JPH02312570A - Production of processing raw material for soy sauce - Google Patents
Production of processing raw material for soy sauceInfo
- Publication number
- JPH02312570A JPH02312570A JP1134318A JP13431889A JPH02312570A JP H02312570 A JPH02312570 A JP H02312570A JP 1134318 A JP1134318 A JP 1134318A JP 13431889 A JP13431889 A JP 13431889A JP H02312570 A JPH02312570 A JP H02312570A
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- soy sauce
- water
- steam
- raw materials
- 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
- 239000002994 raw material Substances 0.000 title claims abstract description 59
- 235000013555 soy sauce Nutrition 0.000 title claims abstract description 27
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- 238000012545 processing Methods 0.000 title description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 39
- 102000004169 proteins and genes Human genes 0.000 claims description 10
- 108090000623 proteins and genes Proteins 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 abstract description 17
- 238000000034 method Methods 0.000 abstract description 11
- 244000068988 Glycine max Species 0.000 abstract description 6
- 235000010469 Glycine max Nutrition 0.000 abstract description 6
- 241000209140 Triticum Species 0.000 abstract description 5
- 235000021307 Triticum Nutrition 0.000 abstract description 5
- 230000001007 puffing effect Effects 0.000 abstract 2
- 239000011369 resultant mixture Substances 0.000 abstract 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 230000000704 physical effect Effects 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 4
- 229920006395 saturated elastomer Polymers 0.000 description 4
- 238000004925 denaturation Methods 0.000 description 3
- 230000036425 denaturation Effects 0.000 description 3
- 235000012437 puffed product Nutrition 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 230000001580 bacterial effect Effects 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 235000012149 noodles Nutrition 0.000 description 2
- 238000009928 pasteurization Methods 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 244000291564 Allium cepa Species 0.000 description 1
- 235000002732 Allium cepa var. cepa Nutrition 0.000 description 1
- 241000283707 Capra Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000010561 standard procedure Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 230000002522 swelling effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Landscapes
- Soy Sauces And Products Related Thereto (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は醤油用加工原料の製造法、更に詳細には二軸エ
クストルーダー処理による醤油用加工原料の製造法に関
する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing processed raw materials for soy sauce, and more particularly to a method for producing processed raw materials for soy sauce by treatment with a twin-screw extruder.
従来、二軸エクストルーダーを用いて醤油用加工原料を
製造する方法としては、一般に蛋白質原料及び/又は澱
粉質原料と水とを二軸エクストルーダーで加熱膨化せし
めることによって行なわれていた。Conventionally, a method for producing processed raw materials for soy sauce using a twin-screw extruder has generally been carried out by heat-swelling protein raw materials and/or starchy raw materials and water using a twin-screw extruder.
二軸エクストルーダーは一般に加熱バレルによる外部加
熱機能を有し、熱源として、該外部加熱と投入原料とス
クリューとの物理的摩擦により発生ずる内部発生熱との
両者を併用するものである。A twin-screw extruder generally has an external heating function using a heating barrel, and uses both the external heating and internal heat generated by physical friction between the input material and the screw as heat sources.
二軸エクストルーダーが大型化するにつれ加熱バレルに
よる外部加熱効果が相対的に小さくなり、物理的摩擦に
よる内部発生熱の比率が逆に高くなるき云う傾向があっ
た。As the size of the twin-screw extruder increases, the external heating effect by the heating barrel becomes relatively smaller, and the ratio of internally generated heat due to physical friction tends to increase.
