JPH0552184B2 - - Google Patents

Info

Publication number
JPH0552184B2
JPH0552184B2 JP12141087A JP12141087A JPH0552184B2 JP H0552184 B2 JPH0552184 B2 JP H0552184B2 JP 12141087 A JP12141087 A JP 12141087A JP 12141087 A JP12141087 A JP 12141087A JP H0552184 B2 JPH0552184 B2 JP H0552184B2
Authority
JP
Japan
Prior art keywords
koji
raw material
raw materials
puffed
extruder
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 - Fee Related
Application number
JP12141087A
Other languages
Japanese (ja)
Other versions
JPS63287481A (en
Inventor
Kazuo Sekine
Takayuki Kawazoe
Mikio Uehara
Misao Sugishita
Hiroshi Motai
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.)
Kikkoman Corp
Original Assignee
Kikkoman Corp
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 Kikkoman Corp filed Critical Kikkoman Corp
Priority to JP62121410A priority Critical patent/JPS63287481A/en
Publication of JPS63287481A publication Critical patent/JPS63287481A/en
Publication of JPH0552184B2 publication Critical patent/JPH0552184B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Alcoholic Beverages (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、エクストルーダー処理によ得られた
膨化原料を用いる固体麹の製造法の改良に関し、
エクストルーダー処理により得られた膨化原料に
微粉砕小麦、炒熬割砕小麦等、粉状物の適量を混
合被覆することによつて、該膨化原料の粘着性
(ベトつき)を防止し、製麹が容易に行なえるよ
うにするもので雑細菌が非常に少なく、プロテア
ーゼ等の酵素力価の高い、高品質の麹が得られる
固体麹の製造法に関する。 従来、脱脂大豆等の蛋白質原料と小麦等の炭水
化物原料の混合物を、エクストルーダーにて加熱
加圧混練した後、低圧下に急激に放出して膨化せ
しめ、製麹用の膨化原料を得ることが知られてい
る。 しかし、この膨化原料は中空の密閉容器内で飽
和水蒸気等により加圧加熱後、より低圧下に急激
に放出し得られた膨化原料とは異なり、麹菌を生
育させ易くするため適宜散水し、吸水させると、
該膨化原料の表面が強い粘着性を帯びるので、
種麹又は麹菌胞子を均一に散布することができな
い、雑細菌に汚染され易くなる、相互に付着
結合して団塊となり易いので、この部分における
麹品温の制御が正確に行なえなくなり、麹菌の生
育が阻害され、高品質の麹が得られない、盛込
機、手入機、製麹槽(カステン)等の製麹装置に
付着結合するので、これをあとで取り除く作業が
大変となる等の欠点を有する。 本発明は、固体麹の製造法におけるこのような
欠点を解決するため種々検討を重ねた結果、完成
されたものであつて、蛋白質原料と炭水化物原料
を、エクストルーダーにて加熱加圧混練した後、
低圧下に急激に放出して膨化せしめ、得られた膨
化原料を用いて固体麹を製造するに際し、該膨化
原料に粉状物の適量を混合被覆することを特徴と
する固体麹の製造法である。 以下、本発明を詳細に説明する。 先ず、本発明に用いる蛋白質原料としては、通
常の醤油、味噌等の製造に用いられる丸大豆、脱
脂大豆(脱脂加工大豆)等の一種又は二種以上が
挙げられる。また炭水化物原料としては醤油、味
噌、清酒、焼酎等の製造に用いられる小麦、大
麦、トウモロコシ、米、皴、各種澱粉等の一種又
は二種以上が挙げられる。 次に、本発明に用いられるエクストルーダーと
しては、単軸式のタイプ、二軸式のタイプ、いず
れを用いても良いが、二軸式のエクストルーダー
はバレルとスクリユーの間で原料が剪断発熱する
ことが少ないので、バレルの外周壁からヒーター
等で原料の品温を正確に制御し、原料を適度に変
性させることができるので好ましい。 次に、本発明を実施するには、上記蛋白質原料
及び炭水化物原料を、エクストルーダーのフイー
ド口に供給し、加熱加圧混練する。このとき、同
時に、フイード口(供給口)に、又は連通するパ
イプを通じてバレル内に、水を供給する。水は、
全原料中、5〜65%、好ましくは20〜28%になる
ように添加すれば良い。水分が5%より少ない
と、原料を均一に加熱変性することが難しく、焦
げ易くなり、また連続的に圧出、混練することが
難しくなる。反対に、65%より多いと、原料中の
固形分が希薄になり、軟らかい麺線状の圧出物が
得られるが、圧出後にベトついて、一体的に結着
し易く、アラレ状等に切断、造粒することが難し
くなる。 エクストルーダーのバレル内での原料の品温は
40〜200℃、好ましくは120〜130℃に設定し、バ
レル内の圧力は、10〜100Kg/cm2、好ましくは40
〜60Kg/cm2に設定し、そして、加熱バレル部分の
実質的滞留時間は、通常3〜120秒、好ましくは
5〜60秒になるように原料供給量を調節する。 上記したバレル内での温度が40℃より低い場
合、再び後で加熱処理が必要となる。またバレル
内での温度が200℃よりも高くなると、焦げが生
じ易くなるので好ましくない。また滞留時間は、
温度が低いときは時間を長くし、反対に温度が高
いときは時間を短くすることた好ましい。 次に、このように、水分、圧力、温度及び時間
の各条件を満たすことによつて、バレル内で加熱
加圧混練された原料をより低圧下、例えば大気圧
下に、連続的に圧出することができる。 ダイから圧出された原料は、麺線状又は帯状で
あるが、これを製麹し易い形にするため、アラレ
状等に切断又は造粒する。 この場合、かさ比重[一定容積()に対する
重量(Kg)の割合]が0.25〜0.45となるように切
断又は造粒することが好ましい。即ちかさ比重が
0.25より小さいと原料当たりの表面積が少なくな
り、酵素力価の高い麹が得にくく、反対に0.45よ
り大きいと細かい粒子となるため、通風製麹の
再、麹層に対して調温調湿の空気をスムーズに通
流させ、麹層の温度調節を常に所望の通り容易に
均一に行なうと共に、麹層内の有害ガスの排除を
円滑に行なうことが困難となり、良麹が得にくく
なる。 このようにして得られた膨化原料は、麹菌の繁
殖を容易にするため、そのまま、又は乾燥、又は
加水して、水分を25〜65%、好ましくは37〜47%
に調整したのち、粉状物の適量を混合被覆する。 本発明において、この粉状物を添加することは
極めて重要であつて、水分を25〜65%に調整した
膨化原料は、冒頭でも述べた如く、非常に強い粘
着性を有するため、種々の欠点を招来する。 これに対し、粉状物の適量を混合被覆するとき
は、該膨化原料の表面がサラサラとしたものとな
るため、種麹又は麹菌胞子を均一に散布すること
が容易となり、また原料相互の結着が防止され、
調温調湿の空気をスムーズに通流させ、麹層の温
度調節を常に所望の通り容易に均一に行なうこと
ができ、また麹層内の有害ガスの排除も円滑に行
なうことができ、雑細菌の非常に少ない、酵素力
価の高い麹が得られる。また、膨化原料の盛込
機、手入機、製麹槽等への付着が少なくなるた
め、これら製麹装置の洗滌管理が容易となる。 次に、本発明における粉状物としては、上記し
た炭水化物原料を乾燥後、粉砕したもの、炒熬割
砕したもの、又は澱粉等、非エクストルーダー処
理による炭水化物原料の粉状物、及び炭水化物原
料単独又はこれと蛋白質原料の混合物をエクスト
ルーダーで膨化し、乾燥した後粉砕して得られた
エクストルーダー処理による粉状物等が挙げられ
る。 これらは、醤油醸造における炒熬割砕小麦と同
程度あるいはそれより細かい粒度、例えば28メツ
シユ(目開き0.59m/m)程度に粉砕したものが
好ましい。 粉状物の添加は、できる限り少ない方が好まし
いが、膨化原料の粘着性を効果的に防止するため
には、蛋白質原料と炭水化物原料の出発総原料に
対して3重量%以上、特に10〜20%が好ましい。
尚、粉状物の添加量が多くなる場合には、エクス
トルーダーで膨化原料を調製するに当たり、予め
蛋白質原料と炭水化物原料の使用量を加減して、
目的とする食品の相対的な蛋白質原料と炭水化物
原料の配合バランス(例えば醤油の場合、ほぼ
1:1の配合バランス)を損なわないようにする
ことが好ましい。 次に、このように膨化原料に対し粉状物の適量
を混合被覆した後、麹菌等、糸状菌を接種し、そ
の使用菌の生育に好適な培養環境、例えば温度25
〜35℃、湿度90〜100%の室内で菌糸のハゼ込み、
又は胞子の着生数が十分となるのに必要な時間、
例えば30〜80時間培養する。 上記糸状菌としては、制限されるものではな
