案されたのが
、本発明の過熱水蒸気乾燥装置である。In view of this current situation, without having the above defects,
Furthermore, the superheated steam drying device of the present invention has been devised as a drying device that can carry out superheated steam drying while effectively suppressing the intrusion of air into the drying chamber.
以下、添付図面に示す実施例に基づき本発明の詳細な説
明する。Hereinafter, the present invention will be described in detail based on embodiments shown in the accompanying drawings.
図中(la)〜(ld、)は、ネットコンベヤ等の通知
性を有する被乾燥物搬送体(2)が、その中を貫通する
過熱水蒸気乾燥室であり、隔壁(3)により凹室に区画
化されている。In the figure, (la) to (ld,) are superheated steam drying chambers through which a drying material conveyor (2) with notification properties such as a net conveyor passes through, and is connected to a concave chamber by a partition wall (3). It is compartmentalized.
又、同乾燥室内部には、夫々ヒーター(図示せず)及び
プロア=(図示せず)が設置され、さらに同乾燥室には
、各乾燥室ごとに水蒸気が供給されており、各室内は、
被乾燥物搬送体(2)に対し、図示した風向きで過熱水
蒸気が吹きつけられるべく、各室交互に過熱水蒸気が内
部循環している。Additionally, a heater (not shown) and a proa (not shown) are installed inside the drying room, and water vapor is supplied to each drying room. ,
Superheated steam is internally circulated alternately in each chamber so that the superheated steam is blown onto the drying object carrier (2) in the illustrated wind direction.
このような過熱水蒸気吹きっけ方向の反転措置は、被乾
燥物の乾燥ムラを解消する上で有効な措置である。Such a measure of reversing the direction of blowing superheated steam is an effective measure for eliminating uneven drying of the material to be dried.
被乾燥物搬送体(2)の被乾燥物搬送態様は、被乾燥物
をその上に直接を置する方式あるいは、多孔質金属軸の
リテーナ−を搬送体上に装着する方式等何れでもよく、
又同搬送体に沿ってその上方にネットコンベヤ等通気性
を有する搬送体を別途設置し、抑えコンベヤとして作用
させることもでき得る。The method of conveying the material to be dried by the material to be dried (2) may be either a method in which the material to be dried is placed directly on it, or a method in which a porous metal shaft retainer is mounted on the carrier.
Further, a conveyor such as a net conveyor having air permeability may be separately installed along and above the conveyor to function as a restraining conveyor.
次に図中(4)は、乾燥室(la)始端の搬送体入口に
同乾燥室に隣接して設けられた空気混入抑制装置である
。同抑制装置(4)は、図示した如く搬送体(2)が、
その中を貫通する箱型形状を呈しており、さらに隣接す
る乾・操室(la)の風下側、即ち搬送体(2)に対し
てE方側に排気ダクト(5)が連結さ昨、同排気ダクト
(5)は、吸引力調整ダンパー(6)を介して、乾燥室
終端部の空気M人抑制装置からの排気ダクトと合流し、
排気ファン(7)に連結している。Next, (4) in the figure is an air entrainment suppressing device provided adjacent to the drying chamber (la) at the conveyance body entrance at the starting end of the drying chamber (la). As shown in the figure, the suppression device (4)
It has a box-like shape that passes through it, and an exhaust duct (5) is connected to the leeward side of the adjacent drying and handling room (LA), that is, the E side with respect to the carrier (2). The exhaust duct (5) joins the exhaust duct from the air control device at the end of the drying chamber via the suction force adjustment damper (6),
It is connected to an exhaust fan (7).
又、図中(8)も、乾燥室(1cL)終端の搬送体出口
に、同転・顕室と隣接して設けられた、空気混入抑制装
置である。Further, (8) in the figure is also an air entrainment suppressing device installed at the conveyor outlet at the end of the drying chamber (1 cL), adjacent to the co-rotation/concentration chamber.
