JP2779808B2 - Fluidized bed dryer for food - Google Patents
Fluidized bed dryer for foodInfo
- Publication number
- JP2779808B2 JP2779808B2 JP63032457A JP3245788A JP2779808B2 JP 2779808 B2 JP2779808 B2 JP 2779808B2 JP 63032457 A JP63032457 A JP 63032457A JP 3245788 A JP3245788 A JP 3245788A JP 2779808 B2 JP2779808 B2 JP 2779808B2
- Authority
- JP
- Japan
- Prior art keywords
- fluidized bed
- food
- superheated steam
- drying
- filter
- 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 - Lifetime
Links
- 235000013305 food Nutrition 0.000 title claims description 17
- 238000001035 drying Methods 0.000 claims description 26
- 239000002184 metal Substances 0.000 claims description 17
- 238000010030 laminating Methods 0.000 claims description 3
- 238000003466 welding Methods 0.000 claims 1
- 239000000843 powder Substances 0.000 description 7
- 238000009423 ventilation Methods 0.000 description 7
- 239000000428 dust Substances 0.000 description 5
- 230000001954 sterilising effect Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 238000011001 backwashing Methods 0.000 description 3
- 238000010981 drying operation Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 241000283973 Oryctolagus cuniculus Species 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 241000588724 Escherichia coli Species 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000009545 invasion Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Freezing, Cooling And Drying Of Foods (AREA)
- Filtering Materials (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は過熱蒸気を使用する流動層乾燥装置に関し、
特に乾燥室の上部に金属フィルタを取り付けて粉末状食
品の乾燥を可能にしたことを特徴とするものである。Description: FIELD OF THE INVENTION The present invention relates to a fluidized-bed dryer using superheated steam,
In particular, a metal filter is attached to the upper part of the drying chamber to enable drying of the powdery food.
(従来の技術) 粉粒体を乾燥するには流動層乾燥装置が多く用いられ
る。流動層乾燥装置は乾燥室の底面に通気板が張られて
おり、更にこれに熱風供給ダクトが接続されていて通気
板から乾燥室に熱風を吹き上げて乾燥室内に流動層を形
成するもので、粉粒体を能率よく連続的に乾燥するに適
している。(Prior Art) Fluidized bed dryers are often used to dry powders. In the fluidized bed drying apparatus, a ventilation plate is provided on the bottom of the drying chamber, and a hot air supply duct is further connected to the ventilation plate to blow up hot air from the ventilation plate to the drying chamber to form a fluidized bed in the drying chamber. It is suitable for drying the granules efficiently and continuously.
ところで、一般に流動層乾燥装置は乾燥室の上部に織
布やフェルト等を用いて形成したバグフィルタが取り付
けられていて排気ダクトに向かって上昇する軽量な粉粒
体を捕集するようになっているが、粉粒体が粉末状の食
品の場合にはフィルタバッグ内で架橋現象を作り易いた
めに目づまりを起こし易い。殊に食品の乾燥には殺菌の
ために過熱蒸気を使用するのでその傾向が著しいうえこ
れらのフィルタバッグは逆洗によって目づまりした粉粒
体をを取り除くことが極めて困難であり、しかもフェル
ト製のフィルタバッグは水洗することもできず、一旦目
づまりを起こすと再使用することが出来ない。By the way, in general, a fluidized bed drying apparatus is provided with a bag filter formed using a woven cloth, felt, or the like at the upper part of a drying chamber, and collects light-weight particles rising toward an exhaust duct. However, when the powder is a food in the form of powder, clogging is liable to occur since the crosslinking phenomenon easily occurs in the filter bag. In particular, the drying of food uses superheated steam for sterilization, so the tendency is remarkable.In addition, it is extremely difficult for these filter bags to remove clogged powder particles by backwashing, and furthermore, felt bags made of felt are used. Filter bags cannot be washed with water and cannot be reused once they become clogged.
