JPS5911150A - Method for steaming hard grain - Google Patents

Method for steaming hard grain

Info

Publication number
JPS5911150A
JPS5911150A JP57120523A JP12052382A JPS5911150A JP S5911150 A JPS5911150 A JP S5911150A JP 57120523 A JP57120523 A JP 57120523A JP 12052382 A JP12052382 A JP 12052382A JP S5911150 A JPS5911150 A JP S5911150A
Authority
JP
Japan
Prior art keywords
grains
steaming
water
steam
hard
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP57120523A
Other languages
Japanese (ja)
Inventor
Wakio Araki
荒木 和鬼夫
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.)
NAGATA JOZO KIKAI KK
Original Assignee
NAGATA JOZO KIKAI KK
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 NAGATA JOZO KIKAI KK filed Critical NAGATA JOZO KIKAI KK
Priority to JP57120523A priority Critical patent/JPS5911150A/en
Publication of JPS5911150A publication Critical patent/JPS5911150A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To carry out the complete steaming of hard grains to absorb water uniformly even to the core parts of the hard grains, by primarily steaming the hard grains previously absorbing water with steam on an air-permeable conveyor, sprinkling the grains with water under agitation, and regularly steaming the grains with steam. CONSTITUTION:Grains having the hard property are previously subjected to the water absorption, deposited on an air-permeable conveyor 3 and transferred. In the process, steam generated from steam generating chambers (a) and (b) is fed to a layer 10 of the grains for 10-15min to carry out the primary steaming of the grains. An agitating apparatus 4 is then rotated to agitate and finely divide the grains, which are sprinkled uniformly with water from a water sprinkling nozzle 5. The sprinkled grains are kept in the state in a part (c) without generating steam for 4-10min. During the time, adhesive moisture on the grain surfaces is absorbed to the core parts thereof. The grains are then regularly steamed with steam in the same way as in the primary steaming on steam generating chambers (d)-(f) for 15-20min. Thus, a given amount of water according to the purpose of use is uniformly absorbed even to the core parts of the hard grains and carry out the complete steaming.

Description

【発明の詳細な説明】 この発明は吸水困難な硬質穀類に芯部にまで均一に吸水
させて完全蒸煮を行なわぜる方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for completely steaming hard grains that are difficult to absorb water by uniformly absorbing water down to the core.

従来硬質穀類の性状はその程度に差はあるが穀類の種類
、産地の別、或いは貯蔵期間等を起因とし、一度の浸漬
処理では粒子の芯部迄均−に吸水できず、浸漬処理後−
次蒸煮を行ない、更に浸漬或いは撒水して穀類の芯部迄
吸水させ、再度蒸煮工程を経て芯部まで蒸煮を行なうの
が通例であった。しかしながらかような手段で(′i。
Conventionally, the properties of hard grains vary depending on the type of grain, production area, storage period, etc., and a single soaking treatment cannot absorb water evenly to the core of the grain, and after soaking, water cannot be evenly absorbed.
It was customary to perform a second steaming, then soak or sprinkle water to absorb water to the core of the grain, and then go through the steaming process again to steam the grain to the core. However, by such means ('i.

撒水吸水の工程において吸水に計画性及び均一性がな(
、また穀類の種類、状態及び使用目的により撒水量はそ
れぞれ異るため、浸漬撒水による吸水では穀類余計に使
用目的の水分を均一に与えることすなわち補給水量の調
整を行なうことは技術的に困難であった。
In the water sprinkling and water absorption process, water absorption is not well planned and uniform (
Also, since the amount of water applied varies depending on the type, condition, and purpose of use of the grain, it is technically difficult to uniformly give the grain additional moisture for the purpose of use, that is, adjust the amount of supplementary water, by soaking and watering. there were.

