JPH1176841A - Vacuum conditioning treatment method and apparatus of grain stock - Google Patents
Vacuum conditioning treatment method and apparatus of grain stockInfo
- Publication number
- JPH1176841A JPH1176841A JP9251433A JP25143397A JPH1176841A JP H1176841 A JPH1176841 A JP H1176841A JP 9251433 A JP9251433 A JP 9251433A JP 25143397 A JP25143397 A JP 25143397A JP H1176841 A JPH1176841 A JP H1176841A
- Authority
- JP
- Japan
- Prior art keywords
- vacuum
- water
- wheat
- grain
- water treatment
- 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
Links
- 238000011282 treatment Methods 0.000 title claims abstract description 106
- 238000000034 method Methods 0.000 title claims abstract description 55
- 230000003750 conditioning effect Effects 0.000 title claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 183
- 235000013339 cereals Nutrition 0.000 claims abstract description 59
- 238000003801 milling Methods 0.000 claims abstract description 23
- 230000008859 change Effects 0.000 claims abstract description 13
- 230000007246 mechanism Effects 0.000 claims abstract description 9
- 241000209140 Triticum Species 0.000 claims description 134
- 235000021307 Triticum Nutrition 0.000 claims description 134
- 238000007670 refining Methods 0.000 claims description 72
- 239000002994 raw material Substances 0.000 claims description 50
- 238000012545 processing Methods 0.000 claims description 33
- 238000003756 stirring Methods 0.000 claims description 33
- 244000068988 Glycine max Species 0.000 claims description 23
- 235000010469 Glycine max Nutrition 0.000 claims description 23
- 240000008042 Zea mays Species 0.000 claims description 19
- 235000002017 Zea mays subsp mays Nutrition 0.000 claims description 19
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 claims description 16
- 235000005822 corn Nutrition 0.000 claims description 16
- 235000009419 Fagopyrum esculentum Nutrition 0.000 claims description 9
- 235000007164 Oryza sativa Nutrition 0.000 claims description 9
- 235000009566 rice Nutrition 0.000 claims description 9
- 235000013305 food Nutrition 0.000 claims description 5
- 238000007654 immersion Methods 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 239000000356 contaminant Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 240000008620 Fagopyrum esculentum Species 0.000 claims 2
- 240000007594 Oryza sativa Species 0.000 claims 2
- 238000004378 air conditioning Methods 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 241000894006 Bacteria Species 0.000 abstract description 7
- 238000009434 installation Methods 0.000 abstract description 4
- 235000013312 flour Nutrition 0.000 abstract description 2
- 238000013019 agitation Methods 0.000 abstract 2
- 230000001143 conditioned effect Effects 0.000 abstract 1
- 238000010276 construction Methods 0.000 abstract 1
- 230000008569 process Effects 0.000 description 21
- 238000012937 correction Methods 0.000 description 15
- 238000012733 comparative method Methods 0.000 description 11
- 238000005303 weighing Methods 0.000 description 8
- 241000219051 Fagopyrum Species 0.000 description 7
- 241000209094 Oryza Species 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 6
- 244000005700 microbiome Species 0.000 description 6
- 238000005496 tempering Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000012216 screening Methods 0.000 description 5
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 4
- 230000007062 hydrolysis Effects 0.000 description 4
- 238000006460 hydrolysis reaction Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 230000032258 transport Effects 0.000 description 4
- 240000005979 Hordeum vulgare Species 0.000 description 3
- 235000007340 Hordeum vulgare Nutrition 0.000 description 3
- 235000016383 Zea mays subsp huehuetenangensis Nutrition 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 235000009973 maize Nutrition 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 235000012149 noodles Nutrition 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 208000003643 Callosities Diseases 0.000 description 2
- 206010020649 Hyperkeratosis Diseases 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 238000007666 vacuum forming Methods 0.000 description 2
- 238000009875 water degumming Methods 0.000 description 2
- 235000013527 bean curd Nutrition 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- -1 foreign matter Substances 0.000 description 1
- 235000011868 grain product Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Cereal-Derived Products (AREA)
- Adjustment And Processing Of Grains (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、麦、大豆、米、蕎
麦、トウモロコシ等の穀物原料について製粉加工を始め
として各種の食品加工を行う際に実施する穀物原料の調
質(テンパリング)処理方法およびこの処理方法におい
て使用する調質処理装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for tempering a grain raw material, which is carried out when performing various food processings such as a milling process on a raw material such as wheat, soybean, rice, buckwheat, corn and the like. And a heat treatment apparatus used in this processing method.
【0002】[0002]
【従来の技術]▲麦、大豆、米、蕎麦、ト
ウモロコシ等の穀物原料の製粉加工、麺加工、成分( 【従来の技術]麦、大豆、米、蕎麦、トウモロコシ等の
穀物原料の製粉加工、麺加工、成分(油分)抽出加工、
圧扁加工処理等の食品加工処理をするとき、良好な処理
結果を得るためには、これらの穀物原料を各種の食品加
工処理に適した物理的状態に調質する必要がある。たと
えば、小麦の原麦(以下原麦という)の製粉加工におい
ては、その前段の精選工程では異物、夾雑物、被害粒な
ど混入阻害物を精選(分離)して除去し、正常な原麦粒
を選別し、この精選した原麦粒に水分を添加し、一定時
間タンク内で調質して胚乳部に水分を浸透させ、かつ外
皮を強靭にすることによって、ロ一ル機で処理したとき
の胚乳部とふすまの分離および胚乳部の粉砕を良好にす
る必要がある。 【0003】原麦の調質処理を行うについては、水分、
温度、時間の調整が重要であり、室温において加熱せず
に原麦を自然水分以上の高水分に調質するテンパリング
(tempering)や、加熱して原麦を自然水分以上の高水分
に調質するコンディショニング(conditionig)が従来よ
り実施されている。[Prior art] ▲ Milling processing of cereal raw materials such as wheat, soybeans, rice, buckwheat, corn, noodle processing, and ingredients ([Prior art] milling processing of cereal raw materials such as wheat, soybeans, rice, buckwheat, corn, Noodle processing, ingredient (oil) extraction processing,
When performing food processing such as press processing, it is necessary to refine these cereal raw materials to a physical state suitable for various food processing in order to obtain good processing results. For example, in the milling process of raw wheat (hereinafter referred to as “raw wheat”), foreign substances, contaminants, and damaged particles such as damaged grains are carefully selected (separated) and removed in a preceding screening step, and normal raw wheat grains are removed. When water is added to the selected raw wheat grains, tempered in a tank for a certain period of time to infiltrate the moisture into the endosperm, and make the outer skin tough, and then processed with a roll machine. It is necessary to improve the separation of the endosperm and the bran and the grinding of the endosperm. [0003] For the refining of raw wheat, moisture,
It is important to adjust the temperature and time, and tempering the raw wheat to a higher moisture level than natural moisture without heating at room temperature, or heat the raw wheat to a higher moisture level than natural moisture. Conditioning has been conventionally performed.
【0004】従来の原麦の調質方法と装置の一例を、図
1にしたがって説明すると、先ず原麦を産地別、種類別
に各原麦タンク1に投入して一時貯蔵し、送出機2によ
って上部ホッパー3を経て計量機4に流入させ、製粉目
的に従って産地別、種類別の原麦の所定重量を適宜計っ
た後、これらの原麦をミキサー5に充填して所定割合に
なるように混合し、この混合した原麦を下部ホッパー6
を経て空気輸送機7によって第1精選機8、第2精選機
9、第3精選機10、第4精選機11に順次導入して、
原麦に含まれている異物、夾雑物、被害粒等の混入阻害
物を完全に除去する。One example of the conventional raw wheat refining method and apparatus will be described with reference to FIG. 1. First, raw wheat is put into each raw wheat tank 1 for each production area and type and temporarily stored. After flowing into the weighing machine 4 through the upper hopper 3 and appropriately measuring the predetermined weight of the raw wheat according to the place of production and the type according to the purpose of milling, the raw wheat is filled into the mixer 5 and mixed so as to have a predetermined ratio. Then, the mixed raw wheat is put in the lower hopper 6
, And sequentially introduced into the first screening machine 8, the second screening machine 9, the third screening machine 10, and the fourth screening machine 11 by the air transport machine 7,
Completely remove contamination inhibitors such as foreign matter, contaminants, and damaged grains contained in raw wheat.
【0005】前述の精選した原麦は自己水分9%前後
(重量)を含有しており、これを空気輸送機12によっ
て第1次加水装置(原料流量検出付)13内に搬送し、
ここで原麦の水分4%に相当する水を原麦に対して1次
加水として水槽14より添加し、コンベヤー15によっ
て原麦と均一に混合し、第1次調質タンク16内に導入
して以下の原麦の第一段階の調質処理を行う。The above-mentioned selected raw wheat contains about 9% (weight) of self-moisture and is conveyed by an air transporter 12 into a primary water-supplying device (with a raw material flow detection) 13.