そのため従来は食品用の流動層乾燥装置にはバグフィル
タは取り付けず、これに代えて排気経路にサイクロン集
塵器やマルチクロン集塵器を接続して排ガスと共に機外
に排出される粉粒体を捕集する方策が採られていた。For this reason, conventionally, bag filters are not attached to fluidized bed dryers for foods, and instead, cyclone dust collectors or multi-cyclone dust collectors are connected to the exhaust path, and the powder particles discharged outside the machine together with exhaust gas Measures were taken to capture
(従来技術の問題点) しかしながらサイクロン集塵器やマルチクロン集塵器
は数ミクロン以下の微粉は捕集することが出来ないの
で、更に後段にスクラバー等の高性能の集塵装置を備え
ざるを得なかった。(Problems of the prior art) However, cyclone dust collectors and multi-cyclone dust collectors cannot collect fine powder of several microns or less, so a high-performance dust collector such as a scrubber must be provided at a later stage. I didn't get it.
そのため設備費が嵩み、保守が面倒になると言う不具合
があった。As a result, there has been a problem that equipment costs are increased and maintenance is troublesome.
(発明の目的) 本発明は乾燥用熱風として過熱蒸気を使用した場合に
も目づまりを起こしにくく、逆洗をすることの出来る金
属フィルタを取り付けることを目的とする。(Object of the Invention) It is an object of the present invention to attach a metal filter which is hardly clogged even when superheated steam is used as hot air for drying and can be backwashed.
(発明の概要) 本発明は線経数十〜数百マイクロメータの金属線を平
織り又は畳織りした金網を数枚重ね合わせて金属フィル
タとし、この金属フィルタを微紛の捕集用として使用す
るため流動層乾燥装置の所定の位置に取り付けたもので
ある。(Summary of the Invention) In the present invention, a metal filter is formed by stacking several wire nets each having a wire of several tens to several hundreds of micrometers in plain weave or tatami weave, and used as a metal filter for collecting fine powder. Therefore, it is attached to a predetermined position of a fluidized-bed dryer.
(実施例) 以下、本発明を図示の実施例に基づいて具体的に説明
する。(Examples) Hereinafter, the present invention will be specifically described based on illustrated examples.
図は本発明に係る食品用流動層乾燥装置の概略を示すも
ので、図中符号1は乾燥機本体、2は被乾燥材料定量供
給装置、3は過熱蒸気供給装置である。The figure schematically shows a fluidized bed drying apparatus for food according to the present invention. In the figure, reference numeral 1 denotes a dryer main body, 2 denotes a material to be dried to be supplied constant, and 3 denotes a superheated steam supply.
乾燥機本体1はフィルタ室に金属フィルタを用いて形成
した捕集装置が取り付けられている以外は通常の流動層
乾燥装置の乾燥機本体と変わるところはない。即ち、乾
燥機本体1は流動層室4とフィルタ室5とからなり、流
動層室4には一端に被乾燥材料の投入口6が形成され、
これに被乾燥材料定量供給装置2が接続されていて流動
層室4に削り節や卯の花等の粉末状の被乾燥食品を定量
的に投入するようになっており、他端には乾燥製品の取
り出し口7が形成されていてここから乾燥された粉末状
食品を取り出すようになっている。そして底面には通気
8が張られていてその下に熱風供給ダクト9が形成され
ており、更にこれに過熱蒸気供給装置3が接続されてい
て通気鈑8から流動層室4に向けて乾燥用過熱蒸気を吹
き上げるようになっている。また、フィルタ室5の上端
には排気口10が形成されていてここから乾燥排ガス(過
熱蒸気)を排出すると共に室内には金属フィルタを用い
て形成した捕集装置11が取り付けられていて乾燥排ガス
に浮遊して上昇する粉末状食品を瀘別して捕集するよう
になっている。The dryer main body 1 is the same as the dryer main body of a general fluidized bed drying apparatus except that a collecting device formed using a metal filter is attached to a filter chamber. That is, the dryer main body 1 includes a fluidized-bed chamber 4 and a filter chamber 5, and the fluidized-bed chamber 4 is formed at one end with an inlet 6 for a material to be dried.