この発明は、上述のような欠点゛を排除し、理論的に硬
質穀類の芯部まで使用目的による所定辰の水分を均一に
吸水させて蒸釜?虱処理を行なう方法である。・ この発明の方法における硬質穀類としての対象物は古米
、外米、麦その他の硬質穀類を含むが、こ又では味噌原
料としての硬質米を例に掲げて説明する。古米或いは外
米は種類、産地により異なるが硬質米としての性状を有
するため吸水性が悪い。これら硬質米(以下単に穀類と
称す。)の処理としては、穀類をあらかじめ浸漬して所
定の吸水処理を行なうが、この工程での吸水率は23〜
24%であり、この水分で本蒸しの処理を施しても使用
目的に合致した水分とはならない0.この発明はあらか
じめ吸水処理した穀類を、通気性を有する搬送体上に堆
積し、穀類層等新規の蒸気、或も・は蒸気加熱機によっ
て蒸總に適切な温度、水分とした角生蒸気な供給して穀
類と接触させ、相互熱交換によりドレン化と共に蒸米に
吸収されて蒸米の温度は逐次−1−昇する。そして堆積
厚によっても異なるが10〜15分の時間で蒸気は堆積
層を吹き抜は吸水しやすい状態となる。
This invention eliminates the above-mentioned drawbacks, and theoretically allows the core of hard grains to uniformly absorb a predetermined amount of water depending on the purpose of use. This is a method of treating lice. - Target objects as hard grains in the method of this invention include old rice, foreign rice, barley, and other hard grains, but in Komata, hard rice as a raw material for miso will be used as an example for explanation. Old rice or foreign rice differs depending on the type and region of production, but because it has properties as hard rice, it has poor water absorption. To process these hard rice (hereinafter simply referred to as grains), the grains are soaked in advance and subjected to a specified water absorption treatment, but the water absorption rate in this process is 23~
The moisture content is 24%, and even if this moisture is subjected to the main steaming process, the moisture content will not meet the purpose of use. In this invention, grains that have been treated with water absorption in advance are piled up on a conveyor with air permeability, and a new steam such as a grain layer is heated, or a steam heating machine is used to heat the grains to an appropriate temperature and moisture for steaming. It is supplied and brought into contact with the grains, and through mutual heat exchange, it is absorbed into the steamed rice as well as drained, and the temperature of the steamed rice increases by -1-. Although it varies depending on the thickness of the deposit, the steam reaches a state where it is easy to absorb water through the deposited layer in the atrium after 10 to 15 minutes.

こ〜で撒水を行なうが、穀類の量と不足水分給水量との
相対比の給水ができても、蒸煮中・穀類が一度蒸しの完
了時点で凝固した状態にあるため、堆積層の上部、中部
及び下部の各粒子の吸水は不均一となり、いわゆる均−
蒸しの醸成は不可能である。そこで均一吸水を行なわせ
るため、穀類層に攪拌作用を与えて細分化し穀類の品質
及び使用目的に応じた補給水を蒸煮穀類に均一に液体又
は水を撒水して、穀類の処理条件により4〜IO分その
ま〜の状態に置き、粒子表面の剛着水分を徐々に吸水さ
せて芯部迄均−に吸水させ、吸水工程を完了する。均−
吸水完了後再び一次蒸しと同様に蒸気を15〜20分供
給して蒸釘披を行ない、蒸し上り水分を目的水分に均一
にする。実施例では一度蒸し、不足水分の均一−吸水、
本蒸しの工程を連続蒸煮となり得るように構成されてい
るので、従来のような一度蒸し、浸漬(撒水)及び本蒸
しの断続的な穀類の蒸煮作業を理論的、連続的に行なう
ことができ、しかも品質向上、省力、省エネルギに関し
ても大きな貢献をすることができるものである。
Water is sprinkled here, but even if water is supplied in the relative ratio between the amount of grains and the water shortage, the upper part of the sedimentary layer, The water absorption of each particle in the middle and bottom becomes uneven, so-called uniformity.
Steaming is impossible. Therefore, in order to achieve uniform water absorption, the grain layer is subdivided by stirring, and liquid or water is uniformly sprinkled on the steamed grains depending on the quality of the grains and the purpose of use. The particles are left in the same state for IO minutes to gradually absorb the moisture that adheres to the surface of the particles and evenly absorb water to the core, thereby completing the water absorption process. Average
After water absorption is completed, steam is supplied again for 15 to 20 minutes in the same way as in the primary steaming, and steaming is performed to uniformize the steamed moisture to the target moisture content. In the example, steaming is carried out once, the lack of moisture is uniformly absorbed,
Since the main steaming process is configured to be continuous steaming, it is possible to theoretically and continuously perform the conventional steaming, soaking (water sprinkling), and intermittent main steaming of grains. Moreover, it can make a significant contribution to quality improvement, labor saving, and energy saving.

