JP2848901B2 - Sake rice processing method - Google Patents
Sake rice processing methodInfo
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- JP2848901B2 JP2848901B2 JP3905290A JP3905290A JP2848901B2 JP 2848901 B2 JP2848901 B2 JP 2848901B2 JP 3905290 A JP3905290 A JP 3905290A JP 3905290 A JP3905290 A JP 3905290A JP 2848901 B2 JP2848901 B2 JP 2848901B2
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- rice
- water
- white rice
- white
- yield
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Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は酒米の処理方法に関し、より詳細には、搗
(とう)精した白米粒面に水を接触させて白米粒面に過
剰に付着している水分を遠心分離して白米の含水率を増
加させるとともに、白米に付着している糠(ぬか)及び
残存糠層を除去する酒米処理方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for treating sake rice, and more particularly, to bringing water into contact with milled polished white rice grains to make the rice grains excessively wet. The present invention relates to a method for treating sake rice that increases the water content of white rice by centrifuging water adhering thereto and removes bran and residual bran layers adhering to white rice.
酒米は、一般的に竪型研削式精米機を数十回も循環通
過させることにより高精米度の白米に精白される。普通
の酒米は精米歩留まり50〜80%程度で精米されるが、吟
醸米では特に精米歩留まり30%程度まで精白される。そ
のため、米粒が精米機で何度も精白される間に米温が上
昇し、それに伴って含水率が低下(10〜12%程度)す
る。その含水率の低下した白米を次の洗米及び浸漬(し
んし)工程に移送すると、洗米及び浸漬工程において急
激な吸水作用により白米粒に亀裂を生じる。それは、水
に白米を浸漬すると、水分の低いものは吸水速度が早く
体積歪みが大きいために白米粒に亀裂が生じるためであ
る。その亀裂に余分な水分が吸収されて水分過剰の白米
となり、次の蒸米工程での蒸し加減が非常に難しくなる
という問題点があった。Sake rice is generally polished to white rice with a high degree of rice polishing by circulating through a vertical grinding rice mill several tens of times. Normal sake rice is polished with a milled rice yield of about 50-80%, but ginjo rice is particularly whitened with a milled rice yield of about 30%. For this reason, the rice temperature rises while the rice grains are whitened many times by a rice mill, and the water content decreases accordingly (about 10 to 12%). When the white rice with the reduced water content is transferred to the next rice washing and dipping (shinshin) step, cracks are generated in the white rice grains due to abrupt water absorption in the rice washing and dipping step. This is because, when polished rice is immersed in water, cracks occur in the polished rice grains with low moisture because the water absorption rate is high and the volume distortion is large. Excess moisture is absorbed by the cracks, resulting in white rice with excessive moisture, and there is a problem that it is very difficult to control steaming in the next steamed rice process.
本発明は、上記問題点を解消することを課題とするも
ので、白米を短時間にしかも安全に標準含水率に調質す
ることができて、そのため、蒸米工程において蒸し加減
が簡単にでき、また、短時間に白米に付着した糠と白米
に残存している糠層を剥(はく)離除去して、洗米時間
の短縮又はその不用が可能となる酒米処理方法を提供す
ることを目的とする。The present invention has been made to solve the above problems, and it is possible to refinish white rice to a standard moisture content in a short time and safely, and therefore, it is possible to easily adjust steaming in a steamed rice process, It is another object of the present invention to provide a method for treating sake rice in which rice bran and the rice bran layer remaining in the white rice are removed (stripped) and removed in a short time, thereby shortening the rice washing time or making it unnecessary. Aim.
本発明は、白米に水又は水溶液を1分以内接触させた
後、回転筒の多孔壁から、白米に付着した過剰な水を遠
心分離することにより、該処理後の白米の含水率を処理
前の含水率より1〜5%増加する、という技術的手段を
講じた。In the present invention, the water content of the white rice after the treatment is adjusted by contacting the white rice with water or an aqueous solution within 1 minute, and then centrifuging excess water adhering to the white rice from the porous wall of the rotating cylinder. Technical measures were taken to increase the water content by 1 to 5%.