しかし、投入原料とスクリューとの物理的摩擦の度合い
が高くなると投入原料の物理的損傷が増大し、この結果
書られる製品の物性が低下するという現象を招いていた
。例えば澱粉質原料を単独で、または蛋白質原料と混合
して加熱11−化処理を行なった場合、得られた製品(
醤油用加工原料)を製麺に供すると非常に粘り易く、特
に工場規模で製麹を実施した場合、盛込み、手入れ等の
作業が困難になり、かつ雑菌汚染され易くなるという問
題点があった。However, as the degree of physical friction between the input raw material and the screw increases, physical damage to the input raw material increases, resulting in a phenomenon in which the physical properties of the resulting product deteriorate. For example, when a starchy raw material is heated alone or mixed with a protein raw material and subjected to heating 11-treatment, the obtained product (
When processed raw materials for soy sauce) are used to make noodles, they become very sticky, and especially when making koji on a factory scale, there are problems in that it is difficult to incorporate and maintain the koji, and it is also susceptible to bacterial contamination. .
また蛋白質原料を単独で処理した場合には、運転が不安
定になり易く、そのL−果製品の膨化度や粒の大きさが
著しく不揃いになり、製品化が困難となるという問題点
があった。Furthermore, when protein raw materials are processed alone, there are problems in that operation tends to become unstable, and the degree of swelling and grain size of the L-fruit products become significantly uneven, making it difficult to commercialize them. Ta.
また、大型の二軸エクストルーダーでは、スクリューの
直径が大きいためスクリューフライ1−(羽根)の先端
部と根本部との径の差が大きくなって両者の周速度の差
が顕著となり、熱処理の程度に差が生じやすく、また原
料が加熱バレルの表面に接触する顛度にも多大な差を生
じるため、加熱が均一に行なわれないという不安定な運
転状況になりやすかった。In addition, in large twin-screw extruders, the diameter of the screw is large, so the difference in diameter between the tip and the root of the screw fly (blade) becomes large, and the difference in circumferential speed between the two becomes noticeable, which makes heat treatment difficult. Since the degree of heating tends to vary, and the frequency with which the raw material comes into contact with the surface of the heating barrel also varies greatly, it tends to lead to unstable operating conditions in which heating is not carried out uniformly.
そこで、本発明者は斯かる従来の二軸エクストルーダー
による加熱処理法の問題点を解消すべく種々研究を重ね
た結果、使用する水の一部を水蒸気として供給すれば、
極めて良い結果が得られることを見い出し、本発明を完
成した。Therefore, the present inventor has conducted various studies to solve the problems of the conventional heat treatment method using a twin-screw extruder, and has found that if some of the water used is supplied as steam,
They discovered that extremely good results could be obtained and completed the present invention.
ちなみに、−軸エクストルーダーを用いてd5k Ml
用原料の処理時に蒸気を併用しようとすると、−軸エク
ストルーダーの構造」二の1h性から、■ 運転が不安
定になり易く、安定した品質の製品が得られない。By the way, using a -axis extruder, d5k Ml
If steam is used in conjunction with the processing of raw materials, due to the structure of the -shaft extruder, (1) operation tends to become unstable and products of stable quality cannot be obtained.
■ 蛋白質の熱変性が不均一となり、一部未変性の部分
が残る。■ Thermal denaturation of proteins becomes uneven, leaving some undenatured parts.
■ 多量の蒸気を供給した場合、蒸気がバレル内を逆流
する。■ If a large amount of steam is supplied, the steam will flow backwards inside the barrel.
等の問題があった。There were other problems.
本発明は蛋白質原料及び/又は澱粉質原料と水との混合
物を二軸エクストルーダーで加熱膨化処理して醤油用加
工原料を製造する方法において、使用する水の一部を水
蒸気として供給することを特徴とする醤油用加工原料の
製造法である。The present invention provides a method for producing processed raw materials for soy sauce by heating and expanding a mixture of protein raw materials and/or starchy raw materials and water using a twin-screw extruder, in which a portion of the water used is supplied as steam. This is a unique method for producing processed raw materials for soy sauce.
