JPH0675493B2 - Liquid injection device for food extruder - Google Patents
Liquid injection device for food extruderInfo
- Publication number
- JPH0675493B2 JPH0675493B2 JP60054871A JP5487185A JPH0675493B2 JP H0675493 B2 JPH0675493 B2 JP H0675493B2 JP 60054871 A JP60054871 A JP 60054871A JP 5487185 A JP5487185 A JP 5487185A JP H0675493 B2 JPH0675493 B2 JP H0675493B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- water
- food
- tank
- metering pump
- 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
- 239000007788 liquid Substances 0.000 title claims description 40
- 238000002347 injection Methods 0.000 title claims description 34
- 239000007924 injection Substances 0.000 title claims description 34
- 235000013305 food Nutrition 0.000 title claims description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 53
- 230000000903 blocking effect Effects 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims description 2
- 229920002472 Starch Polymers 0.000 description 10
- 239000008107 starch Substances 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 8
- 239000000463 material Substances 0.000 description 6
- 235000019698 starch Nutrition 0.000 description 6
- 238000001125 extrusion Methods 0.000 description 3
- 230000001737 promoting effect Effects 0.000 description 3
- 240000007594 Oryza sativa Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 229920002261 Corn starch Polymers 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000008120 corn starch Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 102000038379 digestive enzymes Human genes 0.000 description 1
- 108091007734 digestive enzymes Proteins 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 235000020357 syrup Nutrition 0.000 description 1
- 239000006188 syrup Substances 0.000 description 1
- 235000019583 umami taste Nutrition 0.000 description 1
- 235000019607 umami taste sensations Nutrition 0.000 description 1
Landscapes
- Confectionery (AREA)
- Manufacturing And Processing Devices For Dough (AREA)
- Formation And Processing Of Food Products (AREA)
Description
【発明の詳細な説明】 〔発明の属する技術分野〕 本発明は食品押出成形機の注液装置に係り特に連続的か
つ均一な注液を可能にした注液装置に関する。Description: TECHNICAL FIELD The present invention relates to a liquid injection device for a food extrusion molding machine, and more particularly to a liquid injection device that enables continuous and uniform liquid injection.
例えばお菓子等の食品押出成形機では一般にバレル内に
スクリュを嵌合した軸を一軸或いは複数軸を配設してこ
の軸を回転させ、一軸の場合バレル内壁とスクリュとの
間で催かな隙間を保ちながら回転させ、そして複数軸の
場合スクリュ同志を噛合或いは非噛合状態にしてバレル
内壁との間で僅かな隙間を保ちながら回転するようにし
て構成していた。このような構成においてコーンスター
チや小麦等の澱粉類および或いは肉や魚類等の食材をバ
レル内に導入し、細く砕いたりつぶしたりそして加圧お
よび加熱することにより粒状或いは粉状に粉砕しさらに
煉成しこれを小孔から押出し食品に成形していた。For example, in an extruder for food products such as sweets, generally, one or more shafts with screws fitted in the barrel are arranged and the shafts are rotated. In the case of a single shaft, a minor gap is formed between the inner wall of the barrel and the screw. In the case of multiple shafts, the screws are engaged or disengaged so that they rotate with a slight gap between them and the inner wall of the barrel. In such a configuration, starches such as corn starch and wheat and / or foodstuffs such as meat and fish are introduced into the barrel, crushed or crushed finely, and crushed into granules or powder by pressurizing and heating, and further briquetting. This was extruded through small holes to form a food product.