く、例えば醤油、味噌等の醸造食品用、種麹用、
酵素製造用等、その固体麹の用途に応じた微生物
を選択して用いることができる。例えば、アスペ
ルギルス・ソーヤ、アスペルギルス・オリゼー、
アスペルギルス・タマリ、アスペルギルス・ニガ
ー等が挙げられる。 このようにして、本発明によれば雑細菌(生細
菌)が非常に少なく、プロテアーゼ、アミラーゼ
等の酵素力価の非常に高い、高品質の麹が得られ
る。 以下、実施例を示して、本発明を具体的に説明
する。 尚、本実施例において、得られた固体麹の生細
菌数及びプロテアーゼ活性の測定は、以下の方法
により行なつた。 (1) 生細菌数の測定 加糖ブイヨン寒天培地を用いる平板法により、
35℃、48時間培養後のコロニー数を測定して求め
た。 (2) プロテアーゼ活性の測定 ミルクカゼイン(PH7.0)を基質とするアンソ
ン−萩原氏法により測定した。 実施例 1 脱脂加工大豆と小麦とを第1表記載の原料配合
となるように混合し、フイーダーを通して二軸式
エクストルーダーに供給し、水を加えながら(水
分26%)、圧力50Kg/cm2、品温128℃、滞留時間25
秒の条件で、加熱加圧混練し、麺線状に常圧下に
圧出し、プロペラカツターにて切断し、乾燥して
直径約4mm、厚さ3mmの円筒型をした、カサ比重
約0.4の膨化原料を得た。 次いで、この膨化原料に対し、盛込水分が第1
表記載の如き値となるように、スクリユー容器内
にて均一に散水した。散水、吸水後の該原料は表
面がかなり粘着性を有していることが観察され
た。 次いで、これに予め上記と同一条件で小麦をエ
クストルーダー処理して得られた膨化小麦を乾燥
した後、粉砕した得られた微粉末小麦(水分6
%、32メツシユ篩通過品)を第1表記載の割合と
なるように混合被覆し、これに醤油用種麹を接種
し、温度28℃で、常法に従い通風製麹し、本発明
の固体麹(醤油麹)を得た。 尚、比較のため、上記の固体麹の製造法におい
て、微粉末小麦を添加しない以外は上記と全く同
様に処理して、対照の固体麹を得た。 このようにして得られた固体麹について、生細
菌数、プロテアーゼ活性を測定したところ第1表
に示す如き結果が得られた。
The present invention relates to an improvement in the method for producing solid koji using a puffed raw material obtained by extruder treatment,
By mixing and coating the puffed raw material obtained by extruder treatment with an appropriate amount of powder such as finely ground wheat, cracked roasted wheat, etc., the stickiness (stickiness) of the puffed raw material is prevented. This invention relates to a method for producing solid koji that makes it easy to make koji, has very few bacteria, and produces high-quality koji that has a high titer of enzymes such as protease. Conventionally, a mixture of protein raw materials such as defatted soybeans and carbohydrate raw materials such as wheat is kneaded under heat and pressure in an extruder, and then rapidly released under low pressure to cause expansion, thereby obtaining expanded raw materials for koji making. Are known. However, this puffed raw material is different from the puffed raw material obtained by heating under pressure with saturated steam etc. in a hollow airtight container and then rapidly releasing it under lower pressure.In order to facilitate the growth of koji mold, this puffed raw material is sprinkled with water as needed to make it absorb water. If you let
Since the surface of the puffed raw material becomes highly sticky,
The seed koji or koji mold spores cannot be uniformly spread, they are easily contaminated by miscellaneous bacteria, and they tend to adhere to each other and form clumps, making it impossible to accurately control the temperature of the koji product in this area, which hinders the growth of koji mold. It is difficult to obtain high-quality koji, and it adheres to the koji making equipment such as the filling machine, handling machine, and koji making tank (kasten), making it difficult to remove it later. It has its drawbacks. The present invention was completed as a result of various studies to solve these drawbacks in the method for producing solid koji. ,
A method for producing solid koji, which is characterized in that when solid koji is produced by rapidly discharging it under low pressure to cause it to expand, and using the obtained puffed raw material, the puffed raw material is mixed and coated with an appropriate amount of powder. be. The present invention will be explained in detail below. First, the protein raw materials used in the present invention include one or more kinds of whole soybeans, defatted soybeans (defatted processed soybeans), etc., which are commonly used in the production of soy sauce, miso, etc. Examples of the carbohydrate raw materials include one or more of wheat, barley, corn, rice, coriander, various starches, etc. used in the production of soy sauce, miso, sake, shochu, and the like. Next, as the extruder used in the present invention, either a single-screw type or a twin-screw type may be used, but in a twin-screw extruder, the raw material generates heat due to shearing between the barrel and the screw. This is preferable because the temperature of the raw material can be accurately controlled using a heater or the like from the outer peripheral wall of the barrel, and the raw material can be appropriately denatured. Next, to carry out the present invention, the above-mentioned protein raw material and carbohydrate raw material are supplied to the feed port of the extruder and kneaded under heat and pressure. At this time, water is simultaneously supplied to the feed port (supply port) or into the barrel through a communicating pipe. The water is