本発明に用いられる蛋白質原料としては例えば脱脂大豆
及びその粉砕物等が挙げられ、また澱粉質原料としては
例えば小麦、米、玉蜀黍及びそれらの粉砕物等が挙げら
れる。因に、当該原料は、その粒度を60メツシユ、好
ましくは100メツシユ以下に粉砕して使用するのが特
に良い結果を与える。Examples of protein raw materials used in the present invention include defatted soybeans and pulverized products thereof, and examples of starchy raw materials include wheat, rice, onion corn, and pulverized products thereof. Particularly good results are obtained when the raw material is ground to a particle size of 60 mesh, preferably 100 mesh or less.
かかる原料への水の添加量は特には問わないが、二軸エ
クストルーダー運転時の安定性を考慮すれば、原料1[
]0[71部(以下単に部という)に対し、加水量は5
〜40部が好ましい。There is no particular restriction on the amount of water added to the raw material, but if stability during operation of the twin-screw extruder is taken into consideration, the amount of water added to the raw material 1[
]0 [71 parts (hereinafter simply referred to as parts), the amount of water added was 5
~40 parts is preferred.
本発明はかかる添加水の一部、好ましくは5〜80 (
重量)%(以下単に%という)を水蒸気として供給する
。供給する水蒸気の比率が5%未満の場合には水蒸気供
給による加熱効果は得られに<<、又80%を超える場
合には二軸エクストルーダーの運転が不安定となりやす
い。The present invention provides a portion of such added water, preferably 5 to 80 (
(weight)% (hereinafter simply referred to as %) is supplied as water vapor. If the ratio of the supplied steam is less than 5%, no heating effect can be obtained by supplying the steam, and if it exceeds 80%, the operation of the twin-screw extruder tends to become unstable.
本発明に於いて使用する水蒸気としては飽和水蒸気が好
ましいが、これに限定されない。尚、水蒸気添加用バル
ブには逆止弁等を設け、且つスクリューについては、水
蒸気供給位置より原料投入口側のピッチを小さくするの
が、バレル内での水蒸気の逆流を防止する上で良い結果
を与える。The steam used in the present invention is preferably saturated steam, but is not limited thereto. In addition, it is best to install a check valve, etc. in the steam addition valve, and to make the pitch of the screw smaller on the raw material input port side than the steam supply position, in order to prevent backflow of steam inside the barrel. give.
また水蒸気の吐出圧力はゲージ圧で8kg/cm’以下
が好ましい。8kg/Cm2を超えるとバレル並びに前
処理用攪拌コンベアでの逆流を起こし易い。Further, the discharge pressure of steam is preferably 8 kg/cm' or less in gauge pressure. If it exceeds 8 kg/Cm2, backflow is likely to occur in the barrel and pretreatment stirring conveyor.
斯かる水蒸気の供給方法としては、その具体的方法の如
何を問わないが、例えば前処理用とじてバレル原料投入
口側ご′攪拌コンベアを設け、このコンベア内で原料に
水と共に水蒸気を添加混合せしめてから二軸エクストル
ーダーに投入する方法、あるいは二軸エクストルーダー
のバレル内に直接水蒸気を投入する方法およびこれらの
併用等の方法が挙げられる。The specific method for supplying such steam does not matter, but for example, for pre-treatment, a stirring conveyor is provided at the raw material input port side of the barrel, and water and steam are added to and mixed with the raw material in this conveyor. Examples include a method of charging the water vapor into a twin-screw extruder after letting it cool, a method of directly charging steam into the barrel of a twin-screw extruder, and a combination of these methods.
本発明で使用する二軸エクストルーダーは特に限定され
ないが、スクリューの直径が100mm以上の大型のも
のを用いた場合に特に本発明の効果が顕著である。Although the twin-screw extruder used in the present invention is not particularly limited, the effects of the present invention are particularly remarkable when a large-sized one with a screw diameter of 100 mm or more is used.