この場合スクリュとしては主に移送および圧縮を目的と
するスクリュ形状或いは混煉を目的とするスクリュ形
状、さらに或いは破砕を促進するスクリュ形状等それぞ
れ目的の異なる形状が組合され使用されていた。食材は
これらのスクリュとバレル内壁ならびに複数軸のスクリ
ュとスクリュとの間に強く押圧されることにより、混煉
や破砕そして加熱加圧されて食材は炊く或いは蒸す等の
α化のための加工が加えられる。この食材のα化促進の
ための重要な要素として食材への加水および加熱の問題
がある。In this case, as the screw, a screw shape intended mainly for transfer and compression, a screw shape intended for blending, or a screw shape for promoting crushing is used in combination with different purposes. The food is strongly pressed between these screws and the inner wall of the barrel as well as between the screws and screws of multiple shafts, so that the food is processed by kneading, crushing, heating and pressurizing, so that the food is cooked or steamed. Added. There is a problem of water addition and heating to the foodstuff as an important factor for promoting the gelatinization of the foodstuff.
食材に水を供給すると粘性は高まり粘性が高まると圧力
は増加し加熱の場合温度上昇が見込まれる。即ち食材に
圧力を加えて加熱すると一気圧毎に沸点温度は約10℃上
昇し、通常100℃で沸騰するものも100℃以上の加熱が可
能になり、さらに水分が食材間の伝熱媒体になってより
良い加熱効果を期待することができる。When water is supplied to the food, the viscosity increases, and when the viscosity increases, the pressure increases, and the temperature is expected to increase in the case of heating. That is, when pressure is applied to foods to heat them, the boiling point temperature rises by about 10 ° C for each atmospheric pressure, and even those that normally boil at 100 ° C can be heated to 100 ° C or more, and moreover moisture can be used as a heat transfer medium between foods. Therefore, a better heating effect can be expected.
α化された澱粉(α澱粉)は天然澱粉(β澱粉)に比較
して水で膨張する力は強く消化酵素の作用を受け易くい
わゆるうま味がある。このα澱粉を高温の状態で急速に
15%以下の水分率に脱水乾燥するとβ澱粉化しない。こ
のようなα澱粉は水や温湯を加えるのみで加熱すること
なく直ちに食することが可能なため、乾燥飯や即席もち
或いは乳幼児用食品等に広く使用されている。このよう
に食材の加工即ち澱粉のα化を促進するには加水は重要
な要素である。Compared with natural starch (β starch), gelatinized starch (α starch) has a stronger swelling power with water and is easily affected by digestive enzymes and has a so-called umami taste. This α-starch rapidly increases at high temperature
When dehydrated to a moisture content of 15% or less, β-starch does not form. Since such α-starch can be eaten immediately without heating by simply adding water or hot water, it is widely used for dried rice, instant sticky rice, food for infants and the like. As described above, water is an important factor for promoting the processing of foodstuffs, that is, the gelatinization of starch.
上記した乾燥α澱粉製造の際食材に対する不必要な加水
は余分の水分を脱水しなければならず、余分な食材への
加熱乾燥が必要になってコストを高くしていた。このた
め食品押出成形機の注液装置としては食材への加水量を
制御する機能が必要である。さらに食品押出成形機とし
て食材を加工する場合最も適した温度と圧力そして水分
率を制御する必要があり、場合によっては高圧に加圧さ
れた食材への加水を必要とする場合もあり注液装置とし
ては高圧の加水機能も必要である。Unnecessary water addition to the food material during the production of the dry α-starch described above requires dehydration of excess water, which requires heating and drying of the excess food material, resulting in high cost. Therefore, the liquid injection device of the food extrusion molding machine must have a function of controlling the amount of water added to the food material. Furthermore, when processing foodstuffs as a food extruder, it is necessary to control the most suitable temperature, pressure, and moisture content, and in some cases it may be necessary to add water to foodstuffs that have been pressurized to high pressure. Therefore, a high-pressure water addition function is also required.