なお前述した撒水量は蒸しの使用目的、穀類の品質等に
よって調整を行なうが、基本的には撒水量は次式によっ
て算出する。
The above-mentioned amount of water to be sprinkled is adjusted depending on the purpose of steaming, the quality of the grain, etc., but basically the amount of water to be sprinkled is calculated using the following formula.

撒水量/毎時=蒸し上り水分−(浸漬水分十蒸4熾時吸
水分)十処理原穀量/毎時×2この撒水量と穀類とを一
定比率に均一にするのである。
Amount of water sprayed/hourly = Moisture after steaming - (Soaked water 10 Steamed 4 Moisture absorbed during heating) 10 Amount of raw grain processed/hourly x 2 The amount of water sprinkled and the grains are made uniform at a constant ratio.

上記は例として味噌原料としての穀類を対象に説明した
が、この処理法によれば一度の浸漬工程で吸水しきれな
い、すなわち不足水分補給を必要とする古米、外米、麦
等の処理に対して大きな効果を奏し、更に醸造用として
、或(・は飯米用としてその使用目的に応じた蒸し」ニ
リ水分例として製麹用として37〜40チ、飯米用とし
て50〜60%等に任意調整することができる。
The above explanation was given as an example for grains used as raw materials for miso, but this treatment method can also be used to treat old rice, foreign rice, barley, etc. that cannot absorb enough water in one soaking process, that is, require replenishment of insufficient moisture. It has a great effect on steaming and steaming depending on the purpose of use, such as for brewing or for cooking rice.For example, the moisture content can be adjusted to 37-40% for making koji, 50-60% for rice, etc. Can be adjusted.

上記した蒸煮方法を実施する装置としては、通気性を有
するパンチング板、或いはネットコンベア等により構成
される蒸煮装置が種々考えられる。
As the apparatus for carrying out the above-mentioned steaming method, various steaming apparatuses including a punching plate having air permeability, a net conveyor, etc. can be considered.

図面に示されているものはネットコンベアにより構成さ
れた一実施例であって、図中1.は蒸煮装置本体、2は
本体内に設けられた回転ドラムで、2′は駆動装置であ
る。3は回転ドラムに捲回されたネットコンベアで、コ
ンベア3上に攪拌装置4、撒水ノツズル5が設けられ、
流量側6、パルプ6′によって調整される11、a、b
What is shown in the drawing is one embodiment constructed by a net conveyor, and in the drawing, 1. 2 is a rotating drum provided in the main body, and 2' is a driving device. 3 is a net conveyor wound around a rotating drum, and a stirring device 4 and a water sprinkling nozzle 5 are provided on the conveyor 3.
Flow rate side 6, regulated by pulp 6' 11, a, b
.

d、e、lはネットコンベアの下位に接して設けられた
蒸気発生室で、バルブa’ l b’ + d’ 、e
′。
d, e, l are steam generation chambers installed in contact with the lower part of the net conveyor, and valves a' l b' + d', e
'.

r′により調整される。Cは攪拌装置4、ノズル5で均
一に撒水された水分を吸水する工程である。また排風機
7で吸引された蒸気は、他の熱源で加熱される蒸気加熱
機8を経由し前段側に供給される。熱源の調整はバルブ
8′で行なう。
It is adjusted by r'. C is a step of absorbing water uniformly sprayed by the stirring device 4 and the nozzle 5. Further, the steam sucked in by the exhaust fan 7 is supplied to the front stage side via a steam heater 8 heated by another heat source. The heat source is adjusted by valve 8'.