前記の大型の二軸エクストルーダーを使用する場合、二
軸エクストルーダーへの原料の供給量は400kg/時
以上が好ましい。400kg/時より少ないとバレル内
部での空隙が多い為、水蒸気を直接バレル内に供給する
と、かえって運転状況が不安定になり易い。When using the above-mentioned large-sized twin-screw extruder, the feed rate of raw materials to the twin-screw extruder is preferably 400 kg/hour or more. If it is less than 400 kg/hour, there will be a lot of voids inside the barrel, so if steam is supplied directly into the barrel, the operating situation will tend to become unstable.
本発明方法によれば、二軸エクストルーダーにより蛋白
質原料及び/又は澱粉質原料を加熱膨化処理するに際し
、熱エネルギーの一部が供給水蒸気で代替されるため、
投入原料とスクリ;・−との物理的l!?擦による内部
発生熱を最小限に抑えることができ、その結W投大原料
の物理的損傷が少なくなるとともに、安定した運転状況
が(11られ、均〜な優れた品質の御油用原料をljる
、−とが出来る3゜すなわ鼾)、拐られる製品は物性が
良好で粘らず、製麹工程に於ける、盛込み、丁入れ等の
作業が容易となるだけでなく、製麹中に過度にl!+1
菌汚染されることを防止できる。According to the method of the present invention, when a protein raw material and/or a starchy raw material is heated and expanded using a twin-screw extruder, a part of the thermal energy is replaced by the supplied steam.
Physical relationship between input raw materials and scraping;・-! ? The internal heat generated by rubbing can be minimized, and the physical damage to the large raw materials is reduced, and stable operating conditions are maintained (11), making it possible to produce uniform and excellent quality raw materials for oil. The product to be peeled has good physical properties and is not sticky, which not only makes it easier to incorporate and add ingredients during the koji making process. Excessively l! +1
It can prevent bacterial contamination.
更に、新たな熱汎1である水蒸気を添加することにより
製造能力を飛躍的に向」ニさせることが出来、その結果
、製品価格の低廉化が可能となる。Furthermore, by adding steam, which is a new thermal expansion agent, manufacturing capacity can be dramatically increased, and as a result, product prices can be reduced.
本発明方法は、スクリュー直径が100 mm以」二の
大型の一輔エクストルーダーによる原料の加熱膨化処理
の場合に4Nlに顕著な効果を示す。The method of the present invention exhibits a remarkable effect on 4Nl when raw materials are heated and expanded using a large extruder with a screw diameter of 100 mm or more.
以下に実施例を挙げて本発明を更に説明する。 The present invention will be further explained below with reference to Examples.
実施例1
各々60メンシJ以下に粉砕した脱脂加工大豆と小麦と
4、連続式混合1(l拌機([]清エンジニアリンクQ
↑)製スーパーターボ)に800 kg/ l+投入し
、次いで水64kg/h及びゲージ圧(3kg/ cm
2の飽和水蒸気80 kg/ h (総加水量14
4kg/h、その内の水蒸気添加量の比率が55%)を
添加し混合した。この混合物を二軸エクストルーダー(
Werner & I”fleidere社製[120
型)に投入して加圧加熱処理を行ない、次いでこれを常
圧下に押し出して膨化物を得た。丙られた膨化物を乾怪
して水分約8%の醤油用加工原料を得た。Example 1 Defatted processed soybeans and wheat, each crushed to 60 menshi
↑) 800 kg/l + water was added to the super turbo (manufactured by ↑), and then 64 kg/h of water and gauge pressure (3 kg/cm
2 saturated steam 80 kg/h (total amount of water added 14
4 kg/h, of which the ratio of the amount of water vapor added was 55%) was added and mixed. Transfer this mixture to a twin-screw extruder (
Manufactured by Werner & I”fleidere [120
The mixture was put into a mold) and subjected to pressure and heat treatment, and then extruded under normal pressure to obtain a expanded product. The puffed product was dried to obtain a raw material for soy sauce with a water content of about 8%.
この醤油用加工原料に水分が42%となるように加水し
、同時に種麹を1,6加湿合して、円盤式自動jli!