ここで従来の注液装置を備えた食品押出成形機の一例を
第3図により述べる。先づ食品押出成形機11はベース12
上に複数のバレル13A、13B、13C・・・13Nが一体的に取
付けてあり、その内部にはベース12の図において右方に
設けた不図示の駆動部により回転される軸14の外周に、
移送或いは混練等の各種作業を目的とした複数のスクリ
ュ15が組合せの上嵌合されている。右側のバレル13Aの
上部には食材(図示せず)の導入を受けるホッパー16が
設けられており、ホッパー16はフイーダ17から一定量の
食材が供給されるようになっている。なおバレル13B、1
3C・・・13Nは耐圧性を有している。Here, an example of a food extruder having a conventional liquid injection device will be described with reference to FIG. First, the food extruder 11 is the base 12
A plurality of barrels 13A, 13B, 13C, ... 13N are integrally mounted on the upper side, and inside the outer periphery of the shaft 14 rotated by a drive unit (not shown) provided on the right side of the base 12 in the figure. ,
A plurality of screws 15 for the purpose of various operations such as transfer or kneading are combined and fitted together. A hopper 16 for receiving ingredients (not shown) is provided above the right barrel 13A, and the hopper 16 is adapted to be supplied with a certain amount of ingredients from a feeder 17. Barrel 13B, 1
3C ... 13N has pressure resistance.
右から2番目のバレル13B以降のバレル外周にはこれを
冷却或いは加熱するための複数の熱交換器18B、18C・・
・18Nが取付けてあり、各バレルの温度は各バレルに設
けた温度センサ19B、19C・・・19Nと自動温度調節計
(図示せず)により任意に制御し得るようになってい
る。先端のバレル13Nの端面には小孔20を有するダイ21
が固着されている。A plurality of heat exchangers 18B, 18C for cooling or heating the second barrel 13B on the outer periphery of the second barrel from the right onward.
18N is attached, and the temperature of each barrel can be arbitrarily controlled by temperature sensors 19B, 19C ... 19N and an automatic temperature controller (not shown) provided in each barrel. A die 21 having a small hole 20 on the end surface of the barrel 13N at the tip.
Is stuck.
注水装置31として上方を開口しかつ内部に水を貯えたタ
ンク32はその下面から開閉弁33と計量ポンプ34そして逆
止弁35が直列になってバレル13Aのフランジに開口した
孔22に接続されている。As a water injection device 31, a tank 32 having an upper opening and having water stored therein is connected from its lower surface to a hole 22 opened on a flange of a barrel 13A in which an opening / closing valve 33, a metering pump 34 and a check valve 35 are connected in series. ing.
このような機構において食品を成形するには、駆動部に
より軸14を介してスクリュ15を回転駆動させると共にフ
イーダ17からホッパー16を通してバレル13A内部に食材
を導入する。導入された食材はスクリュ15により移送混
練加圧破砕そして加熱されながらバレル13A、13B、13C
・・・13N内を左進し、この間α加工がなされてダイ21
の小孔20から押出される。食材がバレル13A等内を進行
しているときバレル13Aの孔2からタンク32内の水が計
量ポンプ34により加圧されて注入される。In order to form the food with such a mechanism, the screw 15 is rotationally driven by the drive unit via the shaft 14 and the food is introduced into the barrel 13A from the feeder 17 through the hopper 16. The introduced food material is transferred, kneaded, pressure crushed, and heated by the screw 15 while barrels 13A, 13B, 13C are being heated.
... Move left in 13N, and during this time α processing is performed, die 21
Is extruded through the small holes 20 of. When the foodstuff is traveling in the barrel 13A or the like, the water in the tank 32 is pressurized and injected from the hole 2 of the barrel 13A by the measuring pump 34.