更に、精米歩留80%以下の任意精米歩留りの白米に、
水を1分以内接触させた後、回転筒の多孔壁から、白米
に付着した水とともに遊離糠及び残存糠層を遠心分離す
ることにより、該処理後の白米の精米歩留まりを処理前
の精米歩留まりより低い方に進行させるにより課題解決
の手段とした。Furthermore, to white rice with optional rice yield of 80% or less,
After contacting the water within 1 minute, the free bran and the remaining bran layer are centrifuged together with the water adhering to the white rice from the porous wall of the rotating cylinder, so that the rice yield of the white rice after the treatment is reduced to the rice yield before the treatment. It was a means of solving the problem by proceeding to the lower side.
玄米に対する白米重量比率(精米歩留まり)が80%以
下の白米の粒面全体一様にごく短時間に水を付着させ
る。付着させる方法は、遠心分離機に供給する前工程に
おいて水を浸漬する方法、流動中の米粒に水を噴出する
かノズル等でミスト状の水を噴霧する方法、遠心分離機
内に米と水を供給する等適宜選択できるものである。水
で粒面全体が湿潤した白米は過剰な水分が付着してお
り、この過剰な水分は一粒についても偏在し、米粒の接
触部はさらに多くの過剰水分が偏在している。この状態
で放置すると、水分の米粒内部への吸収速度と吸収量が
米粒の部位により異なって米粒に亀裂が生じたり、米粒
が目標含水率以上に水分を吸収したりすることになるか
ら、1分以内の短時間に米粒表面に付着している過剰水
分を回転筒の多孔壁から遠心力で分離・除去し、米粒表
層部に一定量の均一な水膜を形成する。この表層部に形
成された均一な水膜は、米粒全体から均一な速度で内部
に吸収されるので亀裂が発生しない。接触時間の長さは
白米原料含水率や処理後の目標含水率により調節する必
要がある。実験によると、白米原料含水率11.5%、精米
歩留まり71.5%の白米の処理に適当な接触時間は20秒で
あった。このときの処理後は白米は含水率13.6%、歩留
り70.6%であった。また、他の実験によると、白米原料
含水率10.5%、精米歩留り51.3%の白米の処理に適当な
接触時間は20秒であった。このときの処理後の白米は含
水率13.3%、歩留り50.1%であった。Water is applied in a very short time uniformly over the whole grain surface of white rice having a white rice weight ratio of 80% or less (polished rice yield) to brown rice. The method of adhering is a method of immersing water in a pre-process of supplying to a centrifuge, a method of spraying water onto a flowing rice grain or spraying mist-like water with a nozzle or the like, a method of mixing rice and water in a centrifuge. It can be appropriately selected such as supply. Excess moisture is attached to the white rice whose entire grain surface is wetted with water, and the excess moisture is unevenly distributed even in one grain, and more excess moisture is unevenly distributed in the contact portion of the rice grains. If left in this state, the rate and amount of absorption of moisture into the rice grain will differ depending on the location of the rice grain, causing cracks in the rice grain or the rice grain absorbing moisture above the target moisture content. In a short time of less than a minute, excess water adhering to the rice grain surface is separated and removed from the porous wall of the rotary cylinder by centrifugal force to form a uniform water film on the rice grain surface layer. The uniform water film formed on the surface layer portion is absorbed into the whole rice grain at a uniform speed, so that no crack is generated. The length of the contact time needs to be adjusted according to the moisture content of the raw rice raw material and the target moisture content after the treatment. According to experiments, a suitable contact time for treating white rice having a moisture content of 11.5% and a rice yield of 71.5% was 20 seconds. After the treatment, the white rice had a moisture content of 13.6% and a yield of 70.6%. According to another experiment, a suitable contact time for treating white rice having a raw rice moisture content of 10.5% and a milled rice yield of 51.3% was 20 seconds. At this time, the treated white rice had a moisture content of 13.3% and a yield of 50.1%.
この処理方法の第2の作用は上述のとおり、精米の歩
留まりの減少、すなわち精米が行われることである。通
常の精米作用で精米された白米は精米歩留り80%内外で
あるが、表面に糠が付着するとともに米粒の一部に糠層
が残ったものがある。この白米又は精米程度の低い精米
歩留り80%までの白米の米粒表面に水を付着させると、
糠及び糠層はさらに軟らかくなり、米粒同志の軽い接触
で剥離されて過剰水分と共に分離除去される。こうし
て、洗米が短時間か不要な白米となる。As described above, the second effect of this processing method is to reduce the yield of polished rice, that is, to perform polished rice. White rice milled by normal milling action has a rice milling yield of around 80%, but some have rice bran attached to the surface and a bran layer remaining on some of the rice grains. When water is attached to the rice grain surface of this white rice or white rice up to 80%
The bran and the bran layer are further softened, peeled off by light contact between rice grains, and separated and removed together with excess moisture. In this way, the rice is washed for a short time or becomes unnecessary white rice.