A drying material fixed supply device 2 is connected to the drying device so that powdered food to be dried, such as shavings and rabbit flowers, is quantitatively charged into the fluidized bed chamber 4, and the other end of the drying product is taken out. A mouth 7 is formed from which the dried powdered food is taken out. A ventilation 8 is formed on the bottom surface, and a hot air supply duct 9 is formed below the ventilation 8. A superheated steam supply device 3 is connected to the ventilation duct 8. Superheated steam is blown up. An exhaust port 10 is formed at the upper end of the filter chamber 5 to discharge drying exhaust gas (superheated steam) from the exhaust port 10 and a collection device 11 formed using a metal filter is attached to the inside of the chamber. The powdered food that rises and floats on the surface is filtered and collected.
更に詳しく説明すると、被乾燥材料定量供給装置2は
定量供給機12、送りコンベヤ13、ホッパー14等から成っ
ていて乾燥機本体1内での処理速度に合わせて被乾燥食
品を間歇的に又は連続的にホッパー13に供給し、しかし
てこれを乾燥機本体1に投入するようになっている。More specifically, the material-to-be-dried 2 is composed of a constant-rate feeder 12, a feed conveyor 13, a hopper 14, and the like, and intermittently or continuously feeds the food to be dried in accordance with the processing speed in the dryer body 1. The hopper 13 is supplied to the hopper 13, and the hopper 13 is supplied to the dryer body 1.
過熱蒸気供給装置3はデミスタ15、ヒータ16、ブロワ17
等から成り、デミスタ15にはボイラ等の蒸気発生装置18
が接続されていて、蒸気発生装置18から供給される蒸気
を所望の温度にまで加熱して熱風供給ダクト9に送り込
むようになっている。The superheated steam supply device 3 includes a demister 15, a heater 16, and a blower 17.
The demister 15 includes a steam generator 18 such as a boiler.
Is connected, and the steam supplied from the steam generator 18 is heated to a desired temperature and sent to the hot air supply duct 9.
尚、この装置は過熱蒸気を使用するところからして全
体に断熱処理が施されていることは勿論として、乾燥機
本体1から排出される排ガスはデミスタ15に戻して循環
使用すると共に、被乾燥材料の投入口6、乾燥製品の取
出口7等にはロータリーバルブ20、21を取り付けて外気
の侵入を防ぎ、系内を3%V/V以下の低空気濃度に保っ
て殺菌効果を高める様になっている。In addition to the use of superheated steam, this apparatus is not only heat-insulated, but also the exhaust gas discharged from the dryer body 1 is returned to the demister 15 for circulating use. Rotary valves 20 and 21 are attached to the material inlet 6 and dried product outlet 7 to prevent the invasion of outside air, and to maintain the inside of the system at a low air concentration of 3% V / V or less to enhance the sterilization effect. It has become.
符号22は予熱管であって、乾燥作業を開始する際に最初
の被乾燥食品を投入するに先立ってロータリーバルブ2
0、その他を加熱してこの部分の結露を取り除くもので
ある。Reference numeral 22 denotes a preheating tube, which is a rotary valve 2 before feeding the first food to be dried when the drying operation is started.
0, to heat the others to remove condensation from this part.
ところで、金属フィルタは線経数十〜数百マイクロメ
ーターの金属線を平織り又は畳織りした金網を数枚〜十
数枚積層して金網の各支点及び各層の接触点を熔接して
シート状にしたものである。By the way, a metal filter is formed by laminating several to several tens of wire meshes in which a wire of several tens to several hundreds of micrometers is plain-woven or tatami-woven, welds the fulcrums of the wire mesh and the contact points of each layer to form a sheet. It was done.
(作用) 乾燥作業を行うには、まず熱風供給ダクト9から乾燥
機本体1に向けて加熱蒸気を吹き込んで乾燥機本体1の
内壁、通気鈑8、金属フイルタ11、その他を予熱し、更
にロータリーバルブ20等を予熱してこれらに付着する結
露を取り除き、しかる後、ロータリーバルブ20を開けて
被乾燥食品を流動層室4に投入する。(Operation) To perform the drying operation, first, heated steam is blown from the hot air supply duct 9 toward the dryer main body 1 to preheat the inner wall of the dryer main body 1, the ventilation plate 8, the metal filter 11, and the like, and further, the rotary The valve 20 and the like are preheated to remove condensation adhering thereto, and thereafter, the rotary valve 20 is opened and the food to be dried is put into the fluidized bed chamber 4.