Here, water equivalent to a water content of 4% of the raw wheat is added as primary water to the raw wheat from the water tank 14, mixed uniformly with the raw wheat by the conveyor 15, and introduced into the primary refining tank 16. The following first stage tempering treatment of raw wheat is performed.
【0006】すなわち、第1次調質タンク16において
原麦を大気圧下で室温で24時間程度放置(寝かし)を
して、前述した4%の1次加水の原麦に対する含浸を開
始するが、大気圧下においては24時間程度の放置によ
っては、原麦に対する十分な水分の含浸はできず、水分
の胚乳組織への浸透、粒質の軟化、外皮の強靭化はでき
ない。That is, the raw wheat is left in the primary refining tank 16 at room temperature for about 24 hours at atmospheric pressure for about 24 hours to start impregnation of the above-mentioned 4% primary water into the raw wheat. However, if left at atmospheric pressure for about 24 hours, the raw wheat cannot be sufficiently impregnated with water, and cannot penetrate water into the endosperm tissue, soften the granular material, and toughen the outer skin.
【0007】そこで、この第一段階の調質処理を行った
原麦を送出機17によって上部ホッパー18を経て計量
機19に導入して重量を計り、ミキサー20で混合して
下部ホッパー21を経て空気輸送機22によって第2次
加水装置(原料流量検出付)23内に搬送し、この第2
次加水計量槽23内に水槽24より原麦の水分2%に相
当する水を二次加水として原麦に再度添加し、コンベヤ
ー25によって原麦と均一に混合し、第2次調質タンク
26に導入して以下の原麦の第二段階の調質処理を行
う。The raw wheat subjected to the first-stage refining treatment is introduced into a weighing machine 19 via an upper hopper 18 by a feeder 17 and weighed, mixed by a mixer 20 and passed through a lower hopper 21. The water is conveyed by a pneumatic transporter 22 into a secondary water addition device (with a raw material flow rate detection) 23,
In the secondary water metering tank 23, water equivalent to 2% water content of the raw wheat is added again from the water tank 24 to the raw wheat as secondary water, mixed uniformly with the raw wheat by the conveyor 25, and the secondary refining tank 26 And the following second stage refining treatment of raw wheat.
【0008】すなわち、第2次調質タンク26に導入し
た原麦を大気圧下で室温で再び12時間程度放置して、
前述した2%の2次加水を原麦に対して含浸させ、水分
の胚乳組織への浸透、粒質の軟化、外皮の強靭化を行
い、原麦全体として14〜17%前後の水分を加水し
て、原麦の胚乳とふすまの分離および胚乳の粉砕を良好
にし、製扮に最適な物理状態に整えた後、この調質をし
た原麦を定量送出機27によってホッパー28を経て空
気輸送機29によってロール粉砕機30に搬送して公知
の原麦の製粉を行っている。That is, the raw wheat introduced into the secondary refining tank 26 is left again at room temperature under atmospheric pressure for about 12 hours,
The above-mentioned 2% secondary water is impregnated into the raw wheat to infiltrate the water into the endosperm tissue, soften the grain, and toughen the outer skin, and add about 14 to 17% of the water as the whole raw wheat. Then, the separation of the endosperm and the bran of the raw wheat and the grinding of the endosperm are improved, and the physical state optimal for the dressing is adjusted. Then, the tempered raw wheat is pneumatically transported through the hopper 28 by the quantitative feeder 27. The raw wheat is conveyed to a roll crusher 30 by a mill 29 to perform the milling of known raw wheat.
【0009】しかし、前述した従来の原麦の調質処理方
法と調質処理装置によると、原麦に対する調質処理が、
第1段階の調質処理(24時間)と第2段階調質処理
(12時間)と二段階に渡って行うことになるため、調
質処理時間が長時間(36時間)になり、作業が夜間に
渡ったり、維持管理作業も面倒になり、原麦の調質処理
効率が悪いという欠点があった。[0009] However, according to the above-mentioned conventional raw wheat refining method and refining apparatus, the refining of raw wheat is performed by:
Since the first stage refining process (24 hours) and the second stage refining process (12 hours) are performed in two stages, the refining process time is long (36 hours), and the work is There was a drawback that nighttime and maintenance work became troublesome, and the efficiency of refining the raw wheat was poor.
【0010】また、第1次調質タンク16および第2次
調質タンク26と、これらの関連機器類(各空気輸送
機、加水装置、水槽、コンベヤー等)を必要とするため
に、装置製造費用が嵩んで装置のイニシャルおよびラン
ニングコストが高価になる不都合があるばかりか、装置
全体が大型化して装置設置面積が大きくなり、スペース
エコノミーが良くないという不都合もあった。[0010] Further, since the primary refining tank 16 and the secondary refining tank 26 and their related equipment (pneumatic transporters, watering equipment, water tanks, conveyors, etc.) are required, the equipment is manufactured. In addition to the disadvantage that the cost is increased and the initial and running costs of the apparatus are high, there is also the disadvantage that the entire apparatus is enlarged, the installation area of the apparatus is increased, and the space economy is not good.
【0011】さらに、前述したように、原麦に対する調
質処理が二段階になって処理時間が長時間となり、原麦
が水を含んで調質タンクに滞留する時間が長くなるため
に、調質タンク内および原麦の表面に細菌や微生物が繁
殖して衛生面において問題を起こすこともあった。Further, as described above, the refining treatment for raw wheat is performed in two stages, resulting in a long processing time, and the time for the raw wheat to stay in the refining tank containing water becomes long. Bacteria and microorganisms may propagate in the quality tank and on the surface of raw wheat, causing problems in hygiene.
【0012】[0012]
【発明が解決しようとする課題】本発明の目的は、麦、
大豆、米、蕎麦、トウモロコシ等の穀物原料を製粉加工
等の食品加工処理をする際に行うこれらの穀物原料の調
質処理を、従来の第1段階の調質処理と第2段階の調質
処理のように二段階に渡って長時間に行うことはせず
に、一段階で支障なく行うことによって、調質処理時間
を従来の場合に比較して二分の一以下にし、調質処理時
間の短縮化を計り、処理作業の簡略化、省力化を計るも
のである。SUMMARY OF THE INVENTION An object of the present invention is to provide wheat,
The first and second-stage refining treatments of soybeans, rice, buckwheat, corn and other cereal raw materials, which are performed when food processing such as milling is performed on these cereal raw materials. Rather than performing the process in a long time over two stages as in the process, by performing it in one stage without any trouble, the refining process time is reduced to half or less compared to the conventional case, And to simplify the processing work and save labor.
【0013】また、本発明の他の目的は、前述した穀物
原料の調質処理を、従来のように第1次調質タンクと第
2次調質タンク(関連機器類等を含めて)の2セットを
使用して実施するのではなく、1セットだけで調質処理
を支障なく行うことによって、装置のイニシャルおよび
ランニングコストの低減を計るとともに、装置全体のコ
ンパクト化を計り、装置設置面積を小さくして、スペー
スエコノミーを改善することにある。Another object of the present invention is to perform the above-described refining treatment of the cereal raw material using a conventional refining tank and a secondary refining tank (including related equipment and the like). Rather than using two sets, the refining process can be performed with only one set without any trouble, thereby reducing the initial and running costs of the equipment, reducing the overall size of the equipment, and increasing the installation area of the equipment. The idea is to make it smaller and improve the space economy.
【0014】さらに、本発明の他の目的は、原麦に対す
る調質処理を一段階で、かつ、短時間で行い、原麦が水
を含んで滞留する時間を短縮することによって、調質タ
ンク内に細菌や微生物が繁殖することを抑制し、原麦に
細菌や微生物が付着して不衛生になることを防止するこ
とにある。[0014] Still another object of the present invention is to perform a refining treatment on raw wheat in one stage and in a short time to shorten the time for which raw wheat stays in water and stays there. The purpose of the present invention is to suppress the growth of bacteria and microorganisms in the inside, and to prevent the bacteria and microorganisms from adhering to raw wheat and becoming unsanitary.
【0015】さらに、本発明の他の目的は、穀物原料の
真空調質処理を行う加水処理装置の複数セットをパラレ
ルに設置して、各加水処理装置を時間をずらせて運転し
て連続的に穀物原料の真空調質処理を行うことにある。Further, another object of the present invention is to provide a plurality of sets of water treatment apparatuses for performing vacuum refining processing of grain raw materials in parallel, and to continuously operate the water treatment apparatuses with a time lag. An object of the present invention is to perform a vacuum refining treatment of a grain raw material.
【0016】[0016]
【課題を解決するための手段】前述の目的を達成するた
め、本発明は、自己水分を9%前後含む穀物原料に、穀
物原料の水分として6%前後の付加水を添加して混合
し、この付加水を添加した原麦等の穀物原料を真空度2
0〜40Torrの状態において1〜2分間低速撹拌し
た後に瞬時に大気圧に戻し、この急激な気圧変化によっ
て穀物原料に付加水を急速に含浸させて一定時間放置し
(寝かし)、一段階で穀物原料の水分を14〜17%に
することによって、穀物原料を製粉加工するに適した状
態に調質する穀物原料の真空調質処理方法に関するもの
である。In order to achieve the above-mentioned object, the present invention relates to a cereal raw material containing about 9% of self-moisture, and adding and mixing about 6% of additional water as moisture of the cereal raw material, The cereal raw material such as raw wheat to which the additional water is added is vacuumed to 2
After stirring at a low speed of 0 to 40 Torr for 1 to 2 minutes, the pressure is immediately returned to the atmospheric pressure, and this raw material is rapidly impregnated with additional water by the rapid change of the atmospheric pressure and left for a certain period of time (sleeping). The present invention relates to a method for vacuum conditioning a grain raw material in which the water content of the raw material is adjusted to 14 to 17% to condition the grain raw material in a state suitable for milling.
【0017】また、本発明は、穀物原料の流入機構と流
出機構を有する真空加水処理装置に、穀物原料の撹拌移
送手段を内設するとともに、穀物原料に付加水添加する
付加水供給槽、真空加水処理装置内を真空度20〜40
Torrにする真空発生装置、真空加水処理装置内を大
気圧に戻す真空解除装置を接続した穀物原料の真空調質
処理装置に関するものである。Further, the present invention provides a vacuum water treatment apparatus having a grain raw material inflow mechanism and a grain raw material outflow mechanism, in which a stirring and transferring means for the grain raw material is internally provided, and an additional water supply tank for adding additional water to the grain raw material is provided. The degree of vacuum is 20 to 40 in the water treatment device.
The present invention relates to a vacuum conditioning apparatus for grain raw materials to which a vacuum generator for reducing pressure to Torr and a vacuum release apparatus for returning the inside of a vacuum water treatment apparatus to atmospheric pressure are connected.
【0018】さらに、本発明は、前述した穀物原料の調
質装置において、真空加水処理装置をパラレルに2セッ
ト以上設け、各加水処理装置を時間をずらせて運転して
連続的に調質処理を行う真空調質処理装置に関するもの
である。Further, in the present invention, in the above-mentioned grain raw material refining apparatus, two or more sets of vacuum water refining apparatuses are provided in parallel, and each water refining apparatus is operated at a different time to continuously perform the refining processing. The present invention relates to a vacuum refining processing apparatus.
【0019】[0019]
【発明の実施形態】以下、本発明の穀物原料の真空調質
方法を小麦(原麦)を一例として説明すると、先ず原麦
に混入する異物、夾雑物、被害粒など混入阻害物を除去
するとともに、正常の麦粒子を精選し、この精選した原
麦を産地別、種類別に分離する。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the method for vacuum refining of cereal raw materials according to the present invention will be described by taking wheat (raw wheat) as an example. First, foreign substances, foreign substances, damaged grains and the like, which are mixed in raw wheat, are removed. At the same time, normal wheat particles are carefully selected, and the selected raw wheat is separated according to production areas and types.
【0020】分離した原麦の自己保持水分は産地別、種
類別によって多少異なるが、通常の場合においては9%
前後の水分を含有しており、これを精選、製粉に適した
状態にするために、以下に述べるような原麦の真空調質
処理を行う。すなわち、9%前後の自己保持水分を含有
する原麦に6%前後に相当する付加水を添加して混合
し、この付加水を添加した原麦を真空度20〜40To
rrの状態において1〜2分間撹拌した後に瞬時に大気
圧に戻し、この急激な気圧変化によって原麦に付加水を
急速に含浸させて5〜10時間放置して原麦の水分を一
段階で14〜17%前後にする。The self-retained water content of the separated raw wheat varies slightly depending on the locality and the type, but is usually 9%.
The raw wheat is subjected to a vacuum tempering treatment as described below in order to contain water before and after, and to make it suitable for fine selection and milling. That is, raw water containing about 9% of self-retained moisture is added with and mixed with about 6% of additional water, and the raw wheat to which this additional water is added is subjected to a vacuum of 20 to 40 To.
After stirring for 1 to 2 minutes in the state of rr, the pressure is immediately returned to the atmospheric pressure, and the barley is rapidly impregnated with additional water by this rapid change in air pressure and left for 5 to 10 hours to reduce the water content of the barley in one step. It should be around 14-17%.
【0021】前述したような原麦の調質処理を行うこと
によって、原麦の胚乳組織に水を十分に浸透させて原麦
の粒質を軟化させるとともに原麦の外皮を強靭化にし、
原麦の胚乳とふすまの分離、胚乳の粉砕を良好にして、
原麦を精選、製粉に適した状態にする。By performing the above-mentioned temper treatment of the raw wheat, water is sufficiently penetrated into the endosperm tissue of the raw wheat to soften the granularity of the raw wheat and toughen the outer skin of the raw wheat,
Separation of endosperm and bran of raw wheat, crushing of endosperm,
Raw wheat is selected and put into a state suitable for milling.
【0022】原麦に付加水として6%前後、すなわち5
〜7%に相当する水分を添加するのは、5%未満の付加
水の添加では、一段階で原麦の胚乳組織に水を十分に浸
透させることはできず、原麦の粒質の軟化と原麦の外皮
の強靭化が不十分であり、また、7%を超えた付加水の
添加を行っても、原麦に対する水分の増加は全体として
15〜16%前後が加工処理上の限界であって、7%を
超えた付加水の添加は余分な水分の添加になるためであ
る。About 6%, ie, 5%, is added to raw wheat as additional water.
The reason for adding water equivalent to ~ 7% is that, with the addition of less than 5% of added water, water cannot fully penetrate into the endosperm tissue of the raw wheat in one step, and the granularity of the raw wheat is softened. In addition, the toughness of the outer bark of raw wheat is insufficient, and even if additional water exceeding 7% is added, the increase in water relative to raw wheat is about 15-16% as a whole, which is a processing limit. This is because the addition of additional water exceeding 7% results in the addition of extra water.
【0023】付加水を添加した原麦を真空度20〜40
Torrの状態において調質処理を行うのは、真空度2
0Torr未満であると、瞬時に大気圧に戻した際に形
成する急激な気圧変化としては不十分であるためであ
り、また、真空度40Torrを超えると、真空度を高
めただけの効果がなく、エネルギーロスが多くなって経
済的でないことによる。The raw wheat to which the additional water is added is subjected to a vacuum of 20 to 40.
The refining process is performed in the state of Torr when the degree of vacuum is 2
If the pressure is less than 0 Torr, it is insufficient as a rapid change in atmospheric pressure formed when the pressure is instantaneously returned to the atmospheric pressure. If the pressure exceeds 40 Torr, there is no effect of increasing the degree of vacuum. However, energy loss increases and it is not economical.
【0024】前述した真空度において付加水を添加、混
合した原麦を1〜2分間撹拌するのは、1分未満の撹拌
では原麦と水との混合が不十分となって、一段階で原麦
の胚乳組織に水を浸透させることはできず、原麦の粒質
の軟化と原麦の外皮の強靭化が不完全になり、また、2
分を超えた撹拌を行っても、原麦に対する水分の増加は
全体として14〜17%前後が加工処理上の限界であっ
て、2分を超えた撹拌を行っても原麦の水分は増加せ
ず、時間のロスになるだけである。The reason why the raw wheat mixed with added water at the degree of vacuum described above and stirred for 1 to 2 minutes is that if the stirring is performed for less than 1 minute, the mixing of the raw wheat and the water becomes insufficient, and the mixing is performed in one stage. Water cannot penetrate into the endosperm tissue of raw wheat, and the softening of the grain quality of raw wheat and the toughness of raw wheat hulls become incomplete.
Even if the stirring is performed for more than 2 minutes, the increase of the water content to the raw wheat is about 14 to 17% as a whole in the processing limit, and the water content of the raw wheat increases even if the stirring is performed for more than 2 minutes. No, it's just a loss of time.
