JPS58121954A - Apparatus for sterilizing particulate material under heating - Google Patents
Apparatus for sterilizing particulate material under heatingInfo
- Publication number
- JPS58121954A JPS58121954A JP57004478A JP447882A JPS58121954A JP S58121954 A JPS58121954 A JP S58121954A JP 57004478 A JP57004478 A JP 57004478A JP 447882 A JP447882 A JP 447882A JP S58121954 A JPS58121954 A JP S58121954A
- Authority
- JP
- Japan
- Prior art keywords
- hot air
- dryer
- powder
- conveyor
- supply pipe
- 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
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
- Bakery Products And Manufacturing Methods Therefor (AREA)
- Apparatus For Disinfection Or Sterilisation (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】
本発明は粉粒体の加熱殺菌装置に関するもので弗りて、
特に処置速度が速く、熱効率の高い装置であって、しか
も処理能力?更に増大し、′tた熱エネルギーの効率的
利用1図ることのできる装置に侮るものである0′
従来から粉粒体の加熱殺菌装置は種々のものが提案され
ているが、これらは処理時間の短縮化、高能率化や熱エ
ネルギーの効率的利用という点では必ずしも満足できる
ものではなかつ友。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for heat sterilization of powder and granular materials.
In particular, it is a device with fast treatment speed and high thermal efficiency, and is it capable of processing? Furthermore, the heat sterilization equipment for powder and granules has been proposed in the past, but these devices have a short processing time. However, it is not always satisfactory in terms of shortening the time, increasing efficiency, and efficient use of thermal energy.
本発明はこのような従来型装置の欠点?解消せんとして
なされたものでおって、高温高湿熱風を使用し、且つこ
れ全循環させて、加熱殺菌全行々う方式によって処理速
度全速め、熱効率を高めると共に、循環する熱風が所宕
の湿度に調整され定常状態に至つ几彼は粉粒体の供給先
を熱風供給管路の始端に切換えて管路内でも粉粒体の処
理1行ない、処理容ti′に一層増大させるよう圧し友
ものである。Does the present invention overcome the drawbacks of such conventional devices? This method was developed as a solution to the problem, and the method uses high-temperature, high-humidity hot air and circulates it throughout the entire process to completely speed up the processing speed and increase thermal efficiency. After the humidity was adjusted and a steady state was reached, he switched the supply destination of the powder and granules to the starting end of the hot air supply pipe, processed the powder and granules in the pipe, and applied pressure to further increase the processing volume ti'. It's a friend.
進んで本発明?図示O寅施例に基づbて具体的に説明す
ると、符号lは乾燥機であって、−例として横型ドラム
式のものであシ、回転全付与して、図中左側の始端側か
ら供給される粉粒体t1回転によシス中右側の終端側へ
攪拌し乍ら移送し、ドラム内に供給される熱風と接触さ
せて加熱殺菌を行うものである。 同、乾燥機は横型に
限らず竪型の流動層式のものを用いても元より差し支え
ない。Willing to invent this invention? To explain in detail based on the illustrated example, reference numeral l denotes a dryer, and for example, it is a horizontal drum type. The supplied powder and granular material is stirred and transferred to the right end side of the system by rotation t1, and is brought into contact with hot air supplied into the drum to perform heat sterilization. Similarly, the dryer is not limited to a horizontal type, and a vertical fluidized bed type may also be used.
この乾燥Illに対し、先ず一例としてバーナ2を具え
た加熱器3から加湿器41r経て乾燥機l始端に至る熱
風供給管路5t−形成すると共に、乾燥機l終端から湿
度計6、集塵1)?’に経て加熱器3に至る熱風循環管
路Bt影形成、ま友ホッパー9から投入コンベヤlO?
経て乾燥機l始端に至る粉粒体投入路11を形成すると
共に乾燥機l終端から取出コンベヤ12奮経て製品バン
カー 13 K至る粉粒体取出路14 i形成する0
そして高温高湿熱風による加熱殺菌においては、熱風の
湿度會材料に合わせて適当に調整するものであって、こ
れは乾燥機lから排出される熱風の湿度を湿度計6によ
シ計測し、これに応じて加湿器4會自動又は手動で制御
することによシ行なうものである。For this drying Ill, first, as an example, a hot air supply pipe 5t is formed from a heater 3 equipped with a burner 2, through a humidifier 41r, to the beginning of the dryer I, and from the end of the dryer I, a hygrometer 6 and a dust collector 1 are formed. )? 'The hot air circulation pipe Bt leading to the heater 3 through the shadow formation, from the Mayu hopper 9 to the input conveyor lO?
A granular material input path 11 is formed which leads to the start end of the dryer 1, and a granular material take-out path 14 is formed from the end of the dryer 1 to the product bunker 13 via the take-out conveyor 12.
In heat sterilization using high-temperature, high-humidity hot air, the humidity of the hot air is adjusted appropriately according to the material. This is done by automatically or manually controlling the four humidifiers accordingly.