本発明の実施例を図面を参照しながら説明する。 Embodiments of the present invention will be described with reference to the drawings.
第1図は本発明を実施するためのフローチャートであ
る。揚穀機1の前工程はホッパー2を介して精米機等
(図示せず)に連絡し、排出側タンク3に連絡する。揚
穀機1とタンク3との上方に吸引機4A,4Bを取付ける。
タンク3下部に設けた計量機5に米粒を間歇排出するロ
ータリーバルブ6を連結し、バルブ6は揚穀機7に連絡
し、揚穀機7の排出側を浸漬タンク8に連絡する。浸漬
タンク8内に給水管9を臨ませ、浸漬タンク8下部の排
出管10にバタフライ弁11を連絡し、バタフライ弁11はポ
ンプ12を介して送米管13に連絡している。浸漬タンク8
の上部に水位計14とオーバーフロー管15を設ける。FIG. 1 is a flowchart for carrying out the present invention. In the pre-process of the grain-lifting machine 1, a rice-milling machine (not shown) and the like are connected via a hopper 2 to a discharge-side tank 3. The suction machines 4A and 4B are mounted above the graining machine 1 and the tank 3.
A rotary valve 6 for intermittently discharging rice grains is connected to a weighing machine 5 provided at a lower portion of the tank 3, and the valve 6 is connected to a graining machine 7, and the discharge side of the graining machine 7 is connected to a immersion tank 8. A water supply pipe 9 faces the immersion tank 8, and a butterfly valve 11 is connected to a discharge pipe 10 below the immersion tank 8, and the butterfly valve 11 is connected to a rice feed pipe 13 via a pump 12. Immersion tank 8
A water level gauge 14 and an overflow pipe 15 are provided at the upper part of the tank.
送米管13を、後述する遠心分離機16に連絡し、遠心分
離機16の米排出口17は揚穀機18を介して精品タンク19に
連絡する。The rice sending pipe 13 is connected to a centrifugal separator 16 to be described later, and the rice discharge port 17 of the centrifugal separator 16 is connected to a refined product tank 19 via a graining machine 18.
本発明に使用する水は、一部循環させる構成とするこ
とが望ましく、遠心分離機16により分離・除去された水
は糠等の不要固形物を含むものであり、水排出口20は水
処理装置21の沈澱層22Aに連絡する。22A,22B,22Cは沈澱
層であり、沈澱層22Aの水が上限レベルに達すると、順
次同22B,22Cへと移動する構成とする。そして、同22Cの
中間部に設けた取出口23は流量調節弁24及びポンプ25を
介して浸漬タンク8の給水管9に連絡する。The water used in the present invention is desirably configured to be partially circulated, the water separated and removed by the centrifugal separator 16 contains unnecessary solids such as bran, and the water discharge port 20 is used for water treatment. It communicates with the precipitation layer 22A of the device 21. 22A, 22B, and 22C are sedimentation layers, and when the water in the sedimentation layer 22A reaches an upper limit level, the water is sequentially moved to the same 22B, 22C. Then, an outlet 23 provided at an intermediate portion of the immersion tank 8 communicates with the water supply pipe 9 of the immersion tank 8 via a flow control valve 24 and a pump 25.
テンパリングタンク19の一側には含水率測定器26を設
け、該含水率測定器29に設定された目標含水率と処理後
の白米含水率測定値とを比較し、両者の差が小さくなる
ように、水との接触時間、添加水量、遠心分離機の回転
数(遠心加速度)、白米供給量、水圧や水の噴射方向及
び加水位置等の組合せでフィードバック制御する制御装
置27を設ける。また、制御装置27は含水率測定器26を用
いたフィードバック制御でなく、原料白米歩留まり、原
料白米含水率及び目標白米含水率を入力し、あらかじめ
実験により作成したプログラムにより制御するプログラ
ム制御とする方法を用いてもよい。A moisture content measuring device 26 is provided on one side of the tempering tank 19, and the target moisture content set in the moisture content measuring device 29 is compared with the measured value of the white rice moisture content after the treatment, so that the difference between the two is reduced. Further, there is provided a control device 27 for performing feedback control based on a combination of the contact time with water, the amount of added water, the number of revolutions of the centrifuge (centrifugal acceleration), the supply amount of white rice, the water pressure, the jetting direction of water, and the position of water addition. In addition, the control device 27 is not a feedback control using the moisture content measuring device 26, but a method of performing a program control in which the raw rice yield, the raw rice moisture content and the target white rice moisture content are input and controlled by a program created in advance by experiments. May be used.
次に、遠心分離機16の構成について第2図を参照して
説明する。第2図において、機枠28の内部に縦軸29を回
転自在に設け、その上部に、米粒は通過しない多孔壁30
を有する回転筒31を設ける。回転筒31の上部は開放し、
下部には底板32を設ける。また、回転筒31の中心部には
下部に開口を有する案内筒33を底板32に立設し、案内筒
33の上部には供給ホッパー34に連結した供給口35を臨ま
せる。Next, the configuration of the centrifuge 16 will be described with reference to FIG. In FIG. 2, a vertical axis 29 is rotatably provided inside a machine frame 28, and a porous wall 30 through which rice grains do not pass is provided above the vertical axis 29.
Is provided. The upper part of the rotating cylinder 31 is open,
A bottom plate 32 is provided at the lower part. In addition, a guide cylinder 33 having an opening at the bottom is provided on the bottom plate 32 at the center of the rotating cylinder 31, and the guide cylinder is provided.
The supply port 35 connected to the supply hopper 34 faces the upper part of the 33.
さらに、遠心分離機16には給水装置36を設ける。給水
装置36は、水タンク37、供給ホッパー34内に給水する水
管38、及び遠心分離機16の回転筒31に向けて水を噴霧す
るためのノズル40とポンプ41とを有する水管39から構成
される。Further, the centrifuge 16 is provided with a water supply device 36. The water supply device 36 includes a water tank 37, a water pipe 38 for supplying water into the supply hopper 34, and a water pipe 39 having a nozzle 40 and a pump 41 for spraying water toward the rotating cylinder 31 of the centrifuge 16. You.
第2図において、回転筒31は上部の径が下部の径より
大きくテーパー状に構成してあり、回転筒31内に供給さ
れた米粒は、遠心力の分力で上方へ連続的に移動して連
続処理を可能としたものであり、テーパーの程度は処理
能力等考慮して実験により決定されるものであるが、間
歇処理(バッチ処理)する場合には同径若しくは下方を
大径とし、排出に際しては回転筒31の下部位に設けたシ
ャッターを開口して米粒を排出する構成が簡便である。
符号42は米温又は水温を上昇させて米粒内部への均一吸
水を助長するための温風ファンであるが、これは付加的
要素である。In FIG. 2, the rotating cylinder 31 has a tapered shape in which the upper diameter is larger than the lower diameter, and the rice grains supplied into the rotating cylinder 31 continuously move upward by the component force of the centrifugal force. The degree of taper is determined by experiment in consideration of processing capacity and the like, but in the case of intermittent processing (batch processing), the same diameter or the lower part is made larger, In discharging the rice grains, a shutter provided at a lower portion of the rotary cylinder 31 is opened to discharge the rice grains.
Reference numeral 42 denotes a hot air fan for increasing the rice temperature or the water temperature to promote uniform water absorption into the inside of the rice grains, which is an additional element.
遠心分離機は第2図に示す構成に限られるものではな
く、例えば横回転筒式遠心分離機とすれば縦型より重力
の影響が小さく、より簡単に連続処理することが可能と
なる。The configuration of the centrifuge is not limited to the configuration shown in FIG. 2. For example, if the centrifuge is a horizontal rotary cylinder type centrifuge, the influence of gravity is smaller than that of the vertical type centrifuge, so that continuous processing can be performed more easily.
次に、上記実験例の具体的作用について説明する。80
%以下の適度の精米歩留まりに精米された白米(含水率
10〜20%程度)を揚穀機1のホッパー2から供給し、タ
ンク3へ一時貯留する。タンク3下部に設けた計量器5
によって一定重量を計量して排出すると、ロータリーバ
ルブ6の回転により一定流量に規制された白米が排出さ
れ、揚穀機7から浸漬タンク8へ投入される。浸漬タン
ク8に投入された白米重量に対し、設定された重量の水
が給水管9から供給される。そして、この水で白米表層
部全体が水と接触する。供給する水量は白米粒表面全体
を水濡れさせる量であれば足りるが、浸漬タンク8を利
用した場合は白米重量とほぼ同量の水量であったのに対
し、ここではポンプ12で流体輸送するために白米重量に
対して2倍の水量を加えた。浸漬開始から10秒後、バタ
フライ弁11を開いて白米を水と共にポンプ12によって遠
心分離機16に送ると、既に回転している遠心分離機16の
回転筒31の多孔壁30によって水が分離・除去される。短
時間の浸漬による白米と水との接触の間に、白米粒面に
付着した糠の溶出、白米に残存している糠層の剥離及び
遊離脂肪酸の溶出が水と遠心分離の働きにより生じ、水
と共に回転筒31外に分離除去され、また、白米の含水率
が15%程度に調質される。遠心分離機16内を20〜30秒の
短時間で通過した白米は、米排出口17から揚穀機18を介
してテンパリングタンク19へと輸送される。テンパリン
グタンク19に設けた含水率測定器26により該処理後の白
米の含水率を測定する。Next, a specific operation of the experimental example will be described. 80
% Of white rice (water content)
(About 10 to 20%) from the hopper 2 of the fryer 1 and temporarily stored in the tank 3. Measuring device 5 provided under tank 3
When a constant weight is measured and discharged, the white rice regulated at a constant flow rate by the rotation of the rotary valve 6 is discharged, and is put into the immersion tank 8 from the graining machine 7. Water of a set weight is supplied from a water supply pipe 9 with respect to the weight of the white rice put into the immersion tank 8. Then, the whole surface layer of the white rice comes into contact with the water. The amount of water to be supplied is sufficient as long as it wets the entire surface of the white rice grains. However, when the immersion tank 8 is used, the amount of water is almost the same as the weight of the white rice. For this purpose, twice the amount of water was added to the white rice weight. After 10 seconds from the start of the immersion, the butterfly valve 11 is opened and the white rice is sent to the centrifugal separator 16 together with the water by the pump 12, and water is separated by the porous wall 30 of the rotating cylinder 31 of the centrifugal separator 16 already rotating. Removed. During the contact between white rice and water by immersion for a short time, elution of bran attached to the white rice grain surface, exfoliation of the bran layer remaining in white rice, and elution of free fatty acids occur by the action of water and centrifugation, The water is separated and removed from the rotary cylinder 31 together with the water, and the moisture content of the white rice is refined to about 15%. White rice that has passed through the centrifugal separator 16 in a short time of 20 to 30 seconds is transported from the rice discharge port 17 to the tempering tank 19 through the graining machine 18. The moisture content of the treated white rice is measured by a moisture content measuring device 26 provided in the tempering tank 19.
なお、含水率測定器26には電気抵抗式、電気容量式又
は光学式のものが適用できるが、白米は粒表層近くが高
水分のため、通常白米の測定の場合とは誤差を生じるの
で補正する必要がある。電気容量式で測定すると15%の
場合0.5%高い値を示した。The moisture content measuring device 26 can be an electric resistance type, an electric capacity type or an optical type. There is a need to. When measured by the capacitance method, the value was 0.5% higher at 15%.
測定された含水率と設定された含水率との差信号が制
御処理27に連絡され、制御装置27は、白米と水との接触
時間、添加水量、遠心分離機の回転速度、白米供給量、
水圧や水の噴射方向及び加水位置等を制御する。また、
処理白米の精米歩留まりを制御目標にする場合は、含水
率測定器26を白度計に置き換えて、処理後の白米の白さ
を測定し、設定白度たとえば白度43%と比較し、その差
を信号として制御装置27に連絡して上記同様の制御を行
う。The difference signal between the measured moisture content and the set moisture content is communicated to the control processing 27, and the control device 27 controls the contact time between the white rice and water, the amount of added water, the rotation speed of the centrifuge, the white rice supply amount,
Controls water pressure, water spray direction, water addition position, and the like. Also,
When controlling the rice yield of the treated white rice as a control target, the moisture content measuring device 26 is replaced with a whiteness meter, the whiteness of the processed white rice is measured, and the whiteness is compared with a set whiteness of, for example, 43%. The difference is transmitted as a signal to the control device 27 to perform the same control as described above.
以上の工程は遠心分離機外で白米と水とをあらかじめ
接触させたものであるが、第2図に示すように、適度に
精米された白米を供給ホッパー34に供給すると同時にそ
の白米に、水管38から水を噴出して接触させ、回転筒31
に供給して水を分離除去する方法、また、供給ホッパー
34から白米を供給し、回転筒31の内部に設けたノズルか
ら高圧の水滴又はミスト状の水分を噴霧する方法を適宜
選択・組合わせることができる。In the above process, white rice and water are brought into contact in advance outside the centrifugal separator. As shown in FIG. 2, the white rice that has been appropriately milled is supplied to the supply hopper 34, and at the same time, water is supplied to the white rice. Spout water from 38 and bring it into contact, rotating cylinder 31
Method for separating and removing water by supplying water to the feed hopper
A method of supplying white rice from 34 and spraying high-pressure water droplets or mist-like water from a nozzle provided inside the rotary cylinder 31 can be appropriately selected and combined.
上記実施例は連続処理について説明したが、回転筒を
略垂直にすると間歇式遠心分離が可能となり、作用・効
果は同じであるが小能力の処理に適する。In the above embodiment, the continuous processing is described. However, if the rotating cylinder is made substantially vertical, intermittent centrifugal separation becomes possible, and the operation and effect are the same, but the processing is suitable for small capacity processing.
以上のように本発明の酒米処理方法によると、白米に
水又は水溶液を1分以内接触させた後、回転筒の多孔壁
から、白米に付着した過剰な水を遠心分離することによ
り、該処理後の白米の含水率を処理前の含水率より1〜
5%増すことができて適正な含水率となり、浸漬工程に
おいて白米粒に亀裂が生じない。そのため、蒸米工程で
の蒸し加減が極めて簡単に行うことができる。また、精
米歩留り80%以下の白米を供給して処理すると付着糠の
溶出、残存糠層の剥離及び遊離脂肪酸の溶出などのため
精米を進行させ、完全に洗米した白米と同じように不要
物を除去して白度も高くなり、更に、標準的水分のため
保存性もよく、洗米時間の短縮又は洗米を要しない白米
を得ることができる等格別の効果を奏するものである。As described above, according to the sake rice processing method of the present invention, after bringing water or an aqueous solution into contact with white rice within one minute, the excess water adhering to the white rice is centrifuged from the porous wall of the rotating cylinder, whereby the rice is treated. The moisture content of the white rice after the treatment is 1 to
The water content can be increased by 5% and the moisture content becomes appropriate, and cracks do not occur in the white rice grains in the dipping process. Therefore, steaming in the steamed rice process can be performed very easily. In addition, when supplying and processing white rice with a milled rice yield of 80% or less, the milled rice proceeds due to elution of adhered bran, peeling of the remaining bran layer and elution of free fatty acids, and unnecessary substances are removed in the same manner as completely washed rice. By removing it, the whiteness is increased, and furthermore, it has excellent preservability due to the standard water content, and has a special effect such as shortening of rice washing time or obtaining white rice that does not require rice washing.
第1図は本発明のフローチャート、第2図は本発明の一
部を構成する遠心分離機の一実施例を示す正面縦断面図
である。 1……揚穀機、2……ホッパー、3……タンク、4A,4B
……吸引機、5……計量機、6……ロータリーバルブ、
7……揚穀機、8……浸漬タンク、9……給水管、10…
…排出管、11……バタフライ弁、12……ポンプ、13……
送米管、14……水位計、15……オーバーフロー管、16…
…遠心分離機、17……米排出口、18……揚穀機、19……
テンパリングタンク、20……水液排出口、21……水溶処
理装置、22A,22B,22C……沈澱槽、23……取出口、24…
…流量調節弁、25……ポンプ、26……含水率測定器、27
……制御装置、28……機枠、29……縦軸、30……多孔
壁、31……回転筒、32……底板、33……案内筒、34……
供給ホッパー、35……供給口、36……給水装置、37……
水タンク、38……水管、39……水管、40……ノズル、41
……ポンプ。FIG. 1 is a flow chart of the present invention, and FIG. 2 is a front vertical sectional view showing an embodiment of a centrifuge constituting a part of the present invention. 1 ... Frying machine, 2 ... Hopper, 3 ... Tank, 4A, 4B
…… Suction machine, 5… Measuring machine, 6… Rotary valve,
7 ... Frying machine, 8 ... Immersion tank, 9 ... Water pipe, 10 ...
... Drain pipe, 11 ... Butterfly valve, 12 ... Pump, 13 ...
U.S.A. pipe, 14 ... Water gauge, 15 ... Overflow pipe, 16 ...
... Centrifuge, 17 ... Rice outlet, 18 ... Frying machine, 19 ...
Tempering tank, 20… Water liquid outlet, 21… Aqueous solution treatment equipment, 22A, 22B, 22C …… Precipitation tank, 23 …… Outlet, 24…
… Flow control valve, 25… Pump, 26 …… Moisture content measuring instrument, 27
………………………………………………………………………………………………………………………………………………………………………………….
Supply hopper, 35 ... Supply port, 36 ... Water supply device, 37 ...
Water tank, 38 ... water pipe, 39 ... water pipe, 40 ... nozzle, 41
……pump.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭59−71679(JP,A) 特開 昭60−160880(JP,A) 特開 昭60−210975(JP,A) 実開 昭51−101153(JP,U) (58)調査した分野(Int.Cl.6,DB名) C12G 3/02 119 A23L 1/105──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-59-71679 (JP, A) JP-A-60-160880 (JP, A) JP-A-60-210975 (JP, A) 101153 (JP, U) (58) Field surveyed (Int. Cl. 6 , DB name) C12G 3/02 119 A23L 1/105
Claims (3)
の多孔壁から、白米に付着した過剰な水を遠心分離する
ことにより、該処理後の白米の含水率を処理前の含水率
より1〜5%増加することを特徴とする酒米処理方法。1. After contacting white rice with water for less than 1 minute, excess water adhering to the white rice is centrifuged from the porous wall of the rotating cylinder to reduce the water content of the white rice before the treatment. A method for treating sake rice, comprising increasing the water content by 1 to 5%.
に、水又は水溶液を1分以内接触させた後、回転筒の多
孔壁から、白米に付着した水とともに遊離糠及び残存糠
層を遠心分離することにより、処理後の白米の精米歩留
まりを処理前の精米歩留りより低い方に進行させること
を特徴とする酒米処理方法。2. A method in which water or an aqueous solution is brought into contact with white rice at an optional rice yield of 80% or less at a rice yield of not more than 1 minute, and then the free bran and the remaining bran layer together with water adhering to the white rice from the porous wall of the rotating cylinder. And a centrifugal separation of the rice to make the milled rice yield of the processed white rice lower than the milled rice yield before the processing.
米に、水又は水溶液を1分以内接触させた後、回転筒の
多孔壁から、白米に付着した過剰な水を分離し、該処理
後の白米の含水率を処理前の含水率より1〜5%増加さ
せるとともに、前記水に遊離糠及び残存糠層を溶出させ
て処理後の白米の精米歩留りを処理前の精米歩留りより
低い方に進行させることを特徴とする酒米処理方法。3. After contacting water or an aqueous solution within 1 minute with white rice having an optional rice yield of 80% or less, the excess water adhering to the white rice is separated from the porous wall of the rotating cylinder. The moisture content of the white rice after the treatment is increased by 1 to 5% from the moisture content before the treatment, and the free rice and the remaining rice bran layers are eluted in the water so that the rice yield of the white rice after the treatment is lower than the rice yield before the treatment. A rice processing method characterized by proceeding to a step.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3905290A JP2848901B2 (en) | 1990-02-19 | 1990-02-19 | Sake rice processing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3905290A JP2848901B2 (en) | 1990-02-19 | 1990-02-19 | Sake rice processing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03240476A JPH03240476A (en) | 1991-10-25 |
JP2848901B2 true JP2848901B2 (en) | 1999-01-20 |
Family
ID=12542360
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3905290A Expired - Fee Related JP2848901B2 (en) | 1990-02-19 | 1990-02-19 | Sake rice processing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2848901B2 (en) |
-
1990
- 1990-02-19 JP JP3905290A patent/JP2848901B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH03240476A (en) | 1991-10-25 |
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