計量ポンプとしては注水場所によってバレル内の圧力が
高圧であるため通常歯車ポンプやピストンポンプが使用
されており、これらのポンプは水を加圧注水するとき吐
出圧および吐出水量は衆知のように変動、すなわち脈流
現象が発生する。特に少量の水を注水する場合、断続的
な注水であって食材を毎時20kgかつ、10%加水の条件で
押出加工する場合、注水量は毎時2kgであり水の比重を
1とすると毎時2lすなわち毎秒微小な0.56ccの注水量で
あって、ピストンポンプ等ではピストンの圧縮工程にの
み液体が吐出され断続的な注水となり連続かつ均一な食
材への注液は不可能であった。したがって、第3図に示
す従来装置の場合、すなわち、計量ポンプ34の下流側に
細管からなる注水管36が接続されている場合、ポンプ吐
出量が変動すると、この変動は、注水管36内では解消さ
れず、注水量が変動する結果となっている。As the metering pump, the pressure inside the barrel is high depending on the water injection location, so gear pumps and piston pumps are usually used.When these pumps are used to pressurize water, the discharge pressure and the amount of discharged water fluctuate as is well known. That is, a pulsating flow phenomenon occurs. Especially when pouring a small amount of water, if it is intermittent pouring and the food material is extruded under the condition of 20 kg / h and 10% water addition, the pouring amount is 2 kg / h and the specific gravity of water is 1 l / h. It was a small amount of water injection of 0.56 cc per second, and the liquid was discharged only in the compression process of the piston in the piston pump and the like, and the water was intermittently injected, and it was impossible to inject it into the food material continuously and uniformly. Therefore, in the case of the conventional apparatus shown in FIG. 3, that is, in the case where the water injection pipe 36 made of a thin tube is connected to the downstream side of the metering pump 34, when the pump discharge amount changes, this change occurs in the water injection pipe 36. It was not resolved, and the amount of water injection fluctuated.
本発明はこのような欠点を解消したもので、その目的
は、脈流現象の少ない微量な水でも高圧下で連続的に注
水することを可能にした食品押出成形機の注水装置を提
供することにある。The present invention eliminates such drawbacks, and an object thereof is to provide a water injection device of a food extruder capable of continuously injecting even a small amount of water with a small pulsating flow phenomenon under high pressure. It is in.
本発明における食品押出成形機の注液装置は、水等の液
体を貯えるタンクと、このタンク内の液体を加圧して放
出する計量ポンプと、液タンク内の液体の放出を許容あ
るいは阻止すべく前記計量ポンプに直列接続された開閉
弁と、前記計量ポンプの下流に接続された注水管とから
なる食品押出成形機の注液装置において、前記注水管が
液溜め機能を有する太管部と絞り機能を有する細管部と
からなり、かつ、前記太管部と前記タンクとの間にリリ
ーフ弁を設けたことを特徴としている。The liquid injection device of the food extruder according to the present invention comprises a tank for storing a liquid such as water, a metering pump for pressurizing and discharging the liquid in the tank, and a liquid pump for allowing or blocking the discharge of the liquid in the liquid tank. In a liquid injection device of a food extruder comprising an on-off valve serially connected to the metering pump and a water injection pipe connected to the downstream of the metering pump, the water injection pipe has a thick pipe portion having a liquid reservoir function and a throttle. It is characterized by comprising a thin tube portion having a function, and providing a relief valve between the thick tube portion and the tank.
以下本発明について一実施例を示した第1図により説明
する。食品押出成形機11は従来例である第3図において
既に説明したので新たな説明は省略する。The present invention will be described below with reference to FIG. 1 showing an embodiment. The food extrusion molding machine 11 has already been described with reference to FIG. 3, which is a conventional example, and therefore a new description will be omitted.