更に熱風循環管路8は循環ファン15金具え、また管路
途中には排気管167設け、バルブ又はダンパ17.1
8によシ排気の流通方向?切換えるものである。 また
集塵器7の下端は排出バルブ又は排出ダンパ19ケ経て
粉粒体取出路14の取出コンベヤ12に接続される。
同、集塵器7は一〇!iとしてサイクロン會図示したが
、これに限らず邪魔板による集塵器など適宜公知の装置
を使用し得るものである。Furthermore, the hot air circulation pipe 8 is equipped with a circulation fan 15, and an exhaust pipe 167 is provided in the middle of the pipe, and a valve or damper 17.1 is provided.
8. Exhaust flow direction? It is something that can be switched. The lower end of the dust collector 7 is connected to the take-out conveyor 12 of the powder take-out path 14 through 19 discharge valves or discharge dampers.
Same, dust collector 7 is 10! Although a cyclone is shown as i, the present invention is not limited to this, and any known device such as a dust collector using a baffle plate may be used as appropriate.
このように構成された装置において、前記粉粒体投入路
11における投入コンベヤ10は熱風供給管路5の始端
(図中符号加で示す)にも接続し、切換え自在とするも
のである。 図示の実施例は一例として正逆転自在のコ
ンベヤ金横置きし、その略中夫にホッパー9を臨ませる
と共にその一端を乾燥機lの始端に接続し、ま文他端?
熱風供給管路5における加湿器4の後段に接続し、投入
コンベヤLOの移送方向?切換えることによシ粉粒体の
供給光音選択できるように構成されている。 尚、投入
コンベヤは上記の笑施例會−例とするけれどもこれに限
定されない。 要は粉粒体の供給先を乾燥機lの始端と
熱風供給管路5の始端の両方に接続し、且つ、これt切
換え自在としたコンベヤの配置がなされていれば良いの
である。In the apparatus configured in this way, the feeding conveyor 10 in the powder feeding path 11 is also connected to the starting end (indicated by the addition symbol in the figure) of the hot air supply pipe 5, so that it can be switched freely. In the illustrated embodiment, as an example, a reversible conveyor is placed horizontally, with a hopper 9 facing the center of the conveyor, one end of which is connected to the starting end of a dryer l, and the other end of the conveyor placed horizontally.
Connected to the downstream of the humidifier 4 in the hot air supply pipe 5, and in the transfer direction of the input conveyor LO? It is configured so that the light and sound to be supplied to the powder and granular material can be selected by switching. Incidentally, although the input conveyor is shown in the above embodiment, it is not limited thereto. In short, it is sufficient that the conveyor is arranged such that the powder supply destination is connected to both the starting end of the dryer 1 and the starting end of the hot air supply pipe 5, and can be switched freely.
本発明は以上述べ几ような構成を有するものであって、
次の様に作動する。 先ず最初に乾燥機l?回転駆動し
、また投入コンベヤ10.取出コンベヤL21j駆動す
ると共にバーナ2に点火し、熱風t−発生させる。 熱
風は加湿器4によル高湿度化され、高温高湿熱風となっ
て熱風供給管路5内會通過し、乾燥機l内に供給される
。The present invention has the configuration as described above,
It operates as follows. First of all, the dryer? It is rotatably driven and also has an input conveyor 10. The take-out conveyor L21j is driven and the burner 2 is ignited to generate hot air t-. The hot air is made highly humid by the humidifier 4, becomes high temperature, high humidity hot air, passes through the hot air supply pipe 5, and is supplied into the dryer 1.
−万ホツバ−9からは一定量づつ粉粒体全投入コンベヤ
lOに投下し、且つ投入コンベヤto ’2図中右方へ
運転し、乾燥機l内へ投入する。- A constant amount of powder and granular material is dropped from the 1000-pound container 9 onto the input conveyor lO, and the input conveyor to'2 is driven to the right in the figure to be input into the dryer l.
乾燥機l内においては、粉粒体は攪拌され乍ら熱風と接
触して加熱殺菌され、且つ移送されて終端よシ排出され
、取出コンベヤ12によって製品バンカー瀞に貯溜され
る。 一方、高温高湿熱風は乾燥様lの終端よシ排出さ
れ、熱風循環管路8に至)、先ず集塵器7によシ微細な
粉粒体を分離除去され、次いで循環ファン15によシ加
熱器3に戻され、再び熱風供給管路5に供給される。
またここにおいて熱風の湿度は湿度計6により検出し、
これが所定値になるまで加湿器4によシ調整されるもの
であって、所定の湿度に至った後は定常状態に入る。
しかる時は投入コンベヤto 2逆転させ、粉粒体を熱
風供給管路5の始端加に投入する。 すると粉粒体は適
当な湿度に調整された熱風によシ熱風供給管路5中會粉
体輸送され、同時に加熱殺菌されて、乾燥機lに至る。In the dryer 1, the granular material is stirred and sterilized by heating in contact with hot air, and is transferred and discharged to the end, and is stored in a product bunker by a take-out conveyor 12. On the other hand, the high-temperature, high-humidity hot air is discharged from the end of the dryer 1 and reaches the hot air circulation pipe 8), where fine particles are first separated and removed by the dust collector 7, and then by the circulation fan 15. The hot air is returned to the heater 3 and supplied to the hot air supply pipe 5 again.