【0025】付加水を含浸させた原麦を5〜10時間放
置するのは、5時間未満の放置(寝かせ)では、一段階
で原麦の胚乳組織に水を浸透させて原麦の粒質の軟化と
原麦の外皮の強靭化を行うことが不十分であり、また、
10時間を超えた放置を行っても、前述した理由と同じ
く原麦の水分は増加はせず、時間のロスになるだけであ
る。大豆、米、蕎麦、トウモロコシ等の穀物原料につい
て、真空調質処理を行う場合には、、付加水の添加量と
真空度の条件は原麦のときと同じでよいが、放置時間
は、30〜60分と短くてよい。The raw wheat impregnated with the additional water is allowed to stand for 5 to 10 hours. If the raw wheat is left for less than 5 hours (laying down), water is allowed to penetrate into the endosperm tissue of the raw wheat in one step, and Is insufficient to soften and toughen the outer skin of raw wheat,
Even if it is left for more than 10 hours, the water content of the raw wheat does not increase as in the above-mentioned reason, and only the time is lost. When performing vacuum refining treatment on cereal raw materials such as soybeans, rice, buckwheat, and corn, the conditions of the amount of added water and the degree of vacuum may be the same as those of raw wheat, but the leaving time is 30 minutes. It may be as short as ~ 60 minutes.
【0026】次に、本発明の穀物原料の真空調質処理装
置を、小麦の原麦の真空調質処理装置を一例として、図
2にしたがって説明すると、原麦を投入する複数個の原
麦タンク1から始まって、原麦を搬送する空気輸送機1
2までの処理ラインについては、前述した図1の従来の
原麦の調質処理装置と同じであるので説明を省略する
が、異なるところは、原麦を一次貯蔵するサービスタン
ク31とスクリューコンベヤー排出機36を付設する
点、加水供給ユニット40と真空ポンプユニット45を
接続した円筒形の真空加水処理装置32を別途に設置し
た点である。Next, the vacuum refining treatment apparatus for grain raw material of the present invention will be described with reference to FIG. 2 using a vacuum refining treatment apparatus for raw wheat as an example. Pneumatic transport machine 1 that transports raw wheat, starting from tank 1
The processing lines up to 2 are the same as those of the conventional raw wheat refining processing apparatus shown in FIG. 1 described above, and thus description thereof is omitted. However, different points are a service tank 31 for temporarily storing raw wheat and a screw conveyor discharge. The point that the machine 36 is attached is that a cylindrical vacuum water treatment apparatus 32 to which a water supply unit 40 and a vacuum pump unit 45 are connected is separately installed.
【0027】本発明装置の特徴は、真空加水処理装置3
2に加水供給ユニット40と真空ポンプユニット45と
を接続したを設置したことであって、真空加水処理装置
32の内部には駆動モーター49で回転する撹拌および
送り羽根33を付設し、また、真空加水処理装置32に
は真空投入ゲート35を設けるとともに真空排出ゲート
46を設ける。The feature of the apparatus of the present invention is that
2 is provided with a water supply unit 40 and a vacuum pump unit 45 connected thereto, and a stirring and feeding blade 33 rotated by a drive motor 49 is additionally provided inside the vacuum water treatment device 32. The water treatment device 32 is provided with a vacuum input gate 35 and a vacuum discharge gate 46.
【0028】原麦を充填した各真空加水処理装置32に
おいては、加水バルブ38と39を開いて加水供給ユニ
ット40から各真空加水処理装置32の原麦に付加水を
添加するが、この際に流量計37によって、9%前後の
自己保持水分を含有する原麦に対して6%前後に相当す
る水を付加水として添加するように構成する。各真空加
水処理装置32においては、駆動モーター49によって
撹拌および送り羽根33を低速で回転させて原麦と付加
水を混合し、付加水の添加が完了したら加水パルブ38
と39を閉じた後に、真空パルブ42と43を開いて真
空ポンプユニット45を作動して各真空加水処理装置3
2の内部の空気を脱気して真空度を20〜40Torr
の範囲まで下げるように構成する。In each vacuum water treatment apparatus 32 filled with raw wheat, the water supply valves 40 and 39 are opened to add additional water from the water supply unit 40 to the raw wheat in each vacuum water treatment apparatus 32. The flow meter 37 is configured to add water corresponding to about 6% to the raw wheat containing about 9% of self-holding moisture as additional water. In each vacuum water treatment device 32, the raw motor and the additional water are mixed by rotating the stirring and feed blades 33 at low speed by the drive motor 49, and when the addition of the additional water is completed, the water
And 39 are closed, the vacuum valves 42 and 43 are opened, and the vacuum pump unit 45 is operated to operate the respective vacuum water treatment devices 3.
Degas the air inside 2 to reduce the degree of vacuum to 20 to 40 Torr
It is configured to lower to the range.
【0029】すなわち、本発明の各真空加水処理装置3
2においては、6%前後の付加水を添加した原麦を、真
空度20〜40Torrの状態において、撹拌および送
り羽根33によって1〜2分間撹拌して、原麦に6%前
後の付加水を徐々に含浸させ始め、次いで、真空パルブ
41と42を閉じるとともに、真空ブレークバルブ44
を開いて各真空加水処理装置32内を瞬時に大気圧に戻
し、この急激な気圧変化によって原麦に6%前後の付加
水を急速かつ一挙に含浸させて原麦の水分を一段階で1
4〜17%にする真空調質処理を行う点にポイントがあ
る。That is, each vacuum water treatment apparatus 3 of the present invention
In 2, the raw wheat to which the additional water of about 6% is added is stirred for 1 to 2 minutes by the stirring and the feed blade 33 in a state of a vacuum degree of 20 to 40 Torr, and the raw wheat is added with about 6% of the additional water. Gradually begin to impregnate, then close vacuum valves 41 and 42 and vacuum break valve 44
To instantaneously return the inside of each vacuum water treatment apparatus 32 to the atmospheric pressure, and this sudden change in atmospheric pressure rapidly and rapidly impregnates the raw wheat with about 6% of added water to reduce the water content of the raw wheat in one step.
There is a point in performing a vacuum refining process of 4 to 17%.
【0030】このような各真空加水処理装置32による
原麦の真空調質処理を行うことによって、原麦の胚乳組
織に水を十分に浸透させて原麦の粒質を軟化させるとと
もに原麦の外皮を強靭化させ、原麦の胚乳とふすまの分
離をし易くして、胚乳の粉砕も良好にして、原麦を製粉
加工処理に適した状態にする。By performing the vacuum conditioning treatment of the raw wheat by each of the vacuum water treatment devices 32, water is sufficiently penetrated into the endosperm tissue of the raw wheat to soften the granularity of the raw wheat and to reduce the quality of the raw wheat. The outer skin is toughened, the endosperm of the raw wheat is easily separated from the bran, the endosperm is crushed well, and the raw wheat is brought into a state suitable for milling processing.
【0031】そして、撹拌および送り羽根33を高速回
転に切り換えて、真空排出ゲート46を開いて、各真空
加水処理装置32より真空調質処理をした原麦を流出さ
せて、コンベヤー47によって調質タンク48に導入し
て5〜10時間放置(寝かし)をした後、この原麦を図
1に示すような通常の経路(下部排出機、ホッパー、計
量機、ミキサー、ホッパー、空気輸送機)を経てロール
粉砕機に搬送するように構成する。Then, the stirring and feeding blades 33 are switched to high-speed rotation, the vacuum discharge gate 46 is opened, and the raw wheat subjected to the vacuum refining treatment is discharged from each vacuum water treatment device 32, and refined by the conveyor 47. After being introduced into the tank 48 and left (rested) for 5 to 10 hours, the raw wheat is passed through the usual route (lower discharger, hopper, weigher, mixer, hopper, pneumatic transporter) as shown in FIG. And transported to a roll mill.
【0032】連続的に真空調質処理を行う場合には、真
空加水処理装置32Aと真空加水処理装置32Bをパラ
レルに設置するとよく、各真空加水処理装置を時間をず
らせて運転し、たとえば、切替カット機構(図示せず)
で真空加水処理装置32Aと32Bのいずれか選択し、
選択した一方の真空加水処理装置32Aの真空投入ゲー
ト35を開けて、計量機34で投入量を設定した原麦を
充填して、付加水の添加工程を行っている間に、他方の
真空加水処理装置32Bにおいて真空状態の形成工程を
行う。When performing the vacuum refining treatment continuously, it is preferable to install the vacuum water treatment apparatus 32A and the vacuum water treatment apparatus 32B in parallel, and operate each vacuum water treatment apparatus with a time lag. Cutting mechanism (not shown)
Select one of the vacuum water treatment devices 32A and 32B with
The vacuum feeding gate 35 of the selected one of the vacuum water treatment devices 32A is opened, and the raw wheat whose charging amount is set by the weighing machine 34 is filled. A vacuum forming step is performed in the processing device 32B.
【0033】所定時間経過後には、上流切替カットで他
方の真空加水処理装置32Bに切り替えて、他方の真空
加水処理装置32Bの真空投入ゲート35を開けて、計
量機34で投入量を設定した原麦を充填して、付加水の
添加工程を行っている間に、他方の真空加水処理装置3
2Aにおいて真空状態の形成工程を行う。以後、順次、
真空加水処理装置32Aと32Bにおいて前述した工程
を切り替え、これを交互に繰り返すことによって、連続
的に真空調質処理を行えばよく、連続的に真空調質処理
を行う必要がない場合には、真空加水処理装置32は1
セットでもよい。After a lapse of a predetermined time, the apparatus is switched to the other vacuum water treatment apparatus 32B by the upstream switching cut, the vacuum charging gate 35 of the other vacuum water processing apparatus 32B is opened, and the amount set by the meter 34 is set. While the barley is being filled and the additional water is being added, the other vacuum water treatment apparatus 3
In 2A, a vacuum forming step is performed. Thereafter,
By switching the above-described steps in the vacuum water treatment devices 32A and 32B and repeating the process alternately, the vacuum refining process may be continuously performed, and when it is not necessary to continuously perform the vacuum refining process, The vacuum water treatment device 32 is 1
It may be a set.
【0034】各真空加水処理装置32に内接する撹拌移
送手段としては、前述した撹拌および送り羽根33以外
に、パドル式ヌビーターも使用でき、その他、原麦を撹
拌して移送できるものであれば、どんなものでも使用で
き、また、原麦に付加水を添加する付加水供給槽として
は、前述した加水供給ユニット40以外に、加圧水槽、
その他付加水を供給できるものであれば、どんな機器で
も使用でき、さらには、真空加水処理装置としては、前
述した真空ポンプユニット45以外に、エゼクター、そ
の他、真空加水処理装置32内を真空にできるものであ
れば、どんなものでも使用でき、穀物原料の流入機構と
流出機構としては、前述した真空投入ゲート35、真空
排出ゲート46以外にパイプにバルブを付設したものを
使用してもかまわない。As the stirring and transfer means inscribed in each vacuum water treatment apparatus 32, besides the above-described stirring and feeding blades 33, a paddle type nubeater can be used. In addition, any other means capable of stirring and transferring raw wheat can be used. Any water can be used, and as an additional water supply tank for adding additional water to raw wheat, in addition to the above-described water supply unit 40, a pressurized water tank,
Any other device can be used as long as it can supply additional water. In addition to the above-described vacuum pump unit 45, an ejector and other components can be evacuated as the vacuum water treatment device 32. Any mechanism can be used as long as it has a valve attached to a pipe in addition to the above-described vacuum input gate 35 and vacuum discharge gate 46 as the grain raw material inflow mechanism and outflow mechanism.
【0035】[0035]
【実施例1】下記のような構造を有する撹拌および送り
羽根を内臓した円筒型の真空加水処理装置(新明製作所
製)を3セット設置した。 # 撹拌および送り羽根の径20cm、長さ20cm、
スクリューピッチ5cm # 撹拌および送り羽根の回転数30rpm # 真空加水処理装置の径21cm、長さ24cm、 各セットの真空加水処理装置内にカナダ産の自己保持水
分9%前後の製粉用の小麦1、2、3を1リットル投入
し、この小麦に対して6%に相当する水を付加水として
添加して、真空ポンプを作動し、第1セットの真空加水
処理装置(本発明方法の実施装置)の空気を脱気して真
空度30Torrの状態にして、撹拌および送り羽根に
よって小麦1を1分30秒間撹拌した後、第1セットの
真空加水処理装置内を瞬時に大気圧に戻し、8時間放置
するという一連の真空調質処理を行った。EXAMPLE 1 Three sets of cylindrical vacuum water treatment apparatus (manufactured by Shinmei Seisakusho) having the following structure and having built-in stirring and feeding blades were installed. # Stirring and feeding blade diameter 20cm, length 20cm,
Screw pitch 5 cm # Number of rotations of stirring and feeding blades 30 rpm # Vacuum water treatment equipment diameter 21 cm, length 24 cm, Canadian self-retaining moisture of about 9%, wheat 1 for flour milling in each set of vacuum water treatment equipment, A few liters of 2, 3 were added to the wheat, and water equivalent to 6% was added to the wheat as additional water, and the vacuum pump was operated to set the first set of vacuum water treatment equipment (apparatus for implementing the method of the present invention). Air was degassed to a degree of vacuum of 30 Torr, and the wheat 1 was stirred for 1 minute and 30 seconds by stirring and a feed blade. Then, the inside of the first set of vacuum water treatment apparatuses was immediately returned to atmospheric pressure, and 8 hours. A series of vacuum refining treatments in which the substrate was left was performed.
【0036】また、第2セットの真空加水処理装置(比
較方法1の実施装置)の空気を脱気して真空度10To
rrの状態にして、撹拌および送り羽根によって小麦2
を1分30秒間撹拌した後、第2セットの真空加水処理
装置内を瞬時に大気圧に戻し、3時間放置するという一
連の真空調質処理を行った。Further, the air in the second set of vacuum water treatment apparatuses (apparatus for performing the comparison method 1) is degassed to a degree of vacuum of 10 To.
rr, wheat 2 by stirring and feeding blades
After stirring for 1 minute and 30 seconds, the inside of the second set of vacuum water treatment apparatuses was instantaneously returned to the atmospheric pressure, and a series of vacuum refining treatments of leaving for 3 hours was performed.
【0037】さらに、第3セットの真空加水処理装置
(比較方法2の実施装置)の空気を脱気して真空度40
Torrの状態にして、撹拌および送り羽根によって小
麦3を30秒間撹拌した後、第2セットの真空加水処理
装置内を瞬時に大気圧に戻し、11時間放置するという
一連の真空調質処理を行った。Further, the air in the third set of vacuum water treatment apparatuses (apparatus for performing the comparison method 2) is degassed to a degree of vacuum of 40.
After the wheat 3 was stirred for 30 seconds by stirring and feeding blades in the state of Torr, the inside of the second set of vacuum water treatment apparatuses was immediately returned to the atmospheric pressure, and a series of vacuum refining treatments was performed in which it was left for 11 hours. Was.
【0038】以上の真空調質処理を行った結果、各セッ
トの真空加水処理装置より流出する小麦1、2および3
の性状は以下の通りとなった。 調質時間 水分量 胚乳分離性 胚乳粉砕性 製粉加工性 細菌数 小麦1 8時間 16% 良好 良好 良好 104 以下 (本発明法) 小麦2 3時間 12% 不良 不良 不良 104 以下 (比較法1) 小麦3 11 時間 13% やや不良 やや不良 やや不良 105 以下 (比較法2)As a result of performing the above vacuum refining treatment, wheat 1, 2 and 3 flowing out from the vacuum water treatment apparatus of each set
The properties were as follows. Conditioning time Water content Endosperm separability Endosperm crushability Milling processability Bacteria count Wheat 18 hours 16% Good Good Good 10 4 or less (Method of the present invention) Wheat 2 3 hours 12% Bad Bad Bad 10 4 or less (Comparative method 1) Wheat 3 11 hours 13% Somewhat bad Somewhat bad Somewhat bad 10 5 or less (Comparative method 2)
【0039】[0039]
【実施例2】前述の実施例1で使用した真空加水処理装
置3セットを用い、各セットの真空加水処理装置内にア
メリカ産の自己保持水分12%の油脂抽出用の大豆1、
2、3を1リットル投入し、この大豆に対して5%に相
当する水を付加水として添加して、真空ポンプを作動
し、第1セットの真空加水処理装置(本発明方法の実施
装置)の空気を脱気して真空度30Torrの状態にし
て、撹拌および送り羽根によって大豆1を1分間撹拌し
た後、第1セットの真空加水処理装置内を瞬時に大気圧
に戻し、40分間放置するという一連の真空調質処理を
行った。Example 2 Three sets of vacuum water treatment devices used in the above-mentioned Example 1 were used, and soybeans 1 for extracting 12 g of oil and fat with 12% self-holding moisture from the United States were placed in each set of water treatment devices.
A few liters of 2 and 3 were added, and water equivalent to 5% of the soybean was added as additional water, and a vacuum pump was operated to set up a first set of vacuum water treatment apparatus (apparatus for implementing the method of the present invention). Air is degassed to a degree of vacuum of 30 Torr, soybean 1 is stirred for 1 minute by stirring and a feed blade, then the inside of the first set of vacuum water treatment apparatuses is instantaneously returned to atmospheric pressure and left for 40 minutes. A series of vacuum refining treatments was performed.
【0040】また、比較方法として第2セットの真空加
水処理装置(比較方法1の実施装置)の空気を脱気して
真空度10Torrの状態にして、撹拌および送り羽根
によって大豆2を1分間撹拌した後、真空パルブを閉じ
るとともに、真空ブレークパルブを開いて第2セットの
真空加水処理装置内を瞬時に大気圧に戻し、60分間放
置するという一連の真空調質処理を行った。As a comparative method, the air of the second set of vacuum water treatment apparatuses (the apparatus for performing the comparative method 1) was evacuated to a vacuum of 10 Torr, and the soybeans 2 were stirred for 1 minute by stirring and a feed blade. After that, the vacuum pulp was closed, the vacuum break pulp was opened, the inside of the second set of vacuum water treatment equipment was immediately returned to atmospheric pressure, and a series of vacuum refining treatments was performed in which it was left for 60 minutes.
【0041】さらに、比較方法として第3セットの真空
加水処理装置(比較方法2の実施装置)の空気を脱気し
て真空度40Torrの状態にして、撹拌および送り羽
根によって大豆3を1分間撹拌した後、第2セットの真
空加水処理装置内を瞬時に大気圧に戻し、20分間放置
するという一連の真空調質処理を行った。Further, as a comparative method, the air in the third set of vacuum water treatment apparatuses (the apparatus for performing the comparative method 2) was degassed to a vacuum of 40 Torr, and the soybean 3 was stirred for 1 minute by stirring and a feed blade. After that, the inside of the second set of vacuum water treatment apparatuses was immediately returned to the atmospheric pressure, and a series of vacuum refining treatments in which the apparatus was left for 20 minutes was performed.
【0042】以上の真空調質処理を行った結果、各セッ
トの真空加水処理装置より流出する大豆1、2および3
の性状は以下の通りとなった。 調質時間 水分量 フレーク厚みと大きさ 製粉加工性 大豆1 30分 16% 0.3〜0.4mm 良好 (本発明法) 大豆2 60分 13% 不安定 不良 (比較法) 大豆3 20分 12% 0.3〜0.4mm やや不良 (比較法)As a result of the above vacuum conditioning treatment, the soybeans 1, 2 and 3 flowing out of the vacuum water treatment equipment of each set were obtained.
The properties were as follows. Refining time Moisture content Flake thickness and size Milling processability Soybean 1 30 minutes 16% 0.3-0.4mm Good (Invention method) Soybean 2 60 minutes 13% Unstable Unsatisfactory (Comparative method) Soybean 3 20 minutes 12 % 0.3-0.4mm Slightly poor (Comparison method)
【0043】[0043]
【実施例3】前述の実施例1で使用した真空加水処理装
置3セットを用い、各セットの真空加水処理装置内にア
メリカ産の自己保持水分14%の製粉用のトウモロコシ
1、2、3を1リットル投入し、このトウモロコシに対
して3%に相当する水を付加水として添加して、真空ポ
ンプを作動し、第1セットの真空加水処理装置内(本発
明法の実施装置)の空気を脱気して真空度30Torr
の状態にして、撹拌および送り羽根によってトウモロコ
シ1を1分間撹拌した後、第1セットの真空加水処理装
置内を瞬時に大気圧に戻し、40分間放置するという一
連の真空調質処理を行った。EXAMPLE 3 Using three sets of vacuum water treatment equipment used in Example 1 described above, corns 1, 2 and 3 for milling with 14% self-holding moisture from the United States were placed in the vacuum water treatment equipment of each set. 1 liter was added, and water equivalent to 3% of the corn was added as additional water, and the vacuum pump was operated to evacuate the air in the first set of vacuum water treatment equipment (the apparatus for implementing the method of the present invention). Deaerate and vacuum 30 Torr
, The corn 1 was stirred for 1 minute by the stirring and the feed blades, and then the inside of the first set of vacuum water treatment apparatuses was instantaneously returned to the atmospheric pressure, and a series of vacuum refining treatments of leaving the apparatus for 40 minutes was performed. .
【0044】また、第2セットの真空加水処理装置(比
較方法1の実施装置)内の空気を脱気して真空度10T
orrの状態にして、撹拌および送り羽根によってトウ
モロコシ2を1分間撹拌した後、真空パルブを閉じると
ともに、真空ブレークパルブを開いて第2セットの真空
加水処理装置内を瞬時に大気圧に戻し、1時間間放置す
るという一連の真空調質処理を行った。Further, the air in the second set of vacuum water treatment apparatuses (the apparatus for performing the comparison method 1) was degassed to a degree of vacuum of 10T.
After the corn 2 was stirred for 1 minute by the stirring and feeding blades in the orr state, the vacuum pulp was closed, and the vacuum break valve was opened to immediately return the inside of the second set of vacuum water treatment apparatuses to atmospheric pressure. A series of vacuum refining treatments of leaving for a time was performed.
【0045】さらに、第3セットの真空加水処理装置
(比較方法2の実施装置)内の空気を脱気して真空度4
0Torrの状態にして、撹拌および送り羽根によって
トウモロコシ3を1分間撹拌した後、真空パルブを閉じ
るとともに、真空ブレークパルブを開いて第2セットの
真空加水処理装置内を瞬時に大気圧に戻し、20分間放
置するという一連の真空調質処理を行った。Further, the air in the third set of the vacuum water treatment apparatus (the apparatus for performing the comparison method 2) was degassed to obtain a degree of vacuum of 4.
At 0 Torr, the corn 3 was stirred for 1 minute by the stirring and feeding blades, and then the vacuum valve was closed, and the vacuum break valve was opened to immediately return the inside of the second set of vacuum water treatment equipment to atmospheric pressure. A series of vacuum refining treatments, which were left for a minute, was performed.
【0046】以上の真空調質処理を行った結果、各セッ
トの真空加水処理装置より流出するトウモロコシ1、2
および3の性状は以下の通りとなった。 調質時間 水分量 胚乳分離性 胚乳粉砕性 製粉加工性 トウモロコシ1 40分 17% 良好 良好 良好 (本発明法) トウモロコシ2 60分 12% 不良 不良 不良 (比較法) トウモロコシ3 20分 13% やや不良 やや不良 やや不良 (比較法)As a result of performing the above vacuum refining treatment, the corns 1, 2
The properties of and 3 were as follows. Conditioning time Water content Endosperm separating property Endosperm crushing property Milling processability Maize 140 minutes 17% Good Good Good (The present method) Maize 260 60 minutes 12% Poor Poor Poor (Comparative method) Maize 3 20 minutes 13% Somewhat poor Somewhat bad (Comparative method)
【0047】[0047]
【発明の効果】本発明によると、麦、大豆、米、蕎麦、
トウモロコシ等の穀物原料を製粉加工する際に行うこれ
らの穀物原料の調質処理を、従来の第1段階の調質処理
と第2段階の調質処理のように二段階に渡って長時間に
行うことはせずに、真空下で一段階で支障なく行うこと
によって、調質処理時間を従来の場合に比較して二分の
一以下にし、調質処理時間の短縮化を計り、作業の簡略
化、省力化を計ることができる優れた効果を達成でき
る。According to the present invention, wheat, soybeans, rice, buckwheat,
The refining treatment of these cereal raw materials, which is performed when milling cereal raw materials such as corn, is performed over a long period of time in two stages as in the conventional first and second stage refining processes. Rather than performing the process, the refining process time is reduced to one-half or less of the conventional case by performing the process in a single stage under vacuum without any trouble. It is possible to achieve an excellent effect that can reduce power consumption and labor.
【0048】また、本発明によると、穀物原料の調質処
理を、従来のように第1次調質タンクと第2次調質タン
ク(関連機器類等を含めて)の2セットを使用するので
はなく、1セットだけで調質処理を支障なく行うことが
でき、装置のイニシャルおよびランニングコストの低減
を計るとともに、装置全体のコンパクト化を計り、装置
設置面積を小さくして、スペースエコノミーを改善でき
る実用的なメリットがある。Further, according to the present invention, two sets of a primary refining tank and a secondary refining tank (including related equipment, etc.) are used for the refining treatment of the cereal raw material as in the prior art. Instead, the refining process can be performed with only one set without any trouble, reducing the initial and running costs of the equipment, reducing the overall size of the equipment, reducing the equipment installation area, and improving the space economy. There are practical benefits that can be improved.
【0049】さらに、本発明によると、原麦に対する調
質処理を一段階で、かつ、短時間で行い、原麦が水を含
んで滞留する時間を短縮することによって、調質タンク
内に細菌や微生物が繁殖することを抑制し、原麦に細菌
や微生物が付着して不衛生になることを防止できる利点
がある。Further, according to the present invention, the refining treatment of raw wheat is performed in one stage and in a short time, and the time in which the raw wheat stays in water and shortens, so that bacteria can be stored in the refining tank. There is an advantage that it is possible to suppress the propagation of microorganisms and microorganisms, and to prevent bacteria and microorganisms from adhering to raw wheat and becoming unsanitary.
【0050】さらに、本発明によると、穀物原料の調質
処理を行う加水処理装置の複数セットをパラレルに設置
して、各加水処理装置を時間をずらせて運転して連続的
に穀物原料の調質処理を行うことができる効果がある。Further, according to the present invention, a plurality of sets of water treatment devices for performing the refining treatment of grain raw materials are installed in parallel, and each water treatment device is operated with a time lag to continuously prepare the grain raw materials. There is an effect that quality processing can be performed.
【0051】さらに、本発明によると、穀物原料に対し
て均質に加水することが可能であるために、製粉化した
製品の品質が安定し、歩留が向上する効果があり、ま
た、短時間で銘柄の変更可能であり、さらに、穀物原料
の表面に遊離水分が存在しないためにタンクや装置内で
のブロッキングがなくなり、穀物原料の排出が円滑、容
易になる等の利点がある。Furthermore, according to the present invention, it is possible to uniformly add water to the cereal raw material, so that the quality of the milled product is stabilized and the yield is improved. In addition, since there is no free moisture on the surface of the cereal raw material, there is an advantage that the blocking in the tank or the device is eliminated, and the discharge of the cereal raw material becomes smooth and easy.
【0052】さらに、本発明は、前述した小麦の製粉す
る際の小麦の調質処理以外に、大豆の油脂抽出の際に大
豆を圧扁する処理、大豆フレークの厚みを薄く大きくす
る処理に利用でき、また、大豆から豆腐を加工する際に
浸漬前の大豆へ高水分を短時間で浸漬する処理に利用で
き、さらに、米を製粉または麺加工する際に浸漬代りに
利用でき、その他、蕎麦を製粉する際に脱穀前の蕎麦原
料の調質処理、トウモロコシを製粉する際に脱胚芽前の
原料調質処理(乾式)、浸漬前のトウモロコシへ高水分
を短時間で浸漬する処理に利用できるほか、製造する穀
物製品の品質が安定し、歩留が向上する効果がある。Furthermore, the present invention can be used for the treatment of pressing soybeans at the time of extracting fats and oils of soybeans and the treatment of reducing the thickness of soybean flakes, in addition to the above-mentioned tempering treatment of wheat when milling wheat. It can also be used for the process of immersing high moisture in soybeans before immersion in a short time when processing tofu from soybeans, and can be used instead of immersion when milling or processing noodles on rice. It can be used for the refining of buckwheat raw material before threshing when milling, the refining of raw material before degermination (dry type) when milling corn, and the process of immersing high moisture in corn in a short time before immersion. In addition, there is an effect that the quality of the grain product to be manufactured is stabilized and the yield is improved.
【図1】従来の小麦の調質処理方法と調質処理装置の一
例を示す説明図である。FIG. 1 is an explanatory view showing an example of a conventional wheat heat treatment method and heat treatment apparatus.
【図2】本発明の小麦の調質処理方法と調質処理装置の
一例を示す説明図である。FIG. 2 is an explanatory diagram showing an example of a method and apparatus for refining wheat according to the present invention.
【符号の説明】 1 原麦タンク 2 送出機 3 上部ホッパー 4 計量機 5 ミキサー 6 下部ホッパー 7 空気輸送機 8ー11 精選機 12 空気輸送機 13 第1次加水装置 14 水槽 15 コンベヤー 16 第1次調質タンク 17 送出機 18 上部ホッパー18 19 計量機 20 ミキサー 21 下部ホッパー 22 空気輸送機 23 第2次加水装置 24 水槽 25 コンベヤー 26 第2次調質タンク 27 定量送出機 28 ホッパー 29 送りコンベヤー 30 ロール粉砕機 31 サービスタンク 32 真空加水処理装置 33 撹拌および送り羽根 34 計量機 35 真空投入ゲート 36 スクリューコンベヤー排出機 37 流量計 38、39 加水バルブ 40 加水供給ユニット 41 加水バルブ 42、43 真空パルブ 43 真空バルブ 44 真空ブレーキパルプ 45 真空ポンプユニット 46 真空排出ゲート 47 コンベヤー 48 調質タンク 49 駆動モーター[Description of Signs] 1 Raw wheat tank 2 Feeder 3 Upper hopper 4 Weighing machine 5 Mixer 6 Lower hopper 7 Pneumatic transporter 8-11 Purifier 12 Air transporter 13 Primary hydration unit 14 Water tank 15 Conveyor 16 Primary Temper tank 17 Feeder 18 Upper hopper 18 19 Weighing machine 20 Mixer 21 Lower hopper 22 Pneumatic transporter 23 Secondary hydrator 24 Water tank 25 Conveyor 26 Secondary temper tank 27 Quantitative feeder 28 Hopper 29 Feed conveyor 30 Roll Crusher 31 Service tank 32 Vacuum water treatment device 33 Stirring and feed blade 34 Metering machine 35 Vacuum input gate 36 Screw conveyor discharge machine 37 Flow meter 38, 39 Watering valve 40 Watering supply unit 41 Watering valve 42, 43 Vacuum valve 43 Vacuum valve 44 Vacuum breaker Pulp 45 vacuum pump unit 46 vacuum discharge gate 47 conveyor 48 temper tank 49 drive motor
─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成9年9月19日[Submission date] September 19, 1997
【手続補正1】[Procedure amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0023[Correction target item name] 0023
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0023】付加水を添加した原麦を真空度20〜40
Torrの状態において調質処理を行うのは、真空度2
0Torrを超えると、瞬時に大気圧に戻した際に形成
する急激な気圧変化としては不十分であるためであり、
また、真空度40Torr未満であると、真空度を高め
ただけの効果がなく、エネルギーロスが多くなって経済
的でないことによる。The raw wheat to which the additional water is added is subjected to a vacuum of 20 to 40.
The refining process is performed in the state of Torr when the degree of vacuum is 2
If the pressure exceeds 0 Torr , it is insufficient as a sudden change in atmospheric pressure formed when the pressure is instantaneously returned to the atmospheric pressure.
On the other hand, if the degree of vacuum is less than 40 Torr , the effect of merely increasing the degree of vacuum is not obtained, and energy loss increases, which is not economical.
【手続補正2】[Procedure amendment 2]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0028[Correction target item name] 0028
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0028】原麦を充填した各真空加水処理装置32に
おいては、加水バルブ38と39を開いて加水供給ユニ
ット40から各真空加水処理装置32の原麦に付加水を
添加するが、この際に流量計37によって、9%前後の
自己保持水分を含有する原麦に対して6%前後に相当す
る水を付加水として添加するように構成する。各真空加
水処理装置32においては、駆動モーター49によって
撹拌および送り羽根33を低速で回転させて原麦と付加
水を混合し、付加水の添加が完了したら加水バルブ38
と39を閉じた後に、真空バルブ42と43を開いて真
空ポンプユニット45を作動して各真空加水処理装置3
2の内部の空気を脱気して真空度を20〜40Torr
の範囲まで下げるように構成する。In each vacuum water treatment apparatus 32 filled with raw wheat, the water supply valves 40 and 39 are opened to add additional water from the water supply unit 40 to the raw wheat in each vacuum water treatment apparatus 32. The flow meter 37 is configured to add water corresponding to about 6% to the raw wheat containing about 9% of self-holding moisture as additional water. In each of the vacuum hydrolysis processing apparatus 32, the drive motor 49 to rotate the stirring and feeding blade 33 at a low speed by mixing additional water and Genbaku, the hydro valves 38 After the addition of additional water is complete
If after closing the 39, vacuum valves 42 and 43 each vacuum hydrolysis processor 3 by operating the vacuum pump unit 45 is opened
Degas the air inside 2 to reduce the degree of vacuum to 20 to 40 Torr
It is configured to lower to the range.
【手続補正3】[Procedure amendment 3]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0029[Correction target item name] 0029
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0029】すなわち、本発明の各真空加水処理装置3
2においては、6%前後の付加水を添加した原麦を、真
空度20〜40Torrの状態において、撹拌および送
り羽根33によって1〜2分間撹拌して、原麦に6%前
後の付加水を徐々に含浸させ始め、次いで、真空バルブ
42と43を閉じるとともに、真空ブレークバルブ44
を開いて各真空加水処理装置32内を瞬時に大気圧に戻
し、この急激な気圧変化によって原麦に6%前後の付加
水を急速かつ一挙に含浸させて原麦の水分を一段階で1
4〜17%にする真空調質処理を行う点にポイントがあ
る。That is, each vacuum water treatment apparatus 3 of the present invention
In 2, the raw wheat to which the additional water of about 6% is added is stirred for 1 to 2 minutes by the stirring and the feed blade 33 in a state of a vacuum degree of 20 to 40 Torr, and the raw wheat is added with about 6% of the additional water. gradually began impregnated, then, it closes the vacuum valves 42 and 4 3, the vacuum break valve 44
To instantaneously return the inside of each vacuum water treatment apparatus 32 to the atmospheric pressure, and this sudden change in atmospheric pressure rapidly and rapidly impregnates the raw wheat with about 6% of added water to reduce the water content of the raw wheat in one step.