同抑制装置(8)も又、抑制装置(4)と同様に搬送体
(2)が、その中を貫通する箱型形状を呈しており、又
隣接する乾燥室(1d)の風下側、即ち抑制装置(8)
の場合は、同(4)とは逆に搬送体(2)に対して下方
側に、排気ダクト(9)が連結され、同ダクトは、吸引
力調整ダンパー(6)を介して排気ダクト(5)と合流
して#lI気ファン(7)に継がっている。Similar to the suppression device (4), the suppression device (8) also has a box-like shape through which the conveyor (2) passes, and is located on the leeward side of the adjacent drying chamber (1d), i.e. Suppressor (8)
In this case, contrary to (4), an exhaust duct (9) is connected to the lower side of the conveyor (2), and the duct is connected to the exhaust duct (9) via a suction force adjustment damper (6). It merges with #lIkifan (7) and continues with #lIkifan (7).
次に、本発明の乾燥装置の作用機能を説明する。Next, the functions of the drying device of the present invention will be explained.
実施例の如く、内部循環型で搬送体(2)に対して、上
下方向の風の吹きつけにより乾燥を実施するタイプのr
lE炸室内では、搬送体さらには被乾燥物の存在により
通風が妨げられるため、図示す不如く搬送体で2)に対
して風J: m11が陽匝状飽となり一方風下側は陰圧
状態を早オる。As shown in the example, an internal circulation type r is used which performs drying by blowing wind in the vertical direction on the conveyor (2).
In the 1E explosion chamber, ventilation is obstructed by the presence of the conveyor and the material to be dried, so the wind J: m11 becomes positive and swollen with respect to 2) on the conveyor as shown in the figure, while the leeward side is in a negative pressure state. I fall early.
さらに、本発明の空気混入抑制装置(4)及び(8)は
、隣接する乾燥器の風下側に排気ダクト(5)、(9)
及び排気ファン(7)よりなる強制的な排気機構を有し
ており、同排り、ファン(7)の稼動によって、搬送体
(2)の存在により、隣接するlfI、’ m室(la
)、(Id )と同搬送体に対して同様な圧力分布が
呈される。Furthermore, the air entrainment suppression devices (4) and (8) of the present invention have exhaust ducts (5) and (9) on the leeward side of the adjacent dryers.
The system has a forced exhaust mechanism consisting of an exhaust fan (7) and an exhaust fan (7).
), (Id ) and the same pressure distribution is exhibited for the same carrier.
従って、搬送体(2)のト方あるいは下方に於いて、乾
燥室の搬送休出入口付近を通じての空気あるいは過熱水
蒸気の移動が生じず、その結果空気混入抑制装置(4)
及び(8)内に同装置の搬送休出入口付近を介して混入
した空気は、乾燥室内に混入することなく、排気ダク日
5)、(9)を介して排出される。Therefore, there is no movement of air or superheated steam through the vicinity of the transport entrance and exit of the drying chamber in the upper or lower part of the transport body (2), and as a result, the air entrainment suppression device (4)
The air that has entered (8) through the vicinity of the transport entrance and exit of the apparatus is discharged through the exhaust ducts 5) and (9) without entering the drying chamber.
さらに乾燥室内の過熱水蒸気の同抑制装置(4)、(8
)への漏洩排出は最小限に抑止し得、エネルギーロスを
生じないと共に、過熱水蒸気の外部への漏洩は起こらな
い。Furthermore, the same suppression device for superheated steam in the drying room (4), (8)
) can be suppressed to a minimum, energy loss does not occur, and superheated steam does not leak to the outside.
又、吸引力調整ダンパー(6)は、排気ファン(7)に
よる吸引力を調整するための装置であり、被乾燥物の種
類によっては、過熱水蒸気乾燥の際に少量の空気混入を
行うことが、被@j:燥物の変形防市上却って好ましい
ケースがあり、このような場合には、同調整グンバー(
6)を操作して、吸引力を低減し所定量の空気を敢えて
乾燥室内に混入することも可能、である。The suction power adjustment damper (6) is a device for adjusting the suction power of the exhaust fan (7), and depending on the type of material to be dried, a small amount of air may be mixed in during superheated steam drying. , @j: There are cases where it is preferable to prevent the deformation of dry goods, and in such cases, the same adjustment gunbar (
6), it is also possible to reduce the suction force and intentionally mix a predetermined amount of air into the drying chamber.