注液装置41は内部に水等の液体を貯えたタンク32とタン
ク32から液体の放出を許容あるいは阻止するとともにそ
の量を調整すべく絞り機能を有する開閉弁42と、液体を
加圧して放出する計量ポンプ34とその下流に接続された
注水管43と逆止弁35とから構成され、逆止弁35は食品押
出機11のバレル13Aの孔22に接続されている。そして注
水管43はアキュムレータ機能すなわち液溜め機能を有す
ると共に計量ポンプ34の圧力変動があっても、この変動
を吸収するための比較的大径の太管部44と、連続かつ均
一に注水するため絞り機能として例えば内径0.7mmで1m
長さあるいは内径1mmで3m長にし細管部45とからなって
いる。計量ポンプ34の吐出側の太管部44とタンク32との
間にはリリーフ弁46が設けてある。The liquid injection device 41 has a tank 32 that stores a liquid such as water inside, an opening / closing valve 42 that has a throttle function to allow or prevent the discharge of the liquid from the tank 32, and adjusts the amount, and pressurizes and discharges the liquid. The metering pump 34, a water injection pipe 43 connected to the downstream of the metering pump 34, and a check valve 35, and the check valve 35 is connected to the hole 22 of the barrel 13A of the food extruder 11. Further, the water injection pipe 43 has an accumulator function, that is, a liquid storage function, and even if there is a pressure fluctuation of the metering pump 34, a relatively large diameter thick pipe portion 44 for absorbing this fluctuation and continuous and uniform water injection As a diaphragm function, for example, 1 mm with an inner diameter of 0.7 mm
It has a length or inner diameter of 1 mm and a length of 3 m, and consists of a thin tube section 45. A relief valve 46 is provided between the thick pipe portion 44 on the discharge side of the measuring pump 34 and the tank 32.
なお開閉弁42はタンク32と計量ポンプ34との間に設けた
が、開閉弁42は計量ポンプ34と太管部44との間あるいは
太管部44と細管部45との間あるいは細管部45と逆止弁35
との間あるいは逆止弁35と孔22との間のいづれに設けて
もよ。い 次に前述した実施例の動作を説明する。先づタンク32に
水等の液体を貯える。この場合通常は不図示の電磁弁等
を介して水道直結で給水し、不図示の液面制御素子での
電磁弁の開閉を制御することにより定量の水を貯える。
続いて開閉弁42を開いた後計量ポンプ34を運転すると、
タンク32内の水は開閉弁42から流出し計量ポンプ34によ
り加圧され注水管43と逆止弁35を通ってバレル13A内に
注水される。このとき計量ポンプ34から吐出される高圧
の水は太管部44で受けながら蓄えられると共に計量ポン
プ34による突出圧変動は吸収され均一な水圧となる。次
いで細管部45により絞られて断続することなく連続かつ
均一になって逆止弁35を通って孔22に流出する。また、
リリーフ弁46を調節することにより太管部44の内圧を任
意の一定圧力に設定することができるため、この太管部
44の内圧を変化させて注水量を可変に調節することがで
きる。Although the on-off valve 42 is provided between the tank 32 and the metering pump 34, the on-off valve 42 is disposed between the metering pump 34 and the thick pipe portion 44, between the thick pipe portion 44 and the thin pipe portion 45, or in the thin pipe portion 45. And check valve 35
May be provided between the check valve 35 and the check valve 35 and the hole 22. Next, the operation of the above-described embodiment will be described. First, the liquid such as water is stored in the tank 32. In this case, normally, water is directly supplied through a solenoid valve (not shown) or the like, and a fixed amount of water is stored by controlling opening / closing of the solenoid valve by a liquid level control element (not shown).
Subsequently, when the metering pump 34 is operated after opening the on-off valve 42,
The water in the tank 32 flows out from the opening / closing valve 42, is pressurized by the metering pump 34, passes through the water injection pipe 43 and the check valve 35, and is injected into the barrel 13A. At this time, the high-pressure water discharged from the metering pump 34 is stored while being received by the thick pipe portion 44, and the fluctuation of the protrusion pressure by the metering pump 34 is absorbed to become a uniform water pressure. Then, it is squeezed by the narrow tube portion 45 and continuously and uniformly flows through the check valve 35 into the hole 22 without interruption. Also,
By adjusting the relief valve 46, the internal pressure of the thick pipe portion 44 can be set to an arbitrary constant pressure.
It is possible to variably adjust the water injection amount by changing the internal pressure of 44.