なお、9はホッパ、10は蒸煮資料、11は排風機、1
2は蒸気の遮断板、13は出口である。
In addition, 9 is a hopper, 10 is a steaming material, 11 is an exhaust fan, 1
2 is a steam shielding plate, and 13 is an outlet.

上記の構成において、浸漬吸水した穀類をホッパ9に投
入すると、駆動装置2′で駆動されるネットコンベア3
上に一定厚さに堆積されて出口13の方向に搬送される
。搬送される間にネットコンベア3の下位に設けられた
蒸気発生室a。
In the above configuration, when the soaked and water-absorbed grains are put into the hopper 9, the net conveyor 3 driven by the drive device 2'
It is deposited on top to a constant thickness and transported in the direction of the outlet 13. A steam generation chamber a is provided below the net conveyor 3 during transportation.

bから発生する蒸気の供給を受け、蒸気は穀類と接触し
相互熱交換によりドレン化し、蒸米に吸収されて蒸米の
温度は逐次上昇し、10〜15分要して蒸気室a、bを
通過し堆積層を吹き抜ける。穀類は約100℃近くの温
度に達し最も吸水しやすい状態となる。こ又で撒水、吸
水させるが蒸し米は凝固した状態にあるため、穀類と不
足水分給水量との相対比の給水ができても、堆積層の上
部、中部、下部の各粒子の吸水は不均一となるため攪拌
装置4を回転させて攪拌作用を与えて細分化し撒水ノズ
ル5で均一に撒水し、蒸気発生のない0部で4〜10分
間そのま又の状態を維持させ、その間に粒子表面の耐着
水分を芯部迄吸水させる。この場合給水量は穀類の種類
、蒸し上りの目的水分によって、その都度前記計算式か
ら算出して給水量を設定し、均一給水ができ得ろように
攪拌装置4、撒水ノズル5、流歇計6、バルブ6′等に
より構成される。その後芯部まで均一に吸水した穀類は
蒸気発生室dlC1f上を15〜20分要して搬送され
る間に蒸され、出口13に到達したときは完全な計画水
分に蒸煮されているのである。
Receiving the steam generated from b, the steam contacts the grains and becomes drain through mutual heat exchange, is absorbed by the steamed rice, and the temperature of the steamed rice rises gradually, and it takes 10 to 15 minutes to pass through the steam chambers a and b. It blows through the sedimentary layer. Cereals reach a temperature of about 100°C and are in a state where they are most likely to absorb water. Water is sprinkled and absorbed in the komata, but since the steamed rice is in a coagulated state, even if water is supplied in the relative ratio of the grain to the water shortage, the water absorption of each particle in the upper, middle, and lower part of the sedimentary layer is insufficient. In order to achieve uniformity, the agitator 4 is rotated to give a stirring action to the particles, which are then uniformly sprinkled with water by the water sprinkling nozzle 5, and the state is maintained for 4 to 10 minutes at 0 parts without steam generation, during which time the particles are Absorb moisture on the surface to the core. In this case, the amount of water to be supplied is calculated from the above formula depending on the type of grain and the desired moisture content after steaming, and the amount of water to be supplied is determined each time. , valve 6', etc. Thereafter, the grains that have uniformly absorbed water to the core are steamed while being conveyed over the steam generation chamber dlC1f for 15 to 20 minutes, and when they reach the outlet 13, they have been steamed to the desired moisture content.