In addition, the humidity of the hot air is detected by a hygrometer 6,
The humidity is adjusted by the humidifier 4 until it reaches a predetermined value, and after reaching the predetermined humidity, it enters a steady state.
In such a case, the feeding conveyor TO 2 is reversed and the powder is fed into the starting end of the hot air supply pipe 5. Then, the powder is transported through the hot air supply pipe 5 by hot air adjusted to an appropriate humidity, and is simultaneously heat sterilized and delivered to the dryer 1.
このように熱風供給管路51?加熱殺菌に用いること
によって装置の処理容量が増大し、処理能力の向上?図
ることができるのでおる。In this way, the hot air supply pipe 51? By using it for heat sterilization, the processing capacity of the equipment increases and the processing capacity improves? It is possible to achieve this goal.
因みにこの種装置は処理の効率?良くする次め比較的大
型であることよシ、熱ML供給管路5の径や長さも充分
大きく形成されておシ、これ?活用することによって処
理能力の充分な向上金回ることかできるものである。By the way, is this kind of equipment efficient in processing? Second, it should be relatively large, and the diameter and length of the heat ML supply pipe 5 should be sufficiently large. By making full use of it, it is possible to make substantial improvements in processing capacity.
以上詳述したように本発明は、高温高湿熱風を循環使用
することによって処理速度の速い、熱効率の良い加熱殺
菌処理かなし得ると共に、従来型と同規模の装置と比較
しても一層処理能力が太きく、シかも熱エネルギーの節
約7図ることができるなど、総合性能の優れた装置であ
る。As described in detail above, the present invention enables heat sterilization treatment with high processing speed and high thermal efficiency by circulating high-temperature, high-humidity hot air. It is a device with excellent overall performance, with large capacity and the ability to save heat energy.
図は本発明の一実施例?示す骨格的系統図である。
l;乾 燥 4!l 2;パ − す3;加熱器
4;加湿器
5;熱風供給管路 6;湿 度 計
7;集 塵 器 8;熱風循環管路9:ホッパ−l
O:投入コンベヤ
11:粉粒体投入路 12;取出コンベヤ13;製品
バンカー 14:粉粒体取出路15;循環ファン
16;排 気 管17.18;バルブ(又はダンパ)
19;排出バルブ(又は排出ダンパ)
加;熱風供給管路始端Is the figure an example of the present invention? FIG. l; Dry 4! l 2; Part 3; Heater
4; Humidifier 5; Hot air supply pipe 6; Humidity total 7; Dust collector 8; Hot air circulation pipe 9: Hopper l
O: Input conveyor 11: Powder input path 12; Takeout conveyor 13; Product bunker 14: Powder removal path 15; Circulation fan
16; Exhaust pipe 17. 18; Valve (or damper) 19; Exhaust valve (or exhaust damper); Hot air supply pipe starting end
Claims (1)
と、乾燥機終端から湿度計、集塵器?経て加熱器に至る
熱風循環管路音形成し、またホッパーから投入コンベヤ
會経て乾燥機始端に至る粉粒体投入路全形成すると共に
乾燥機終端から取出コンベヤ?経て製品バンカーに至る
粉粒体取出路?形成し、更に上記粉粒体投入路における
投入コンベヤは熱風供給管路の始端にも接続して切換え
自在としたことt特徴とする粉粒体の加熱殺菌装置。The hot air supply pipe from the heater to the humidifier to the start of the dryer, and the hygrometer and dust collector from the end of the dryer? It forms the hot air circulation pipe that goes through the heater, and also forms the entire powder input path from the hopper to the input conveyor to the start of the dryer, and also the take-out conveyor from the end of the dryer. The powder and granule material removal route that leads to the product bunker? 2. A heating sterilization apparatus for powder and granular material, characterized in that the feeding conveyor in the powder feeding path is also connected to the starting end of the hot air supply pipe and can be switched freely.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57004478A JPS58121954A (en) | 1982-01-13 | 1982-01-13 | Apparatus for sterilizing particulate material under heating |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57004478A JPS58121954A (en) | 1982-01-13 | 1982-01-13 | Apparatus for sterilizing particulate material under heating |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58121954A true JPS58121954A (en) | 1983-07-20 |
Family
ID=11585210
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57004478A Pending JPS58121954A (en) | 1982-01-13 | 1982-01-13 | Apparatus for sterilizing particulate material under heating |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58121954A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5626180A (en) * | 1979-08-10 | 1981-03-13 | Kikkoman Corp | Thermal sterilization of powder and granule |
-
1982
- 1982-01-13 JP JP57004478A patent/JPS58121954A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5626180A (en) * | 1979-08-10 | 1981-03-13 | Kikkoman Corp | Thermal sterilization of powder and granule |
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