第2図は本発明における他の実施例の要部を示し前述し
た第1実施例では液体の流量を開閉弁およびリリーフ弁
46により調整していたが、この例では細管部を交換する
ことにより行っている。すなわち注液装置51はタンク32
から計量ポンプ34とこれに続く大管部44の下流に直径あ
るいは長さ、または直径、長さ共異なる例えば3本の細
管部52Aないし52Cを並列に接続しその下流ち開閉弁53A
ないし53Cをそれぞれに接続し、その下流を一本に合流
させてさらにその下流に逆止弁35が接続されている。FIG. 2 shows an essential part of another embodiment of the present invention, and in the above-mentioned first embodiment, the flow rate of the liquid is controlled by an opening / closing valve and a relief valve.
It was adjusted by 46, but in this example, it is performed by replacing the thin tube part. That is, the liquid injection device 51 is
From the metering pump 34 to the downstream of the large pipe portion 44 following the measuring pump 34, for example, three thin pipe portions 52A to 52C having different diameters or lengths or different diameters and lengths are connected in parallel, and the on-off valve 53A is provided downstream thereof.
To 53C are connected to each other, the downstreams thereof are merged into one, and the check valve 35 is connected further downstream thereof.
そして注液量の調整は細管部52Aないし52Cのいづれか1
本あるいは複数本を選びその下流の開閉弁53Aないし53C
を開くことにより巾広い調節が可能である。リリーフ弁
46はこの場合計量ポンプ34から送られた余分な液体をタ
ンク32に戻す働きをする。逆止弁35は逆流の恐れのない
場合は不要であるがバレル13A等の圧力が高い場合は必
要である。なお前述の説明では液体として水を例にした
がシロップ類やその他の味付液体も注入可能であること
はいうまでもない。And the adjustment of the liquid injection amount is done by either one of the thin tube parts 52A to 52C.
Select a book or multiple books and open / close valves 53A to 53C downstream thereof
Wide adjustment is possible by opening. Relief valve
46 serves in this case to return the excess liquid sent from the metering pump 34 to the tank 32. The check valve 35 is unnecessary when there is no risk of backflow, but is necessary when the pressure of the barrel 13A or the like is high. Although water is used as an example of the liquid in the above description, it goes without saying that syrups and other seasoning liquids can be injected.
本発明における食品押出成形機の注液装置は以上説明し
たように、液体を貯えたタンクから開閉弁と計量ポンプ
そして注水管とを直列に配置して食品押出成形機のバレ
ルに接続し、その注水管は液溜め機能を有する太管部と
絞り機能を有する細管部とを直列に接続した。As described above, the liquid injection device of the food extruder according to the present invention is connected to the barrel of the food extruder by arranging the on-off valve, the metering pump and the water injection pipe in series from the tank storing the liquid, As the water injection pipe, a thick pipe portion having a liquid storage function and a thin pipe portion having a restriction function were connected in series.
従って計量ポンプとして吐出水圧と吐出水量に変動のあ
るポンプが用いられても太管部でアキュムレータ的機
能、すなわち液溜め機能を有すると共に水圧の変動を吸
収し均一な高圧の水を貯えながら細管部から連続かつ均
一にその下流へ液体を供給する。これにより従来のよう
に断続的な注液は解消される利点を有する。Therefore, even if a pump whose discharge water pressure and discharge water amount fluctuate is used as a metering pump, the thick pipe portion has an accumulator function, that is, a liquid reservoir function, absorbs fluctuations in water pressure, and stores uniform high-pressure water while maintaining a thin pipe portion. Liquid is continuously and uniformly supplied to the downstream thereof. This has the advantage that intermittent injection as in the past is eliminated.