そして、作業の進行により金属フイルタ11の目づまりが
進み通気性が低下したときは、作業を中断してこれを逆
洗する。尚、この場合において逆洗用ガスは系内の過熱
蒸気を用いるのが適当である。即ち、このようにすると
操作が簡単であるばかりでなく、系内に外気が混入しな
いので低空気濃度の乾燥作業を続行することが出来、殺
菌効果が持続されるのである。When the metal filter 11 is clogged due to the progress of the work and the air permeability decreases, the work is interrupted and the backwash is performed. In this case, it is appropriate to use the superheated steam in the system as the backwash gas. That is, in this case, not only the operation is simple, but also since the outside air does not enter the system, the drying operation with a low air concentration can be continued, and the sterilizing effect can be maintained.
(効果) 以上詳述したように本発明は過熱蒸気を使用する食品
用流動層乾燥装置において、線経数十〜数百マイクロメ
ーターの金属線を用いて平織り又は畳織りした金網を数
枚〜十数枚積層してなる金属フイルタをフィルタ室5に
取り付けたものであって、金属フィルタが耐熱、耐有機
溶剤性であるところから高温の乾燥用ガスを使用するこ
とができるので、殺菌効果が要求される食品の乾燥に適
している。(Effects) As described in detail above, the present invention relates to a fluidized bed drying apparatus for food using superheated steam, in which several wire meshes plain or woven using a metal wire having a wire diameter of several tens to several hundred micrometers are used. A metal filter formed by laminating dozens of sheets is attached to the filter chamber 5, and since the metal filter is heat-resistant and organic solvent-resistant, a high-temperature drying gas can be used, so that a sterilizing effect is obtained. Suitable for required food drying.
殊に、この金属フィルタは目づまりを起こしにくく、し
かも目づまりは逆洗によって簡単に取り除くことができ
るので、乾燥用ガスとして過熱蒸気を使用することが出
来るうえ、この過熱蒸気を逆洗用ガスとしても利用する
ことが出来るので低空気濃度での乾燥が可能となり、殺
菌効果が高められるのでこの点でも粉末状の食品の乾燥
に適しているのである。In particular, this metal filter is less likely to cause clogging, and the clogging can be easily removed by backwashing, so that superheated steam can be used as a drying gas, and this superheated steam can be used as a backwashing gas. Can also be used, so that it can be dried at a low air concentration and the sterilization effect can be enhanced. In this respect, it is also suitable for drying powdered foods.
また、本方法はクローズドシステムのため、その排ガ
スは吹込ガスとして再度循環使用するが、この排ガスは
機内で金属フィルタを通過して清浄化されているので、
吹込ガスによるヒータの目詰まりもなく、長期間の運転
に耐えるものとなる。Further, since the present method is a closed system, the exhaust gas is circulated and reused again as a blowing gas, but since the exhaust gas has been purified by passing through a metal filter in the machine,
There is no clogging of the heater due to the blown gas, and it can withstand long-term operation.
因に、2kg/cm2の飽和蒸気を120〜150℃に加熱したヒ
ータ16を通過させて過熱蒸気とし、これを乾燥機本体1
に吹き込むことにより装置内のエアをパージした後、予
め造粒機で1〜4mmφに造粒した卯の花を流動層室4に
投入して20分間流動させたところ、卯の花は含有水分が
80%から5%に迄乾燥し、大腸菌が20万個/gから100個/
gにまで減少した。However, 2 kg / cm 2 of saturated steam was passed through a heater 16 heated to 120 to 150 ° C. to become superheated steam, which was then dried.
After purging the air in the apparatus by blowing air into the fluidized bed chamber 4, the rabbit flowers previously granulated to 1 to 4 mmφ by the granulator were allowed to flow for 20 minutes.
It is dried from 80% to 5%, and E. coli is 200,000 / g to 100 /
g.