It may be added in an amount of 5 to 65%, preferably 20 to 28% of the total raw materials. If the water content is less than 5%, it will be difficult to uniformly heat and denature the raw material, it will easily burn, and it will be difficult to continuously extrude and knead. On the other hand, if the amount is more than 65%, the solid content in the raw material will be diluted and a soft noodle-like extrudate will be obtained, but it will become sticky after extrusion and will tend to stick together, resulting in flakes, etc. It becomes difficult to cut and granulate. The temperature of the raw material inside the extruder barrel is
Set at 40~200℃, preferably 120~130℃, and the pressure inside the barrel is 10~100Kg/ cm2 , preferably 40℃.
-60 Kg/cm 2 , and the amount of raw material supplied is adjusted so that the substantial residence time in the heating barrel section is usually 3 to 120 seconds, preferably 5 to 60 seconds. If the temperature in the barrel described above is lower than 40°C, a later heat treatment will be required again. Furthermore, if the temperature inside the barrel is higher than 200°C, it is not preferable because it tends to cause scorching. Also, the residence time is
It is preferable to lengthen the time when the temperature is low, and conversely shorten the time when the temperature is high. Next, by satisfying the conditions of moisture, pressure, temperature, and time, the raw materials that have been kneaded under heat and pressure in the barrel can be continuously compressed under lower pressure, such as atmospheric pressure. can do. The raw material extruded from the die is in the shape of noodle strings or strips, but in order to make it easier to make koji, it is cut into strips or granulated. In this case, it is preferable to cut or granulate so that the bulk specific gravity [ratio of weight (Kg) to constant volume ()] is 0.25 to 0.45. In other words, the bulk specific gravity is
If it is smaller than 0.25, the surface area per raw material will be small and it will be difficult to obtain koji with high enzyme titer.On the other hand, if it is larger than 0.45, fine particles will be produced. It becomes difficult to allow air to flow smoothly, to always easily and uniformly control the temperature of the koji layer as desired, and to smoothly eliminate harmful gases within the koji layer, making it difficult to obtain good koji. In order to facilitate the propagation of koji mold, the puffed raw material obtained in this way can be used as is, dried, or added with water to reduce the moisture content to 25 to 65%, preferably 37 to 47%.
After adjusting the amount, mix and coat an appropriate amount of powder. In the present invention, it is extremely important to add this powder, and as mentioned at the beginning, the puffed raw material whose moisture content is adjusted to 25 to 65% has very strong stickiness, so it has various drawbacks. invite. On the other hand, when an appropriate amount of powder is mixed and coated, the surface of the puffed raw material becomes smooth, which makes it easy to uniformly spread the seed koji or koji mold spores, and also allows the mutual bonding of the raw materials. prevents wear and tear,
Temperature-controlled and humidity-controlled air can be circulated smoothly, and the temperature of the koji layer can always be easily and uniformly adjusted as desired. Also, harmful gases in the koji layer can be smoothly removed, making it possible to eliminate miscellaneous Koji with very few bacteria and high enzyme titer can be obtained. In addition, since there is less adhesion of the puffed raw material to the filling machine, handling machine, koji making tank, etc., it becomes easier to manage the cleaning of these koji making equipment. Next, as the powdered material in the present invention, the above-mentioned carbohydrate raw material is dried and pulverized, roasted and crushed, or powdered carbohydrate raw material processed without an extruder, such as