また蒸?夕を作業において蒸gに供給された余剰蒸気は
、従前機外に放出されることを普通としたが、その余剰
蒸気は未だ多量の熱量を含み蒸す強熱源として役立つも
のである。蒸雌作業の後段における余剰蒸気は未だ95
〜97℃の温度を有しおり、この蒸気を排風機7で吸引
し、前段蓋+r1作業に供給する導入管の過程に蒸気加
熱機8を配設して、他の熱源により前段蒸しに最適な温
度に加熱調整(パルプ8′で調整する)して供給する。
Steamed again? In the past, surplus steam supplied to the steamer during evening work was normally discharged outside the machine, but the surplus steam still contains a large amount of heat and serves as a strong heat source for steaming. Surplus steam in the latter stages of steaming work is still 95%
The steam has a temperature of ~97°C, and a steam heater 8 is installed in the process of the inlet pipe to suck this steam with the exhaust fan 7 and supply it to the front stage lid + r1 operation, and to use other heat sources to create the optimal steam for the front stage steaming. The temperature is adjusted (adjusted with pulp 8') and supplied.

余剰蒸気と目的温度との差が5〜8℃のため加熱調整す
る蒸気量も非常に少なく、当初から新規の蒸気を供給す
る場合に比較し、はるかに省エネルギが計れる有益有用
なものである。前段に供給された蒸気は前述したように
蒸p張の役目を果して排風機11に吸引され機外に排出
される。
Since the difference between the surplus steam and the target temperature is 5 to 8 degrees Celsius, the amount of steam to be heated and adjusted is very small, and compared to supplying new steam from the beginning, it is a beneficial and useful method that can save much energy. . As described above, the steam supplied to the previous stage serves as a vaporizer, is sucked into the exhaust fan 11, and is discharged outside the machine.

なお、新規蒸気はA、Bから供給し、Cからは撒水用の
液或いは清水を供給するのである。
Note that fresh steam is supplied from A and B, and water spraying liquid or fresh water is supplied from C.

【図面の簡単な説明】[Brief explanation of drawings]

添付図面はこの発明の方法を実施するに適する装置の賢
所面図である。 なお図において 1 蒸煮装置本体   2 回転ドラム2′ 駆動装置
     3 ネットコンベア4 攪拌袋R8撒水ノズ
ル 6 流量計      6′ バルブ 7 排風機      8 蒸気加熱機9 ホッパ  
    】0 蒸煮資料+I  排風機      1
2  遮断板13  出口           であ
る。 特許出願人  永田醸造機械株式会社
The accompanying drawing is a top view of an apparatus suitable for carrying out the method of the invention. In addition, in the figure 1 Steaming device body 2 Rotating drum 2' Drive device 3 Net conveyor 4 Stirring bag R8 Water spray nozzle 6 Flow meter 6' Valve 7 Exhaust fan 8 Steam heater 9 Hopper
]0 Steaming materials +I Exhaust fan 1
2 blocking plate 13 exit. Patent applicant Nagata Brewing Machinery Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 硬質の性状を有する穀類にあらかじめ吸水処理を施して
通気性搬送体上に堆積し、移行させる間において蒸気或
いは蒸気加熱機による再生蒸気を堆積した穀類層に10
〜15分間供給して一次蒸しを行ない、次いで前記穀類
に所定計の液体を攪拌撒水して4〜10分経過させ、均
一に吸水させた後再び一次蒸しと同様に蒸気を15〜2
0分供給して本蒸しを行なうようにしたことを特徴とす
る硬質穀類の蒸煮方法。
Grains having hard properties are subjected to water absorption treatment in advance and deposited on an air permeable carrier, and during transfer, steam or regenerated steam from a steam heater is applied to the deposited grain layer for 10 minutes.
First steaming is carried out by supplying the grains for ~15 minutes, then stirring and sprinkling a predetermined amount of liquid on the grains, allowing 4 to 10 minutes to pass, allowing water to be evenly absorbed, and then steaming again for 15 to 2 minutes in the same manner as in the primary steaming.
A method for steaming hard grains, characterized in that main steaming is performed by supplying the grains for 0 minutes.
JP57120523A 1982-07-13 1982-07-13 Method for steaming hard grain Pending JPS5911150A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57120523A JPS5911150A (en) 1982-07-13 1982-07-13 Method for steaming hard grain