図は本発明に係る食品用流動層乾燥装置の一例を示すフ
ローシート図である。 1:乾燥機本体置、2:定量供給装置 3:過熱蒸気供給装置、4:流動層室 5:フィルタ室、6:投入口 7:取出口、8:通気鈑 9:熱風供給ダクト、10:排気口 11:金属フィルタ、12:定量供給機 13:送りコンベヤ、14:ホッパー 15:デミスタ、16:ヒータ 17:ブロワ、18:蒸気発生装置 22:予熱管The figure is a flow sheet diagram showing an example of the fluidized bed drying apparatus for food according to the present invention. 1: Dryer main unit, 2: Fixed volume supply device 3: Superheated steam supply device, 4: Fluidized bed room 5: Filter room, 6: Inlet 7: Outlet, 8: Vent plate 9: Hot air supply duct, 10: Exhaust port 11: metal filter, 12: fixed-quantity feeder 13: feed conveyor, 14: hopper 15: demister, 16: heater 17: blower, 18: steam generator 22: preheating tube
Claims (1)
層乾燥装置において、バグフィルタは線経数十〜数百マ
イクロメーターの金属線を平織り又は畳織りした金網を
数枚〜十数枚積層し、金網の各支点及び各層の接触点を
熔着してシート状にした金属フィルタを用いて形成した
ものであり、流動層乾燥装置には熱風供給ダクトに過熱
蒸気供給装置が接続されていて乾燥熱媒体として過熱蒸
気を使用するように構成されていることを特徴とする食
品用流動層乾燥装置。In a fluidized bed drying apparatus provided with a bag filter in a filter chamber, the bag filter is formed by laminating several to several tens of wire meshes in which a metal wire having a wire diameter of several tens to several hundreds of micrometers is plain or woven. It is formed using a metal filter formed by welding each fulcrum of the wire mesh and the contact point of each layer into a sheet shape. The fluidized bed drying device is connected with a superheated steam supply device to a hot air supply duct and dried. A fluidized bed drying apparatus for food, wherein superheated steam is used as a heat medium.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63032457A JP2779808B2 (en) | 1988-02-15 | 1988-02-15 | Fluidized bed dryer for food |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63032457A JP2779808B2 (en) | 1988-02-15 | 1988-02-15 | Fluidized bed dryer for food |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01206980A JPH01206980A (en) | 1989-08-21 |
JP2779808B2 true JP2779808B2 (en) | 1998-07-23 |
Family
ID=12359502
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63032457A Expired - Lifetime JP2779808B2 (en) | 1988-02-15 | 1988-02-15 | Fluidized bed dryer for food |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2779808B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20150077656A (en) * | 2013-12-30 | 2015-07-08 | 조해준 | Moisture supply apparatus for powdered foods before sterilization of powdered foods |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2074389T3 (en) * | 1992-02-12 | 1995-09-01 | Henkel Kgaa | PROCEDURE FOR THE OBTAINING OF GRANULATES SUITABLE AS HUMIDANTS, DETERGENTS AND / OR CLEANING AGENTS. |
WO2001063191A1 (en) * | 2000-02-25 | 2001-08-30 | Glatt Gmbh | Method for producing particulate goods |
JP4777690B2 (en) * | 2005-06-02 | 2011-09-21 | 富士ケミカル株式会社 | Air filter |
CN103123204A (en) * | 2011-11-18 | 2013-05-29 | 大连得达科技发展有限公司 | Continuous type pre-crystallizer used for spinning slices |
CN102564069A (en) * | 2011-12-19 | 2012-07-11 | 大连兆阳软件科技有限公司 | Novel pre-crystallizer |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58210810A (en) * | 1982-06-03 | 1983-12-08 | Mitsubishi Heavy Ind Ltd | Bag filter |
JPS61246577A (en) * | 1985-04-24 | 1986-11-01 | 株式会社大川原製作所 | Continuous fluidized-bed drier incorporating bag filter |
-
1988
- 1988-02-15 JP JP63032457A patent/JP2779808B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20150077656A (en) * | 2013-12-30 | 2015-07-08 | 조해준 | Moisture supply apparatus for powdered foods before sterilization of powdered foods |
Also Published As
Publication number | Publication date |
---|---|
JPH01206980A (en) | 1989-08-21 |
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