starch, and carbohydrate raw material. Powdered materials obtained by extruder treatment, such as those obtained by swelling the protein material alone or in combination with a protein raw material using an extruder, drying it, and then pulverizing it, can be mentioned. These are preferably ground to a particle size of the same level or finer than that of roasted cracked wheat used in soy sauce brewing, for example, about 28 mesh (mesh opening 0.59 m/m). It is preferable to add as little powder as possible, but in order to effectively prevent the stickiness of the puffed material, it should be added at least 3% by weight, especially from 10 to 20% is preferred.
In addition, if the amount of powdered material to be added is large, adjust the amount of protein raw material and carbohydrate raw material used in advance when preparing the puffed raw material with an extruder.
It is preferable not to impair the relative blending balance of protein raw materials and carbohydrate raw materials (for example, in the case of soy sauce, the blending balance is approximately 1:1) of the target food. Next, after mixing and coating the puffed raw material with an appropriate amount of powder, a filamentous fungus such as Aspergillus or the like is inoculated, and the culture environment is suitable for the growth of the bacteria used, for example, at a temperature of 25°C.
Indoor mycelium at ~35℃ and 90-100% humidity,
or the time required for a sufficient number of spores to settle;
For example, culture for 30 to 80 hours. The above-mentioned filamentous fungi are not limited, and include, for example, those for brewed foods such as soy sauce and miso, those for seed koji,
Microorganisms can be selected and used depending on the purpose of the solid koji, such as for enzyme production. For example, Aspergillus soya, Aspergillus oryzae,
Examples include Aspergillus tamari and Aspergillus niger. In this manner, according to the present invention, high-quality koji can be obtained that has very few undesirable bacteria (live bacteria) and has very high enzyme titers such as protease and amylase. Hereinafter, the present invention will be specifically explained with reference to Examples. In this example, the number of viable bacteria and protease activity of the solid koji obtained were measured by the following method. (1) Measurement of the number of viable bacteria By the plate method using a sweetened bouillon agar medium,
The number of colonies was determined after culturing at 35°C for 48 hours. (2) Measurement of protease activity Measurement was performed by the Anson-Hagiwara method using milk casein (PH7.0) as a substrate. Example 1 Defatted processed soybeans and wheat were mixed to have the raw material composition listed in Table 1, and fed through a feeder to a twin-screw extruder, while adding water (moisture 26%) at a pressure of 50 Kg/cm 2 , product temperature 128℃, residence time 25
The mixture was kneaded under heat and pressure for a few seconds, extruded into noodle strings under normal pressure, cut with a propeller cutter, and dried to form a cylindrical shape with a diameter of about 4 mm and a thickness of 3 mm, with a bulk specific gravity of about 0.4. A puffed raw material was obtained. Next, the charged moisture is added to the puffed raw material in the first place.
Water was uniformly sprinkled in a screw container to obtain the values shown in the table. It was observed that the surface of the material after water sprinkling and water absorption was quite sticky. Next, the puffed wheat obtained by previously treating wheat with an extruder under the same conditions as above is dried, and the obtained fine powder wheat (moisture 6
%, passed through a 32-mesh sieve) to the proportions listed in Table 1, inoculated with soy sauce starter koji, and subjected to cross-ventilation koji production at a temperature of 28°C according to a conventional method. Koji (soy sauce malt) was obtained. For comparison, a control solid koji was obtained by performing the same process as above except that finely powdered wheat was not added. When the number of viable bacteria and protease activity of the solid koji thus obtained were measured, the results shown in Table 1 were obtained.