There is a point in performing a vacuum refining process of 4 to 17%.
【手続補正4】[Procedure amendment 4]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0040[Correction target item name] 0040
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0040】また、比較方法として第2セットの真空加
水処理装置(比較方法1の実施装置)の空気を脱気して
真空度10Torrの状態にして、撹拌および送り羽根
によって大豆2を1分間撹拌した後、真空バルブを閉じ
るとともに、真空ブレークバルブを開いて第2セットの
真空加水処理装置内を瞬時に大気圧に戻し、60分間放
置するという一連の真空調質処理を行った。As a comparative method, the air of the second set of vacuum water treatment apparatuses (the apparatus for performing the comparative method 1) was evacuated to a vacuum of 10 Torr, and the soybeans 2 were stirred for 1 minute by stirring and a feed blade. after, closes the vacuum valves, the second set of vacuum hydrolysis processing apparatus returns instantly to the atmospheric pressure by opening the vacuum break valves, we performed a series of true conditioning quality processing for for 60 minutes.
【手続補正5】[Procedure amendment 5]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】図面の簡単な説明[Correction target item name] Brief description of drawings
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図面の簡単な説明】[Brief description of the drawings]
【図1】従来の小麦の調質処理方法と調質処理装置の一
例を示す説明図である。FIG. 1 is an explanatory view showing an example of a conventional wheat heat treatment method and heat treatment apparatus.
【図2】本発明の小麦の調質処理方法と調質処理装置の
一例を示す説明図である。FIG. 2 is an explanatory diagram showing an example of a method and apparatus for refining wheat according to the present invention.
【符号の説明】 1 原麦タンク 2 送出機 3 上部ホッパー 4 計量機 5 ミキサー 6 下部ホッパー 7 空気輸送機 8〜11 精選機 12 空気輸送機 13 第1次加水装置 14 水槽 15 コンベヤー 16 第1次調質タンク 17 送出機 18 上部ホッパー 19 計量機 20 ミキサー 21 下部ホッパー 22 空気輸送機 23 第2次加水装置 24 水槽 25 コンベヤー 26 第2次調質タンク 27 定量送出機 28 ホッパー 29 送りコンベヤー 30 ロール粉砕機 31 サービスタンク 32 真空加水処理装置 33 撹拌および送り羽根 34 計量機 35 真空投入ゲート 36 スクリューコンベヤー排出機 37 流量計 38、39 加水バルブ 40 加水供給ユニット 41 加水バルブ 42、43 真空バルブ 44 真空ブレーキバルプ 45 真空ポンプユニット 46 真空排出ゲート 47 コンベヤー 48 調質タンク 49 駆動モーター[EXPLANATION OF SYMBOLS] 1 Genbaku tank 2 transmitters 3 upper hopper 4 weighing machine 5 Mixer 6 lower hopper 7 air transport 8-11 Collection machine 12 air transporter 13 primary water adding unit 14 water tank 15 conveyor 16 first-order Temper tank 17 Feeder 18 Upper hopper 19 Weighing machine 20 Mixer 21 Lower hopper 22 Air transporter 23 Secondary hydrator 24 Water tank 25 Conveyor 26 Secondary temper tank 27 Quantitative feeder 28 Hopper 29 Feed conveyor 30 Roll crushing machine 31 service tank 32 vacuum hydrolysis processing apparatus 33 stir and feed blade 34 weighing machine 35 vacuum closed gate 36 screw conveyor discharger 37 flowmeter 39 hydro valve 40 hydro supply unit 41 hydro valve 43 vacuum valves 44 vacuum brake Bas Help 45 vacuum port Pump unit 46 Vacuum discharge gate 47 Conveyor 48 Tempering tank 49 Drive motor
Claims (3)
除去した自己水分を9%前後(重量)含む麦、大豆、
米、蕎麦、トウモロコシ等の穀物原料に、穀物原料の水
分として6%前後(重量)に相当する付加水を添加して
混合し、この付加水を添加した穀物原料を真空度20〜
40Torrの状態において1〜2分間浸漬または撹拌
した後に瞬時に大気圧に戻し、この急激な気圧変化によ
って穀物原料に付加水を急速に含浸させて一定時間放置
し、一段階で穀物原料の水分を14〜17%(重量)に
することによって、穀物原料を製粉加工等の食品加工処
理に適した状態に調質する穀物原料の真空調質処理方
法。Claims 1. A wheat, soybean containing about 9% (by weight) of self-moisture from which foreign substances, contaminants, and damaged particles are removed.
Rice, buckwheat, corn and other cereal raw materials are mixed with additional water equivalent to about 6% (weight) as the water content of the cereal raw materials, and the cereal raw materials to which the added water is added are vacuum-
After immersion or stirring for 1 to 2 minutes in the state of 40 Torr, the pressure is immediately returned to the atmospheric pressure, and the grain material is rapidly impregnated with additional water by this rapid pressure change and left for a certain period of time. A vacuum refining method for a grain raw material in which the grain raw material is adjusted to 14 to 17% (weight) so as to be suitable for food processing such as milling.
穀物原料の流入機構と流出機構を有する真空加水処理装
置に、穀物原料の攪拌移送手段を内設するとともに、穀
物原料に付加水を添加する付加水供給槽、真空加水処理
装置内を真空度20〜40Torrにする真空発生装
置、真空加水処理装置内を大気圧に戻す真空解除装置を
接続した穀物原料の真空調質処理装置。2. A vacuum water treatment apparatus having an inflow mechanism and an outflow mechanism for grain raw materials such as wheat, soybeans, rice, buckwheat, and corn, in which a stirring and transferring means for the grain raw materials is internally provided, and additional water is added to the grain raw materials. A vacuum conditioning apparatus for grain raw materials to which an additional water supply tank to be added, a vacuum generator for setting the degree of vacuum in the vacuum water treatment apparatus to 20 to 40 Torr, and a vacuum release apparatus for returning the inside of the vacuum water treatment apparatus to atmospheric pressure are connected.
以上設け、各真空加水処理装置を時間をずらせて運転し
て穀物原料の連続的調質処理をする特許請求項2記載の
穀物原料の真空調質処理装置。3. The cereal raw material according to claim 2, wherein two or more sets of vacuum water treatment apparatuses are provided in parallel, and each of the vacuum water treatment apparatuses is operated with a time lag to perform continuous refining processing of the grain raw material. Air conditioning quality processing equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9251433A JPH1176841A (en) | 1997-09-02 | 1997-09-02 | Vacuum conditioning treatment method and apparatus of grain stock |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9251433A JPH1176841A (en) | 1997-09-02 | 1997-09-02 | Vacuum conditioning treatment method and apparatus of grain stock |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH1176841A true JPH1176841A (en) | 1999-03-23 |
Family
ID=17222775
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9251433A Pending JPH1176841A (en) | 1997-09-02 | 1997-09-02 | Vacuum conditioning treatment method and apparatus of grain stock |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH1176841A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101912796A (en) * | 2010-05-25 | 2010-12-15 | 郑州智信实业有限公司 | Grain Vacuum Rapid Continuous Conditioning Equipment |
| JP2011526538A (en) * | 2008-07-02 | 2011-10-13 | ビューラー・アクチエンゲゼルシャフト | Apparatus and method for producing fine flour and / or coarse flour |
| CN112718040A (en) * | 2020-11-12 | 2021-04-30 | 安徽徽雪食品有限公司 | Wheat wetting and watering device for flour processing |
-
1997
- 1997-09-02 JP JP9251433A patent/JPH1176841A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011526538A (en) * | 2008-07-02 | 2011-10-13 | ビューラー・アクチエンゲゼルシャフト | Apparatus and method for producing fine flour and / or coarse flour |
| US9067213B2 (en) | 2008-07-02 | 2015-06-30 | Buhler Ag | Method for producing flour and/or semolina |
| US10981177B2 (en) | 2008-07-02 | 2021-04-20 | Bühler AG | Apparatus and method for producing flour and/or semolina |
| CN101912796A (en) * | 2010-05-25 | 2010-12-15 | 郑州智信实业有限公司 | Grain Vacuum Rapid Continuous Conditioning Equipment |
| CN112718040A (en) * | 2020-11-12 | 2021-04-30 | 安徽徽雪食品有限公司 | Wheat wetting and watering device for flour processing |
| CN112718040B (en) * | 2020-11-12 | 2022-05-13 | 安徽徽雪食品有限公司 | Wheat wetting and watering device for flour processing |
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