第1図は本発明の一部を断面した側面図、第2図は本発
明の他の実施例における要部系統図、第3図は従来例の
一部を断面した側面図である。 32……タンク、34……計量ポンプ、 42……開閉弁、43……注水管、 44……太管部、45……細管部。FIG. 1 is a side view showing a part of the present invention in section, FIG. 2 is a main part system diagram in another embodiment of the present invention, and FIG. 3 is a side view showing a part of a conventional example. 32 …… tank, 34 …… metering pump, 42 …… open / close valve, 43 …… water injection pipe, 44 …… thick pipe section, 45 …… thin tube section.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 鈴木 俊雄 静岡県沼津市大岡2068の3 東芝機械株式 会社沼津事業所内 (56)参考文献 特開 昭59−82035(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Toshio Suzuki 3-2068 Ooka, Numazu City, Shizuoka Prefecture Numazu Works, Toshiba Machine Co., Ltd. (56) References JP 59-82035 (JP, A)
Claims (1)
内の液体を加圧して放出する計量ポンプと、液タンク内
の液体の放出を許容あるいは阻止すべく前記計量ポンプ
に直列接続された開閉弁と、前記計量ポンプの下流に接
続された注水管とからなる食品押出成形機の注液装置に
おいて、 前記注水管が液溜め機能を有する太管部と絞り機能を有
する細管部とからなり、かつ、前記太管部と前記タンク
との間にリリーフ弁を設けたことを特徴とする食品押出
成形機の注液装置。1. A tank for storing a liquid such as water, a metering pump for pressurizing and discharging the liquid in the tank, and a series connection to the metering pump for allowing or blocking the discharge of the liquid in the liquid tank. An on-off valve and a liquid injection device of a food extruder comprising a water injection pipe connected to the downstream of the metering pump, wherein the water injection pipe is composed of a thick pipe portion having a liquid storing function and a thin pipe portion having a throttling function. A liquid injection device for a food extruder, characterized in that a relief valve is provided between the thick pipe portion and the tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60054871A JPH0675493B2 (en) | 1985-03-19 | 1985-03-19 | Liquid injection device for food extruder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60054871A JPH0675493B2 (en) | 1985-03-19 | 1985-03-19 | Liquid injection device for food extruder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61212269A JPS61212269A (en) | 1986-09-20 |
| JPH0675493B2 true JPH0675493B2 (en) | 1994-09-28 |
Family
ID=12982651
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60054871A Expired - Lifetime JPH0675493B2 (en) | 1985-03-19 | 1985-03-19 | Liquid injection device for food extruder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0675493B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5982035A (en) * | 1982-10-13 | 1984-05-11 | 藤沢 武彦 | Food extrusion molding machine |
-
1985
- 1985-03-19 JP JP60054871A patent/JPH0675493B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61212269A (en) | 1986-09-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3458321A (en) | Method for extrusion cooking of food products | |
| US4748037A (en) | Process for producing a bean cake | |
| Fletcher et al. | An experimental study of twin-screw extrusion-cooking of maize grits | |
| US4965085A (en) | Preparation of a seasoning | |
| US4786514A (en) | Method and apparatus for extruding a food product | |
| CA1087448A (en) | Continuous gelatinization process | |
| US8999422B2 (en) | Production of engineered feed or food ingredients by extrusion | |
| WO2013155331A1 (en) | Micropellets of fine particle nutrients and methods of incorporating same into snack food products | |
| TW201114376A (en) | Extruded, highly cooked, non-sticky starch products | |
| US4254150A (en) | Process for producing a foodstuff of cereal | |
| US6440473B2 (en) | Impregnated composite extrusion product | |
| GB994554A (en) | Method of and apparatus for the production of a food from starch-containing material | |
| CA1066114A (en) | Continuous double coating - natural cereal | |
| US5997934A (en) | Manufacture of cooked cereals | |
| US5216945A (en) | Apparatus for preparation of a flavoring agent | |
| US20010026828A1 (en) | Instant thickener | |
| HU222612B1 (en) | Process and equipment for the preparation of a foodstuff by extrusion | |
| CA2584174C (en) | Three-dimensional food products | |
| WO2016097167A1 (en) | Method for producing a palatable coated dry pet food | |
| JPH0675493B2 (en) | Liquid injection device for food extruder | |
| Harper | Extrusion of foods | |
| CLARK | Texturization by extrusion | |
| US3108530A (en) | Apparatus for the preparation of food compounds | |
| Sudhakar et al. | Extrusion technology of food products: Types and operation | |
| JPH0558703B2 (en) |