これに対し、第2図対照例に示す如く、空気混入抑制装
置の排気ダクトを隣接する乾燥室の田土側に連結した乾
燥装置の場合は、搬送体(2)を介しての子方分布が、
乾燥室内と抑制装置内に於いて正反対のものとなり、そ
の結果矢印で示したように、同抑制装置の搬送体出入口
の搬送体り方より混入した空気が搬送体に沿って多量に
乾燥室内に混入すると共に、乾燥室内の過熱水蒸気も抑
制装置内に多量に流出し、排気パルプを介して排出され
エネルギーロスを生じることにもなる。On the other hand, as shown in the comparative example in Figure 2, in the case of a drying device in which the exhaust duct of the air entrainment suppression device is connected to the rice field side of the adjacent drying room, the distribution of children through the conveyor (2) is ,
The drying chamber and the inside of the suppressor are completely opposite, and as a result, as shown by the arrow, a large amount of air enters the drying chamber along the conveyor at the entrance and exit of the suppressor. In addition to being mixed in, a large amount of superheated steam in the drying chamber also flows into the suppression device and is discharged through the exhaust pulp, resulting in energy loss.
以上本発明の過熱水蒸気乾燥装置は、空気混入抑制装置
の設置により、過熱水蒸気乾燥室内への外部からの多量
の空気混入を、何らエネルギーロスや搬送体の運行効率
の低下を生じることなく有効に抑市し得、以って満足の
いく過熱水蒸気乾燥を実施することが回船、となり、同
叫燥法の有するメリットを最大限に発揮し得る。As described above, the superheated steam drying apparatus of the present invention effectively prevents a large amount of air from entering the superheated steam drying chamber from outside by installing the air entrainment suppressing device without causing any energy loss or reduction in the operating efficiency of the conveyor. It is possible to carry out superheated steam drying that can be carried out satisfactorily, and the advantages of the same drying method can be maximized.
第1図は、本発明実施例の概略横断面図である。 第2図は、対照側の一部切欠概略横断面図である。 FIG. 1 is a schematic cross-sectional view of an embodiment of the present invention. FIG. 2 is a partially cutaway schematic cross-sectional view of the opposite side.
Claims (1)
して、上下方向の過熱水蒸気の吹きつけにより乾燥を実
施する乾燥装置の同搬送体出入口に、隣接する乾燥室の
風下側に強制的な排気機構を有し、さらに同搬送体がそ
の中を貫通する箱型形状の空気混入抑制装置を設けたこ
とを特徴とする過熱水魚気乾・咲装置。A drying device that performs drying by blowing superheated steam vertically onto a conveyor to be dried that has air permeability through the drying chamber.At the entrance and exit of the conveyor, there is a 1. A superheated fish air-drying and blooming device, characterized in that it has an exhaust mechanism and is further provided with a box-shaped air mixture suppression device through which the conveying body passes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21036482A JPS59100383A (en) | 1982-11-30 | 1982-11-30 | Drier for superheated steam |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21036482A JPS59100383A (en) | 1982-11-30 | 1982-11-30 | Drier for superheated steam |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59100383A true JPS59100383A (en) | 1984-06-09 |
JPH0517471B2 JPH0517471B2 (en) | 1993-03-09 |
Family
ID=16588140
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21036482A Granted JPS59100383A (en) | 1982-11-30 | 1982-11-30 | Drier for superheated steam |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59100383A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4816188U (en) * | 1971-07-02 | 1973-02-23 | ||
JPS4916051A (en) * | 1972-06-06 | 1974-02-13 | ||
JPS5032470A (en) * | 1973-07-30 | 1975-03-29 |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4816188B1 (en) * | 1970-08-27 | 1973-05-19 |
-
1982
- 1982-11-30 JP JP21036482A patent/JPS59100383A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4816188U (en) * | 1971-07-02 | 1973-02-23 | ||
JPS4916051A (en) * | 1972-06-06 | 1974-02-13 | ||
JPS5032470A (en) * | 1973-07-30 | 1975-03-29 |
Also Published As
Publication number | Publication date |
---|---|
JPH0517471B2 (en) | 1993-03-09 |
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