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57120523A JPS5911150A (en) 1982-07-13 1982-07-13 Method for steaming hard grain

Publications (1)

Publication Number Publication Date
JPS5911150A true JPS5911150A (en) 1984-01-20

Family

ID=14788359

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57120523A Pending JPS5911150A (en) 1982-07-13 1982-07-13 Method for steaming hard grain

Country Status (1)

Country Link
JP (1) JPS5911150A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6170949A (en) * 1984-09-14 1986-04-11 Takeshi Sugimura Method and apparatus for continuous steaming and cooking of rice
JPS6211415A (en) * 1986-07-16 1987-01-20 株式会社ヰセキエンジニアリング Steam rice cooking apparatus
JPS6211419A (en) * 1986-07-16 1987-01-20 アイセック株式会社 Steam rice cooking apparatus
JPS6211417A (en) * 1986-07-16 1987-01-20 株式会社ヰセキエンジニアリング Steam rice cooking apparatus
JPS6211416A (en) * 1986-07-16 1987-01-20 株式会社ヰセキエンジニアリング Steam rice cooking apparatus
JPS6211420A (en) * 1986-07-16 1987-01-20 株式会社ヰセキエンジニアリング Steam rice cooking apparatus
US6035764A (en) * 1998-08-14 2000-03-14 Showa Sangyo Co., Ltd. Rice processing apparatus with continuously steaming and boiling
US6056986A (en) * 1998-08-14 2000-05-02 Showa Sangyo Co., Ltd. Method and apparatus for continuously steaming and boiling rice

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6170949A (en) * 1984-09-14 1986-04-11 Takeshi Sugimura Method and apparatus for continuous steaming and cooking of rice
JPS6348502B2 (en) * 1984-09-14 1988-09-29 Iseki Fuuzu Enjiniaringu Kk
JPS6211417A (en) * 1986-07-16 1987-01-20 株式会社ヰセキエンジニアリング Steam rice cooking apparatus
JPS6211419A (en) * 1986-07-16 1987-01-20 アイセック株式会社 Steam rice cooking apparatus
JPS6211416A (en) * 1986-07-16 1987-01-20 株式会社ヰセキエンジニアリング Steam rice cooking apparatus
JPS6211420A (en) * 1986-07-16 1987-01-20 株式会社ヰセキエンジニアリング Steam rice cooking apparatus
JPS6211415A (en) * 1986-07-16 1987-01-20 株式会社ヰセキエンジニアリング Steam rice cooking apparatus
JPH055489B2 (en) * 1986-07-16 1993-01-22 Iseki Foods Eng Kk
JPH055490B2 (en) * 1986-07-16 1993-01-22 Iseki Foods Eng Kk
JPH0510931B2 (en) * 1986-07-16 1993-02-12 Iseki Foods Eng Kk
JPH0512928B2 (en) * 1986-07-16 1993-02-19 Iseki Foods Eng Kk
JPH0512929B2 (en) * 1986-07-16 1993-02-19 Iseki Foods Eng Kk
US6035764A (en) * 1998-08-14 2000-03-14 Showa Sangyo Co., Ltd. Rice processing apparatus with continuously steaming and boiling
US6056986A (en) * 1998-08-14 2000-05-02 Showa Sangyo Co., Ltd. Method and apparatus for continuously steaming and boiling rice
US6101926A (en) * 1998-08-14 2000-08-15 Showa Sangyo Co., Ltd. Rice processing apparatus with continuously steaming and boiling

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