【表】 以上の結果から、粉状物の添加量が0%の対照
区では、散水後の盛込原料が何れの区分でもかな
りベトつきが発生し、造粒された膨化原料が相互
の結着し易かつたが、粉状物を添加した本発明の
区分では、散水後の盛込原料があまりベトつか
ず、特に30%以上添加した区分では殆どベトつか
ないことが判明した。 また、第1表の結果から、粉状物を添加しない
対照の麹は、盛込水分が42〜47%の区分で細菌に
よる汚染がひどく、プロテアーゼ活性が非常に低
く観察されたが、粉状物を添加した本発明の麹
は、盛込水分が37〜47%の区分で細菌による汚染
が少なく、プロテアーゼ活性も非常に高い値を示
すことが判る。
[Table] From the above results, in the control area where the amount of powdery material added was 0%, the packed raw materials after watering were quite sticky in all categories, and the granulated and expanded raw materials were bound to each other. However, it was found that in the category of the present invention in which powdery material was added, the loaded material did not become very sticky after watering, and especially in the category in which 30% or more was added, it was found that it was hardly sticky. In addition, from the results in Table 1, the control koji to which no powder was added was severely contaminated with bacteria in the moisture content range of 42 to 47%, and protease activity was observed to be very low. It can be seen that the koji of the present invention to which the compound has been added has little bacterial contamination in the moisture content range of 37 to 47%, and exhibits very high protease activity.

Claims (1)

【特許請求の範囲】 1 蛋白質原料と炭水化物原料を、エクストルー
ダーにて加熱加圧混練した後、低圧下に急激に放
出して膨化せしめ、得られた膨化原料を用いて固
体麹を製造するに際し、該膨化原料に粉状物の適
量を混合被覆することを特徴とする固体麹の製造
法。 2 粉状物が、炭水化物原料の乾燥粉砕物、澱粉
及び膨化原料の乾燥粉砕物からなる群より選ばれ
る少なくとも1つである特許請求の範囲第1項記
載の固体麹の製造法。
[Claims] 1. In producing solid koji using the obtained expanded raw materials obtained by kneading protein raw materials and carbohydrate raw materials under heat and pressure in an extruder, and then rapidly releasing them under low pressure to cause expansion. A method for producing solid koji, which comprises mixing and coating the expanded raw material with an appropriate amount of powder. 2. The method for producing solid koji according to claim 1, wherein the powder is at least one selected from the group consisting of dry and pulverized carbohydrate raw materials, starch, and dry and pulverized materials for puffing.
JP62121410A 1987-05-20 1987-05-20 Production of solid koji Granted JPS63287481A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62121410A JPS63287481A (en) 1987-05-20 1987-05-20 Production of solid koji

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62121410A JPS63287481A (en) 1987-05-20 1987-05-20 Production of solid koji

Publications (2)

Publication Number Publication Date
JPS63287481A JPS63287481A (en) 1988-11-24
JPH0552184B2 true JPH0552184B2 (en) 1993-08-04

Family

ID=14810484

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62121410A Granted JPS63287481A (en) 1987-05-20 1987-05-20 Production of solid koji

Country Status (1)

Country Link
JP (1) JPS63287481A (en)

Also Published As

Publication number Publication date
JPS63287481A (en) 1988-11-24

Similar Documents

Publication Publication Date Title
EP0124270B1 (en) Process for making shredded potato products
EP0367031B1 (en) Dry mix suitable for the preparation of a puffable food product, processes for the use thereof, and the puffable and/or puffed food products so produced
CN1030638C (en) Process for preparing puffed food material
CA1208066A (en) Food product and method of manufacture
EP1151676B1 (en) Process for manufacturing a cereal bar
JPH05192104A (en) Method for preparing precooked cereale food
SE450077B (en) METHOD OF PRODUCING A NUTRITIONAL PRODUCT SIGNIFICANTLY CONSISTING OF A DEFATED SPRAYED WHEAT GROWTH
SU1829916A3 (en) Method for producing extrusion products
JP2610660B2 (en) Culture medium for mushroom cultivation
JPH0552184B2 (en)
CN1023056C (en) Method for producing instant rice flakes
WO2007123318A1 (en) Isinglass-based fine powder composition for use in the production of completely biodegradable disposable tableware
JPH05123121A (en) Instant food and its production
JPH0365147B2 (en)
JPS6130543B2 (en)
KR20190084339A (en) Process
RU2366277C2 (en) Production method of multicereal flakes
JP4236161B2 (en) Process for producing pregelatinized germinated flour
JPS61205479A (en) Preparation of koji
JPH0675473B2 (en) Method for producing puffed feed for fish farming
JPS63129956A (en) Method for producing puffed snack confectionery containing corn grits as the main ingredient
JPS62198386A (en) Production of solid 'koji'
WO2002076222A1 (en) A method for treating highland barley and its equipment
US704530A (en) Stock-food and process of making same.
JPS6049467B2 (en) instant porridge food

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees