JPS6033235B2 - Reduced pressure equilibrium forced rotation convection heating drying method and its equipment - Google Patents

Reduced pressure equilibrium forced rotation convection heating drying method and its equipment

Info

Publication number
JPS6033235B2
JPS6033235B2 JP56022171A JP2217181A JPS6033235B2 JP S6033235 B2 JPS6033235 B2 JP S6033235B2 JP 56022171 A JP56022171 A JP 56022171A JP 2217181 A JP2217181 A JP 2217181A JP S6033235 B2 JPS6033235 B2 JP S6033235B2
Authority
JP
Japan
Prior art keywords
hollow chamber
convection
rotating body
air
action
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
Application number
JP56022171A
Other languages
Japanese (ja)
Other versions
JPS57139271A (en
Inventor
信義 久保山
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP56022171A priority Critical patent/JPS6033235B2/en
Priority to NO820387A priority patent/NO154934C/en
Priority to SE8200763A priority patent/SE450912B/en
Priority to AU80426/82A priority patent/AU546475B2/en
Priority to FR8202315A priority patent/FR2500131B1/en
Priority to NZ199731A priority patent/NZ199731A/en
Priority to BE6/47604A priority patent/BE892149A/en
Priority to CH923/82A priority patent/CH648112A5/en
Priority to US06/349,064 priority patent/US4426793A/en
Priority to CA000396388A priority patent/CA1176524A/en
Priority to NL8200625A priority patent/NL8200625A/en
Priority to BR8200871A priority patent/BR8200871A/en
Priority to AR288450A priority patent/AR231879A1/en
Priority to DE3205845A priority patent/DE3205845C2/en
Priority to ZA821069A priority patent/ZA821069B/en
Priority to GB82044757A priority patent/GB2094964B/en
Priority to IT19727/82A priority patent/IT1153435B/en
Priority to ES509768A priority patent/ES509768A0/en
Priority to KR8200729A priority patent/KR870001831B1/en
Publication of JPS57139271A publication Critical patent/JPS57139271A/en
Priority to ES519792A priority patent/ES8405502A1/en
Publication of JPS6033235B2 publication Critical patent/JPS6033235B2/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00Drying solid materials or objects by processes not involving the application of heat
    • F26B5/04Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24VCOLLECTION, PRODUCTION OR USE OF HEAT NOT OTHERWISE PROVIDED FOR
    • F24V40/00Production or use of heat resulting from internal friction of moving fluids or from friction between fluids and moving bodies
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/02Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Molecular Biology (AREA)
  • Drying Of Solid Materials (AREA)

Description

【発明の詳細な説明】 この発明は密閉された中空室内の空気を回転体の回転に
より強制的に吸引して排気する減圧作用と、空気と回転
体との摩擦作用により発生する摩擦熱の発熱作用と、旋
回対流作用と、さらには外気の導入作用とによって被乾
燥物を有効に乾燥するようにした減圧平衡加熱乾燥方法
およびその装置に於て、中空室内の加熱気流を均一な温
度分布の下に有効に旋回対流させて被乾燥物を迅速かつ
高品質を保って乾燥できるようにした減圧平衡強制旋回
対流加熱乾燥方法およびその装置に関する。
Detailed Description of the Invention This invention utilizes a depressurizing action that forcibly sucks and exhausts the air in a sealed hollow chamber through the rotation of a rotating body, and heat generation of frictional heat generated by the friction between the air and the rotating body. In the reduced pressure equilibrium heating drying method and its device, which effectively dries the material to be dried by the effect of convection, swirling convection, and the effect of introducing outside air, the heated airflow in the hollow chamber is controlled to have a uniform temperature distribution. The present invention relates to a reduced-pressure equilibrium forced swirling convection heating drying method and an apparatus therefor, which enables effective swirling convection to dry a material to be dried quickly and with high quality.

本出願人は、さきに密閉された中空室内の空気を回転体
の回転により強制的に吸引して排気する減圧効果と、空
気と回転体との摩擦作用により発生する摩擦熱の加熱効
果とにより石油、ガスまたは電気ヒーターなどの既存の
熱源を用いない新しい減圧平衡加熱方法および装置を開
発した。
The applicant has previously proposed a system that uses the depressurizing effect of forcibly sucking and exhausting the air in the sealed hollow chamber by the rotation of the rotating body, and the heating effect of frictional heat generated by the friction between the air and the rotating body. We have developed a new vacuum equilibrium heating method and device that does not use existing heat sources such as oil, gas or electric heaters.

この発明は上述の発明を基本とし、かつ上述の発明を利
用して成されたもので中空室内の空気流を強制的に旋回
対流させて温度分布が均一で乾燥効果の顕著な新規な減
圧平衡旋回対流加熱乾燥方法およびその装置を提供する
にある。以下にこの発明の一実施例を図面に示される構
成について詳述する。
This invention is based on the above-mentioned invention and has been made by utilizing the above-mentioned invention, and is a novel depressurized equilibrium that has a uniform temperature distribution and a remarkable drying effect by forcibly swirling and convecting the air flow in a hollow chamber. The present invention provides a swirling convection heating drying method and an apparatus therefor. An embodiment of the present invention will be described below in detail with reference to the configuration shown in the drawings.

1は扉2,2を枢着して観音開き構造とした角筒状の密
閉された中空室で、上下左右の外周壁には断熱材3の被
着介在させて保温できるようになっている。
Reference numeral 1 denotes a rectangular cylindrical sealed hollow chamber with doors 2, 2 pivotally connected to form a double-opening structure, and heat insulating material 3 is interposed on the upper, lower, left, and right outer circumferential walls to keep the room warm.

4は中空室1の天井中央に開□した吸引口で、回転体a
を回転自在に配設した減圧摩擦熱発生機構×を有する。
4 is a suction port opened in the center of the ceiling of hollow chamber 1, and the rotating body a
It has a decompression friction heat generation mechanism x which is rotatably arranged.

そして、この回転体aは図示にあっては、電動機5によ
り回転されるプロペラファン、シロッコフアンなどの回
転羽根6によって構成された所望の傾斜角度を有しかつ
、中空室1内の空気を吸引排気するように回転方向が定
められている。そして、この回転体aの回転領域には摩
擦熱発生部Aが形成される。7は前記減圧摩擦熱発生機
構Xの回転体aに僅かの間隔を置いて対設した回転翼車
で、該回転翼車7と一体で回転する吸引羽根8とにより
従動回転機構Yを構成している。
As shown in the figure, the rotating body a has a desired inclination angle and is configured by rotary blades 6 such as a propeller fan or a sirocco fan rotated by an electric motor 5, and sucks air in the hollow chamber 1. The direction of rotation is determined to exhaust air. A frictional heat generating portion A is formed in the rotating region of the rotating body a. Reference numeral 7 denotes a rotary impeller disposed opposite to the rotating body a of the decompression frictional heat generating mechanism X with a slight interval therebetween, and a driven rotation mechanism Y is constituted by the rotary impeller 7 and a suction blade 8 that rotates integrally with the rotary impeller 7. ing.

すなわち、吸引口4の下端に、臨設されて固定される直
交した支持枠9を取付け談枠9の中心を回転体aの中心
と一致させて軸受部10となしこの軸受部10の上方に
は前記回転翼車7を、また下方には前記吸引羽根8を軸
杵11に螺合固定して一体回転できる構成としている。
That is, an orthogonal support frame 9 is temporarily installed and fixed at the lower end of the suction port 4, and the center of the support frame 9 is aligned with the center of the rotating body a to form a bearing part 10. The rotary impeller 7 and the suction blades 8 below are screwed and fixed to the shaft punch 11 so that they can rotate together.

また、回転翼車7は吸引口4の口径より僅かに小径のり
ング12とそのリング12の外周に突出した多数の羽根
13とによって構成され、吸引口4の内壁とりング12
と羽根13とにより囲経される多数の気室14が形成で
きるようになっている。15は羽根13の上端を梢々斜
方向に曲折した折曲部で、回転性能を高められるように
構成している。
The rotary impeller 7 is composed of a ring 12 with a diameter slightly smaller than the diameter of the suction port 4 and a large number of blades 13 protruding from the outer periphery of the ring 12.
A large number of air chambers 14 surrounded by the blades 13 can be formed. Reference numeral 15 denotes a bent portion in which the upper end of the blade 13 is bent obliquely from top to bottom, and is configured to improve rotational performance.

16は中○取付部17を支持する四本の支村、18はリ
ング12の内側に散設した吸引羽根で、下方の気流を吸
上げできるように同じ方向の傾斜角度を保って取付けら
れている。
16 are four branches that support the middle mounting part 17, and 18 are suction blades scattered inside the ring 12, which are installed with the same angle of inclination in the same direction so as to suck up the downward airflow. There is.

さらに、回転羽根8は、通常のファン構造でよく、中空
室1内の空気を上方に吸上げる方向に羽根8が回転する
ように構成してあればよい。
Furthermore, the rotary blades 8 may have a normal fan structure, as long as the blades 8 are configured to rotate in a direction that sucks up the air in the hollow chamber 1 upward.

なお、また回転羽根8の外方には前記支持枠9の両端を
支持できる環状部19aを有する陣笠状の傾斜板19が
固定してあり、回転羽根8の吸引領域を劃然と規制して
ある。なお、図示しないが、この傾斜板19を回転羽根
8と同様に軸村11に回転可能に固定しこの傾斜板19
の下面にファン機能を呈する傾斜した羽根を取付けて前
記したと同様に吸引効果と吸引領域とを劃然と規制して
実施しても差支えない。
Additionally, a cap-shaped inclined plate 19 having an annular portion 19a that can support both ends of the support frame 9 is fixed to the outside of the rotary blade 8, and it suddenly restricts the suction area of the rotary blade 8. be. Although not shown, this inclined plate 19 is rotatably fixed to the shaft village 11 in the same way as the rotary blade 8.
It is also possible to install slanted blades exhibiting a fan function on the lower surface of the fan to dramatically restrict the suction effect and suction area in the same manner as described above.

20は強制旋回対流案肉機構Zを構成する吸引口4より
下向きに拡開させた円錐状の案内板で、前記傾斜板19
との間で旋回流が形成される。
Reference numeral 20 denotes a conical guide plate that expands downward from the suction port 4 constituting the forced swirl convection guide mechanism Z, and is similar to the inclined plate 19.
A swirling flow is formed between the two.

21は旋回流の流れ方向を規制する規制板で傾斜板19
上に起立させてありかつ両板19,20の間に四個配設
してある。
21 is a regulating plate that regulates the flow direction of the swirling flow; an inclined plate 19;
Four of them are arranged vertically upward and between both plates 19 and 20.

22は電動機5の支持筒で、排気通路23を有し、この
支持筒22の閉口端には消音筒24を備える。
Reference numeral 22 denotes a support cylinder for the electric motor 5, which has an exhaust passage 23, and a silencer cylinder 24 at the closed end of the support cylinder 22.

25は中空室1の下部に配設した外気導入機構で、必要
に応じて補助ヒータを内蔵し、加熱初期の際の昇温効果
を高めるために用いたりさらにはサーモタットなどによ
り温度制御することもある。
Reference numeral 25 denotes an outside air introduction mechanism located at the bottom of the hollow chamber 1. If necessary, an auxiliary heater is built in, and it can be used to enhance the temperature raising effect at the initial stage of heating, or it can also be used to control the temperature with a thermostat or the like. be.

さらにまた、前記外気導入機構25には、その途中に調
節バルブ26を設け手動または室内の温度または室内外
の圧力差を検知して自動的に操作してバルブを開閉でき
るような自動制御弁としても利用できる。27は中空室
1内に多段に配設した網、板などの棚で、被乾燥物の種
類、大きさに応じて上下の棚の間隔、棚の形状を自由に
変えることができ、通気乾燥効果を有効に行わせるもの
である。
Furthermore, the outside air introduction mechanism 25 is provided with a control valve 26 in the middle thereof, and can be used as an automatic control valve that can be operated manually or automatically by detecting the indoor temperature or the pressure difference between the indoor and outdoor. Also available. Reference numeral 27 is a shelf made of nets, boards, etc. arranged in multiple stages inside the hollow chamber 1, and the interval between the upper and lower shelves and the shape of the shelf can be freely changed depending on the type and size of the material to be dried, allowing ventilation drying. This is to make the effect effective.

28はのぞき窓、29は各種計器および制御盤を備えた
コントロールボックスである。
28 is a peephole, and 29 is a control box equipped with various instruments and a control panel.

叙上の構成に基づいて、この発明の作用、方法を説明す
る。
The operation and method of this invention will be explained based on the above configuration.

まず、電動機5に通電し、回転羽根6を回転させれば、
減圧摩擦熱発生機構×が働き密閉された中空室1内の空
気は回転羽根6の吸引排気作用によって、次第に排気減
圧され中空室1の内外に圧力差が次第に大きくなるが、
或る圧力差に達した時点で略平衡状態を維持する。
First, if the electric motor 5 is energized and the rotary blade 6 is rotated,
The decompression frictional heat generation mechanism × operates, and the air in the sealed hollow chamber 1 is gradually exhausted and depressurized by the suction and exhaust action of the rotary vanes 6, and the pressure difference between the inside and outside of the hollow chamber 1 gradually increases.
When a certain pressure difference is reached, an approximately equilibrium state is maintained.

この略−定の平衡状態における中空室1の内外の圧力差
は、回転羽根6の回転吸引力の大きさと吸引口4と回転
羽根6との間隙の大きさなどによって定まるが、この平
衡状態は回転羽根6の回転作用が継続する限り維持され
る。この平衡状態では回転羽根6の回転領域内にある摩
擦熱発生部Aにおいて空気の滞留現象が生じ、回転羽根
6との摩擦作用が反覆継続するので、摩擦熱が発生して
次第にその温度が上昇する。ところで、減圧摩擦熱発生
機構×に相対して従動回転機構Yが設けられており、回
転体aすなわち回転羽根6によって回転される加熱され
た旋回流は流体の粘性効果により、離開しているこの従
動回転機構Yの回転翼車7を同一方向に回転させるよう
に働かせるので回転翼車7のリング12と羽根13と吸
引口4の内壁とで囲経される気室14内の気体を強制的
に旋回させること)なる。
The pressure difference between the inside and outside of the hollow chamber 1 in this approximately constant equilibrium state is determined by the magnitude of the rotational suction force of the rotary blade 6 and the size of the gap between the suction port 4 and the rotary blade 6. This is maintained as long as the rotating action of the rotating blade 6 continues. In this equilibrium state, a phenomenon of air stagnation occurs in the frictional heat generating part A within the rotation area of the rotating blade 6, and the frictional action with the rotating blade 6 continues to be repeated, so frictional heat is generated and the temperature gradually rises. do. By the way, a driven rotation mechanism Y is provided opposite to the decompression friction heat generation mechanism Since the rotary impeller 7 of the driven rotation mechanism Y is operated to rotate in the same direction, the gas in the air chamber 14 surrounded by the ring 12 of the rotary impeller 7, the blades 13, and the inner wall of the suction port 4 is forced. to rotate).

この強制的に旋回作用を受ける気室14内の加熱気流は
、強制旋回対流案内機構Zにより案内板20と傾斜板1
9とで形成される空間部に、規制板21によって旋回流
を附勢されながら導入されさらに中空室1の外周内壁に
向って吐出されるものである。一方、従動回転機構Yは
回転翼車7の回転により一体回転する回転羽根8の作用
で該回転羽根8の下方に位置する気流は強制的に上方に
吸引されリング12の吸引羽根18の吸上効果と相換っ
て減圧摩擦熱発生機構Xの回転羽根6の摩擦熱発生部A
に強制的に送り込まれ該部で既に昇温した気流と入れ替
わりながら回転翼車7によって前述のように下方に旋回
流を形成して吐出されるものである。したがって、従動
回転機構Yと強制旋回対流案内機構Zの働きにより中空
室1内の気流は、外周方向から下降し中央部分から上昇
する強制的な対流作用と、渦巻状の旋回作用(渦巻作用
とも認められる)とを奏することができる。
The heated airflow in the air chamber 14 subjected to this forced swirling action is transferred to the guide plate 20 and the inclined plate 1 by the forced swirling convection guide mechanism Z.
The swirling flow is introduced into the space formed by the regulating plate 21 and is further discharged toward the outer peripheral inner wall of the hollow chamber 1. On the other hand, in the driven rotation mechanism Y, the airflow located below the rotary vane 8 is forcibly sucked upward by the action of the rotary vane 8 which rotates integrally with the rotation of the rotary impeller 7, and is sucked up by the suction vane 18 of the ring 12. In exchange for the effect, the frictional heat generating portion A of the rotating blade 6 of the decompression frictional heat generating mechanism X
The air is forcibly fed into the air, where it replaces the airflow whose temperature has already risen, and is discharged by the rotary impeller 7 forming a swirling airflow downward as described above. Therefore, due to the effects of the driven rotation mechanism Y and the forced swirling convection guide mechanism Z, the airflow in the hollow chamber 1 is caused by a forced convection action that descends from the outer circumferential direction and rises from the center, and a spiral swirling action (also known as a spiral action). (recognized).

このように中空室1内の空気圧が回転羽根6の回転によ
る減圧作用を受けた状態において、旋回する気流を外周
方向から下降させ一旦下降した後中空室1の下部外周よ
り中心側に向って移行する気流の対流作用を強制的に生
起させているので、室1内の温度を所望の設定された温
度に急速に均一化できる。
In this manner, when the air pressure in the hollow chamber 1 is subjected to the depressurizing effect due to the rotation of the rotary vane 6, the swirling airflow is lowered from the outer circumferential direction, and after once descending, it moves from the lower outer circumference of the hollow chamber 1 toward the center. Since the convection action of the air current is forcibly generated, the temperature inside the chamber 1 can be uniformized rapidly to a desired set temperature.

しかも、対流する加溢された気流は多段に配設された棚
27内に均一に侵入して作用し全体を減圧加熱して乾燥
させる。気化した水分は、吸引口4を経て外部に排出さ
れるが必要に応じて外気導入機構25の調節バルブ26
を操作して外気を導入すれば外気は中空室1内に送給さ
れその送給空気に相当する気化水分は排出されて有効な
乾燥作用が行われる。したがって、中空室1内の棚27
上の被乾燥物は減圧作用、旋回対流作用による被乾燥物
の含有水分の遊離性が高められ、かつ室温の上昇による
被乾燥物への加熱作用により被乾燥物の遊離性水分の発
散を促がすと共に加熱された外気の導入による気化蒸発
分の有効な排気作用によって中空室1の全域の被乾燥物
を濁に短時間高能率で乾燥させることができる。
In addition, the convecting and overflowing air current uniformly enters and acts on the shelves 27 arranged in multiple stages, thereby heating and drying the entire area under reduced pressure. The vaporized moisture is discharged to the outside through the suction port 4, but if necessary, the control valve 26 of the outside air introduction mechanism 25
When outside air is introduced by operating the , the outside air is fed into the hollow chamber 1, and the vaporized moisture corresponding to the fed air is discharged to perform an effective drying action. Therefore, the shelf 27 in the hollow chamber 1
The moisture contained in the drying material above is increased due to the reduced pressure effect and the swirling convection effect, and the release of free moisture from the drying material is promoted by the heating effect on the drying material due to the rise in room temperature. Due to the effective evacuation of the vaporized and evaporated components by the introduction of heated outside air, the material to be dried in the entire area of the hollow chamber 1 can be dried in a short period of time and with high efficiency.

ことに旋回対流作用によって気流は中空室1の全域の棚
27に作用し、しかも、温度分布が均一となると共に外
気の間歌的な導入を行うことにより乾燥効果がより促進
され、ことに色彩の変色なく原色をとゞめた美麗な乾燥
物を得ることができる。
In particular, the airflow acts on the shelves 27 throughout the hollow chamber 1 due to the swirling convection effect, and the temperature distribution becomes uniform and the drying effect is further promoted by introducing outside air in a continuous manner. It is possible to obtain a beautiful dried product that retains its primary color without any discoloration.

また、中空室1は図示では立方体形状であるがこの形状
は何等特定されるものでなく円筒構造であっても良いこ
とは勿論である。
Further, although the hollow chamber 1 is shown to have a cubic shape, this shape is not particularly limited, and it goes without saying that it may have a cylindrical structure.

なお、図示のように立方体形状の場合はその四周の四隅
部に屈曲面を形成して旋回層流の流れ抵抗を逓減させる
こともある。この発明は叙上のように、回転体の回転作
用によって密閉された中空室内の空気を吸引排気し、中
空室を減圧状態に保ち、しかも室内外の圧力差を略一定
の平衡状態において回転体の回転作用を継続させて回転
体と空気との摩擦作用によって摩擦熱を発生させると共
に、この摩擦熱を有する気体を従動回転機構と強制旋回
対流案内機構とによって有効な旋回渦巻作用と対流作用
を自然に生起させるようにし、しかも所望の乾燥操作の
後外気導入機構の働きで加熱されまたは加熱されない外
気を送給して被乾燥物を有効に乾燥しているので乾燥効
果が格段と向上し、しかも高品質の乾燥物を得ることが
できるしかも、従来のようなヒータとか燃料などのよう
な直接的な熱源の使用を省き、回転体の回転摩擦作用、
減圧作用、旋回渦巻流による対流作用によって有効な乾
燥作用を行わせ、あらゆる種類の乾燥作用に有効に実施
できる特徴を有する。
In the case of a cubic shape as shown in the figure, curved surfaces may be formed at the four corners of the four circumferences to gradually reduce the flow resistance of the swirling laminar flow. As described above, this invention suctions and exhausts the air in a sealed hollow chamber by the rotational action of a rotating body, maintains the hollow chamber in a reduced pressure state, and maintains the pressure difference between the inside and outside in a substantially constant equilibrium state. The rotating action of the rotating body is continued to generate frictional heat due to the frictional action between the rotating body and the air, and the gas having this frictional heat is subjected to effective swirling action and convection action using a driven rotation mechanism and a forced swirling convection guide mechanism. After the desired drying operation, heated or unheated outside air is supplied by the outside air introduction mechanism to effectively dry the object, so the drying effect is greatly improved. Moreover, it is possible to obtain high-quality dried products, and it eliminates the use of conventional direct heat sources such as heaters and fuel.
It performs an effective drying action through a decompression action and a convection action due to swirling swirl, and has the feature that it can be effectively used for all types of drying actions.

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

図は、この発明に係る減圧平衡旋回対流加熱乾燥装置の
一実施例を示すもので、第1図は全体の一部切欠正面図
、第2図は同上要部の拡大断面図、第3図は回転翼車の
拡大平面図、第4図は拡大側面図、第5図は第3図のV
−V線断面図、第6図は従動回転機構の支持枠と傾斜板
との関係を示す拡大平面図、第7図は同上の肌一肌線断
面図、第8図は傾斜板だけの平面図、第9図は同上正面
図である。 1・・・・・・密閉された中空室、4・・・・・・減圧
摩擦熱発生機構×の吸引口、7・・・・・・従動回転機
構Yの回転翼車、8・…・・回転羽根、12・・・・・
・リンク、18..・・・・吸引羽根、19・・・・・
・陣笠状の傾斜板、20・・・・・・強制旋回対流案内
機構Zの案内板、21・・・・・・規制板、a・・…・
回転体を示し、電動機5と回転羽根6で構成される、A
…・・・摩擦熱発生部。 第1図 第3図 第4図 第5図 第7図 図 N 滋 図 〇 糠 第6図 第8図
The figures show an embodiment of the depressurized balanced swirl convection heating drying apparatus according to the present invention, in which Fig. 1 is a partially cutaway front view of the whole, Fig. 2 is an enlarged sectional view of the main part of the same, and Fig. 3 is an enlarged plan view of the rotary impeller, Fig. 4 is an enlarged side view, and Fig. 5 is the V of Fig. 3.
-V line sectional view, Fig. 6 is an enlarged plan view showing the relationship between the support frame of the driven rotation mechanism and the inclined plate, Fig. 7 is a skin-to-skin sectional view of the same as above, and Fig. 8 is a plane of only the inclined plate. FIG. 9 is a front view of the same as above. 1... Sealed hollow chamber, 4... Suction port of reduced pressure friction heat generation mechanism X, 7... Rotary impeller of driven rotation mechanism Y, 8...・Rotating blade, 12...
・Link, 18. .. ...Suction blade, 19...
- Shape-shaped inclined plate, 20...Guide plate of forced rotation convection guide mechanism Z, 21...Regulation plate, a...
A shows a rotating body and is composed of an electric motor 5 and a rotating blade 6.
...Frictional heat generating part. Figure 1 Figure 3 Figure 4 Figure 5 Figure 7 Figure N Shigeru Figure 6 Figure 8

Claims (1)

【特許請求の範囲】 1 密閉された中空室内の空気を、回転体の回転作用に
より強制吸引して室外に排気させ、室内を減圧して室内
外の圧力差を略一定の平衡状態に保つと共に、この平衡
状態を維持しながら、前記回転体の回転作用を継続させ
て空気との摩擦作用を促進して摩擦熱を発生させ、この
摩擦熱を有する気流を前記回転体を中心とする旋回流と
して生起させ、中空室内の気体を回転体の中心下方より
吸引し、中空室の四周に向つて渦流状に拡散下降する強
制旋回対流を発生して中空室内の被乾燥物を加熱すると
共に必要に応じて外気を導入して気化水分を排出して被
乾燥物を乾燥するようにした減圧平衡旋回対流加熱乾燥
方法。 2 被乾燥物を収納する密閉された中空室に、回転体に
よる減圧摩擦熱発生機構と外気導入機構とを設け、中空
室内を減圧平衡状態で加熱すると共に、該減圧摩擦熱発
生機構の回転体に対抗した位置に従動回転機構を設け、
さらに強制旋回対流案内機構を設けてなる減圧平衡旋回
対流加熱乾燥装置。
[Scope of Claims] 1. The air in the sealed hollow chamber is forcibly sucked by the rotating action of a rotating body and exhausted to the outside, thereby reducing the pressure in the room and keeping the pressure difference between the inside and outside in a substantially constant equilibrium state. While maintaining this equilibrium state, the rotating action of the rotating body is continued to promote frictional action with the air to generate frictional heat, and the airflow having this frictional heat is transformed into a swirling flow around the rotating body. The gas in the hollow chamber is sucked from below the center of the rotating body, and a forced swirling convection is generated that diffuses and descends in a vortex shape toward the four circumferences of the hollow chamber, thereby heating the material to be dried in the hollow chamber and as needed. A vacuum-equilibrium swirl convection heating drying method that dries the material to be dried by introducing outside air and discharging vaporized moisture. 2 A vacuum friction heat generation mechanism and an outside air introduction mechanism using a rotary body are provided in a sealed hollow chamber that stores the material to be dried, and the hollow chamber is heated in a vacuum equilibrium state, and the rotor of the vacuum friction heat generation mechanism is heated. A driven rotation mechanism is provided at a position opposite to the
The decompression balanced swirl convection heating drying device is further provided with a forced swirl convection guide mechanism.
JP56022171A 1981-02-19 1981-02-19 Reduced pressure equilibrium forced rotation convection heating drying method and its equipment Expired JPS6033235B2 (en)

Priority Applications (20)

Application Number Priority Date Filing Date Title
JP56022171A JPS6033235B2 (en) 1981-02-19 1981-02-19 Reduced pressure equilibrium forced rotation convection heating drying method and its equipment
NO820387A NO154934C (en) 1981-02-19 1982-02-10 HEATING INSTALLATION FOR A GAS FORM MEDIUM, SPECIFICALLY DRYING SYSTEM.
SE8200763A SE450912B (en) 1981-02-19 1982-02-10 PROCEDURE AND APPARATUS FOR ASTADCOM AIR CIRCULATION AND CONVECTION IN A HEATING BEACH
AU80426/82A AU546475B2 (en) 1981-02-19 1982-02-12 Air circulation and convection in a heat-generating system
FR8202315A FR2500131B1 (en) 1981-02-19 1982-02-12 METHOD FOR GENERATING AIR CIRCULATION AND CONVECTION IN A HEATING SYSTEM, AND DEVICE FOR IMPLEMENTING IT
NZ199731A NZ199731A (en) 1981-02-19 1982-02-15 Dryer with"friction heat"generating means:air circulation system
BE6/47604A BE892149A (en) 1981-02-19 1982-02-15 METHOD FOR GENERATING AIR CIRCULATION AND CONVECTION IN A HEATING INSTALLATION, AND DEVICE FOR IMPLEMENTING SAME
CH923/82A CH648112A5 (en) 1981-02-19 1982-02-15 METHOD FOR GENERATING AIR CIRCULATION AND CONVECTION IN A HEATING SYSTEM, AND DEVICE FOR IMPLEMENTING IT.
US06/349,064 US4426793A (en) 1981-02-19 1982-02-16 Heat generating apparatus and its process utilizing air circulation and convection
CA000396388A CA1176524A (en) 1981-02-19 1982-02-16 Process for causing air circulation and convection in a heat generating system, and its apparatus
BR8200871A BR8200871A (en) 1981-02-19 1982-02-17 PROCESS AND APPLIANCE TO CAUSE AIR CIRCULATION AND CONVENTION IN A HEAT GENERATOR SYSTEM
NL8200625A NL8200625A (en) 1981-02-19 1982-02-17 DEVICE FOR GENERATING HOT AIR CIRCULATION CONVECTION.
AR288450A AR231879A1 (en) 1981-02-19 1982-02-17 PROCEDURE TO PRODUCE THE CIRCULATION AND CONVENTION OF AIR IN A HEAT GENERATING DISPOSITION AND THE APPARATUS TO PERFORM IT
DE3205845A DE3205845C2 (en) 1981-02-19 1982-02-18 Device for heating a gaseous medium, in particular a drying device
ZA821069A ZA821069B (en) 1981-02-19 1982-02-18 Process for causing air circulation and convection in a heat generating system,and apparatus therefor
GB82044757A GB2094964B (en) 1981-02-19 1982-02-18 Air circulation in aheat generating system
IT19727/82A IT1153435B (en) 1981-02-19 1982-02-18 METHOD AND EQUIPMENT FOR AIR CIRCULATION AND CONVECTION IN A HEAT GENERATING SYSTEM
ES509768A ES509768A0 (en) 1981-02-19 1982-02-19 PROCEDURE TO CAUSE THE CIRCULATION AND CONVECTION OF AIR FOR DRYING AND HEATING APPLICATIONS
KR8200729A KR870001831B1 (en) 1981-02-19 1982-02-19 Heat generation apparatus and its process utilizing air circulation and convection
ES519792A ES8405502A1 (en) 1981-02-19 1983-02-15 Heat generating apparatus and its process utilizing air circulation and convection

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56022171A JPS6033235B2 (en) 1981-02-19 1981-02-19 Reduced pressure equilibrium forced rotation convection heating drying method and its equipment

Publications (2)

Publication Number Publication Date
JPS57139271A JPS57139271A (en) 1982-08-28
JPS6033235B2 true JPS6033235B2 (en) 1985-08-01

Family

ID=12075353

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56022171A Expired JPS6033235B2 (en) 1981-02-19 1981-02-19 Reduced pressure equilibrium forced rotation convection heating drying method and its equipment

Country Status (3)

Country Link
JP (1) JPS6033235B2 (en)
BE (1) BE892149A (en)
ZA (1) ZA821069B (en)

Also Published As

Publication number Publication date
JPS57139271A (en) 1982-08-28
BE892149A (en) 1982-08-16
ZA821069B (en) 1983-01-26

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