JIJ装置で製麹を行なった。この場合、醤ン11凹[
]加工原料は加水しても粘らず、製麹時の物性は良好で
あった。約43時間の製麹の後に、得られた麹を常法に
従い塩水にて仕込み、5力月間醸造した後、圧搾・火入
れ・濾過等の処理を行ない、醤油を得た。拐られた醤油
は品質良好なものであった。Add water to this processed raw material for soy sauce to a moisture content of 42%, and at the same time add 1.6% of the koji starter to the disc-type automatic JLI!
Koji was made using a JIJ device. In this case, 11 holes of soy sauce [
] The processed raw material did not become sticky even when water was added, and its physical properties during koji making were good. After making koji for about 43 hours, the obtained koji was mixed with salt water according to a conventional method, and after brewing for 5 months, it was subjected to processes such as pressing, pasteurization, and filtration to obtain soy sauce. The soy sauce stolen was of good quality.
試験例1〜6
実施例1に於い−C総加水Jjt中の水蒸気の添加量の
比率を下記第1表に示すように変えた以外は実施例1と
同様にしてヤ肝油用加り原料を(+、また。J−の仙油
用加工原料を実施例1と同様に処理して製麺を行なった
。Test Examples 1 to 6 Additive raw materials for goat liver oil were prepared in the same manner as in Example 1, except that the ratio of the amount of water vapor added in the -C total hydration Jjt was changed as shown in Table 1 below. (+ and J-) were treated in the same manner as in Example 1 to make noodles.
S二軸エクストルーダー処理11、シの運転状況、住1
られた醤油相加−[原料の蛋白質変性度、膨化度及び製
麹時の物性について第1表に示す。S two-shaft extruder processing 11, operation status of S, housing 1
Table 1 shows the degree of protein denaturation, degree of swelling, and physical properties during koji making of the raw materials.
尚、蛋白質の変性度は日本醤油研究所4rlr 几u
5 。In addition, the degree of denaturation of the protein is determined by the Japan Soy Sauce Research Institute 4rlr 几u
5.
(4)、165. (1979)に記11市の酢酸お
りall+定法に従って測定し、酢酸おりの発生のある
ものをプラス、無いもの4マイナスと表示した。(4), 165. (1979), the acetic acid deposits in 11 cities were measured according to the standard method, and those with acetic acid deposits were indicated as plus, and those without were indicated as four minus.
以−ド余白
実施例2
脱脂加工大豆を60メツシユ以下に粉砕した後実施例1
と同様の二軸エクストルーダーに720kg/h投入し
、ついで水110 kg/ h及びゲージ圧2kg/c
m2の飽和水蒸気57kg/h(総論水量167 kg
/ )+、その内の水蒸気添加量の比率が34.8%)
を添加し混合して加圧加熱処理を行ない、次いでこれを
常圧下に押し出して膨化物を得た。Example 2 After crushing defatted processed soybeans to 60 mesh or less Example 1
720 kg/h into the same twin-screw extruder, then 110 kg/h of water and 2 kg/c of gauge pressure.
m2 of saturated steam 57 kg/h (overall water volume 167 kg
/ )+, of which the ratio of water vapor addition is 34.8%)
was added, mixed, and subjected to pressure and heat treatment, and then extruded under normal pressure to obtain a expanded product.
得られた膨化物を乾煙し水分約8%の醤油用加工原料を
得た。この醤油用加工原料に水分60%となるよう加水
した後、等量の炒黙割砕小麦を混合し、次いで種麹を添
加して常法に従い製麹した。The obtained puffed product was dried and smoked to obtain a processed raw material for soy sauce having a water content of about 8%. After adding water to this processed raw material for soy sauce to a moisture content of 60%, an equal amount of roasted cracked wheat was mixed, and then seed koji was added and koji was made according to a conventional method.
得られた麹を常法により5力月間醸造し品質良好なる醤
油を得た。The obtained koji was brewed for 5 months in a conventional manner to obtain soy sauce of good quality.
試験例7〜12
実施例2に於いて総論水量中の水蒸気の添加量の比率を
第2表に示すよう変え、二軸エクストルーダーのモータ
ーの負荷がほぼ一定となるよう、原料フィード量を変え
ながら運転した以外は実施例2と同様に処理を行ない醤
油用加工原料を得た。Test Examples 7 to 12 In Example 2, the ratio of the added amount of water vapor in the general water amount was changed as shown in Table 2, and the raw material feed amount was changed so that the load on the motor of the two-shaft extruder was almost constant. Processed raw materials for soy sauce were obtained by carrying out the same treatment as in Example 2, except that the operation was carried out while the process was in progress.
この醤油用加工原料を実施例2と同様に製麹を行なった
。This processed raw material for soy sauce was subjected to koji production in the same manner as in Example 2.
以下余白
上記の結果より、水蒸気添加量を増大させると原料フィ
ード量を増すことができ、その結果製造能力が飛躍的に
向上することが判る。From the above results, it can be seen that by increasing the amount of water vapor added, the feed amount of raw materials can be increased, and as a result, the manufacturing capacity can be dramatically improved.
実施例3
小麦を実施例1と同様の連続式混合攪拌機に800kg
/h投入し、次いで水128kg/h及びゲージ圧2.
Okg/Cm2の飽和水蒸気96 kg/ h添加混合
した。この混合物を実施例1と同様の二軸エクストルー
ダーに投入して更に同圧力の水蒸気96kg/h(総論
水量320 kg/ h、その内の水蒸気添加量の合計
比率60%)を添加して加圧加熱処理を行ない、次いで
これを常圧下に押し出して膨化物を得た。得られた膨化
物を乾燥して水分を約8%とした後、割砕し醤油用加工
原料を得た。Example 3 800 kg of wheat was placed in the same continuous mixer as in Example 1.
/h, then water 128kg/h and gauge pressure 2.
96 kg/h of saturated steam of Okg/Cm2 was added and mixed. This mixture was put into the same twin-screw extruder as in Example 1, and 96 kg/h of steam at the same pressure (total water amount: 320 kg/h, of which the total ratio of the amount of steam added was 60%) was added. A pressure and heat treatment was performed, and then this was extruded under normal pressure to obtain a expanded product. The obtained puffed product was dried to a moisture content of about 8%, and then crushed to obtain a processed raw material for soy sauce.
この醤油用加工原料に常法により得た水分約60%の蒸
煮脱脂大豆を混合し、更に種麹を添加温容し製麹した。Steamed defatted soybeans with a moisture content of about 60% obtained by a conventional method were mixed with this processed raw material for soy sauce, and seed koji was further added and heated to form koji.
この場合、醤油用加工原料は蒸煮脱脂大豆と混合しても
粘らず、製麹時の物性は良好であった。得られた麹を常
法に従い塩水にて仕込み、5力月間醸造の後、圧搾・火
入れ・濾過等の処理を行ない良好な醤油をt!jた。In this case, the processed raw material for soy sauce did not become sticky even when mixed with steamed defatted soybeans, and its physical properties during koji making were good. The obtained koji is prepared in salt water according to the conventional method, and after brewing for 5 months, it is subjected to processing such as pressing, pasteurization, and filtration to produce a good soy sauce! It was.
試験例113〜18
実施例3に於いて総加水量中の水蒸気の添加(jlの比
率を第:3表に示すように変えた以外は実施例3と同様
に処理して醤油用加工原料を拐だ3.11)られた醤油
用加工原料を実施例;(と同様にして製麹を行なった。Test Examples 113 to 18 Processed raw materials for soy sauce were processed in the same manner as in Example 3 except that the ratio of water vapor (jl) in the total amount of water added was changed as shown in Table 3. 3.11) The processed raw material for soy sauce was used to make koji in the same manner as in Example (1).
以下余白Margin below
Claims (1)
二軸エクストルーダーで加熱膨化処理して醤油用加工原
料を製造する方法において、使用する水の一部を水蒸気
として供給することを特徴とする醤油用加工原料の製造
法。1. A method for producing processed raw materials for soy sauce by heat-swelling a mixture of protein raw materials and/or starchy raw materials and water using a twin-screw extruder, characterized in that part of the water used is supplied as steam. A method for producing processed raw materials for soy sauce.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1134318A JP2720070B2 (en) | 1989-05-26 | 1989-05-26 | Manufacturing method of processing raw material for soy sauce |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1134318A JP2720070B2 (en) | 1989-05-26 | 1989-05-26 | Manufacturing method of processing raw material for soy sauce |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02312570A true JPH02312570A (en) | 1990-12-27 |
JP2720070B2 JP2720070B2 (en) | 1998-02-25 |
Family
ID=15125502
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1134318A Expired - Fee Related JP2720070B2 (en) | 1989-05-26 | 1989-05-26 | Manufacturing method of processing raw material for soy sauce |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2720070B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09191850A (en) * | 1996-01-19 | 1997-07-29 | Nippon Suisan Kaisha Ltd | Production of concentrated soy sauce of fish improved in flavor and concentrated soy sauce of fish improved in flavor |
CN116096249A (en) * | 2020-10-13 | 2023-05-09 | 善肴控股株式会社 | Process for producing solubilized product |
-
1989
- 1989-05-26 JP JP1134318A patent/JP2720070B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH09191850A (en) * | 1996-01-19 | 1997-07-29 | Nippon Suisan Kaisha Ltd | Production of concentrated soy sauce of fish improved in flavor and concentrated soy sauce of fish improved in flavor |
CN116096249A (en) * | 2020-10-13 | 2023-05-09 | 善肴控股株式会社 | Process for producing solubilized product |
Also Published As
Publication number | Publication date |
---|---|
JP2720070B2 (en) | 1998-02-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA1122847A (en) | Composition containing animal parts for production of a fried snack food and method for production thereof | |
JPS63263061A (en) | Production of flavoring agent | |
US3062657A (en) | Process for making breakfast cereal flakes | |
RU2109463C1 (en) | Method for producing bread crumb for food product crumbing | |
JPS6158539A (en) | Preparation of snack-like cake | |
JPH05192104A (en) | Method for preparing precooked cereale food | |
US20040109931A1 (en) | Reconstituted grain product | |
JPH02312570A (en) | Production of processing raw material for soy sauce | |
JPH0155863B2 (en) | ||
JP2857897B2 (en) | Puffed molded food | |
JPS6255045A (en) | Production of food with high edible fiber content | |
JPH05123121A (en) | Instant food and its production | |
WO1997004671A1 (en) | Method for thawing frozen ground fish meat | |
KR101555693B1 (en) | Making method for rice noodle containing allium hookeri and rice noodle containing allium hookeri | |
JPH0698686A (en) | Meat-like protein food having improved taste and flavor | |
KR20000063252A (en) | A chicken snack using spent fowl meat and process for preparation thereof | |
JPH0698685A (en) | Meat-like protein food having improved palatability | |
JPH01206974A (en) | Production of proteinaceous food material for fisheries paste product | |
JP2727200B2 (en) | Manufacturing method of processing raw material for soy sauce | |
JP2570554B2 (en) | Manufacturing method and manufacturing apparatus for koji-making raw materials | |
JP2899918B2 (en) | Manufacturing method of processing raw material for soy sauce | |
JPS60120959A (en) | Preparation of liver spread | |
JP3303949B2 (en) | Method for producing puffed food containing fish bone | |
JPS6324675B2 (en) | ||
JPH0738787B2 (en) | Manufacturing method of processing raw materials for brewing |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |