JPH0437698B2 - - Google Patents
Info
- Publication number
- JPH0437698B2 JPH0437698B2 JP59263869A JP26386984A JPH0437698B2 JP H0437698 B2 JPH0437698 B2 JP H0437698B2 JP 59263869 A JP59263869 A JP 59263869A JP 26386984 A JP26386984 A JP 26386984A JP H0437698 B2 JPH0437698 B2 JP H0437698B2
- Authority
- JP
- Japan
- Prior art keywords
- rice
- cooked rice
- drying
- water
- cooked
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 241000209094 Oryza Species 0.000 claims description 141
- 235000007164 Oryza sativa Nutrition 0.000 claims description 141
- 235000009566 rice Nutrition 0.000 claims description 141
- 238000001035 drying Methods 0.000 claims description 53
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 38
- 238000010438 heat treatment Methods 0.000 claims description 23
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 238000010411 cooking Methods 0.000 claims 1
- 238000000034 method Methods 0.000 description 22
- 235000013339 cereals Nutrition 0.000 description 19
- 230000000052 comparative effect Effects 0.000 description 12
- 238000007710 freezing Methods 0.000 description 11
- 230000008961 swelling Effects 0.000 description 8
- 235000013305 food Nutrition 0.000 description 7
- 239000000796 flavoring agent Substances 0.000 description 6
- 235000019634 flavors Nutrition 0.000 description 6
- 230000001007 puffing effect Effects 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000000635 electron micrograph Methods 0.000 description 3
- 230000006837 decompression Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 108010063955 thrombin receptor peptide (42-47) Proteins 0.000 description 2
- 230000005068 transpiration Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Cereal-Derived Products (AREA)
- Cookers (AREA)
Description
本発明は乾燥後における米粒どうしの付着程度
を弱くして、少しの外力によつて単一の米粒にす
ることが可能となり、且つ熱水等の注加により復
元後の食感、風味が乾燥前の食感、風味とほとん
ど変わらないまでに短時間で復元する即席乾燥米
飯の製造法に関する。
従来より熱水等の注加により簡単に復元させる
ことができる即席乾燥米飯に関する技術は数多く
開発されている。本発明者等も復元性、殊に復元
後の食感に優れた即席乾燥米飯を得るための技術
として、食品の減圧膨化乾燥法を開発した(特開
昭58−40057号)。上記食品の減圧膨化乾燥法の要
旨は、食品を、該食品が膨化するに充分な速度で
かつ該食品中の水分が氷結する程度の急速減圧状
態下におき、該食品中の水分が氷結した後加熱乾
燥し、次いで常圧に戻すことを特徴とする食品の
減圧膨化乾燥法にある。しかしながら、この方法
で米飯を乾燥し即席乾燥米飯とした場合、米飯の
粒どうしが相互に付着して塊を形成した状態にな
つたものについては、該塊を崩壊して米粒を一粒
ずつに離すことが困難になる、という欠点があつ
た。
本発明者等はかかる欠点を解消するための方法
について研究した。その結果、米飯を水洗した後
予備乾燥し、その後、上記食品の減圧膨化乾燥法
を採用することが有効である、という知見を得、
即席乾燥米飯の製造法として先に出願した(特開
昭59−31659号)。しかし、この方法によると、米
飯を予め水洗するために米飯の風味が溶出し、最
終製品の風味を若干ではあるが低下させる、とい
う現象がみられた。そこで、更に鋭意研究し、米
飯を予備乾燥するよりも減圧下での乾燥条件、殊
に乾燥温度を高温にすることによつて、上記した
問題を解決することができる、という知見を得る
に到つた。
こうした知見によつて完成された本発明の要旨
は、米飯を、該米飯が膨化するに充分な速度で、
この米飯中の水分が自己氷結する程度の減圧状態
下におき、この米飯中の水分が自己氷結した後直
ちにあるいは20分以内に加熱乾燥を開始し、その
米飯の中心品温が100〜150℃になるまで加熱乾燥
した後米飯が焦げない条件で水分含量が10重量%
以下になるまで保持し、次いで常圧に戻すことを
特徴とする即席乾燥米飯の製造法にある。
以下本発明方法について詳述する。
本発明方法においては、まず常法によつて炊飯
した米飯を減圧下におく。ただし、該米飯を減圧
下におくに当つては、少くとも次の二つの条件を
満足しなければならない。
第1の条件は米飯を膨化が起るに充分な速さで
特定の減圧下におくことである。米飯を減圧下に
おくと、米飯注の水の沸点は当然低下し、それに
よつて該米飯中の水分、殊に自由水分の蒸散現象
が起る。このような蒸散現象が短時間に且つ急速
に起ることによつて上記米飯は膨化する。このこ
とから本発明にいう米飯の膨化が起るに充分な速
度とは、米飯中の水分を短時間で且つ急速に蒸散
せしめるに充分な速さをいう。具体的には1秒以
内であることが好ましい。
第2の条件は、第1の条件で述べた特定の減圧
度を米飯中の水分が自己氷結するに充分な程度の
減圧度にすることである。本発明でいう米飯中の
水分が自己氷結するに充分な程度の真空度は一般
に約609パスカル以下であり、好ましくは約106パ
スカル以下である。
上記二つの条件を満足させて米飯を減圧下にお
いた後、該米飯中の水分が自己氷結するまでに保
持する。この処理によつて膨化した米飯の形状を
そのままの状態に保持させ最終的に得られる乾燥
米飯を膨化状態となすことにより、熱水等による
復元を速めることが可能となる。上記二つの条件
を満足するための減圧方法としては以下の二つが
ある。
第1の方法は、米飯の膨化と該米飯中の水分の
自己氷結を1段階で行う方法、即ち米飯中の水分
が自己氷結する程度の減圧度下に、米飯を膨化が
起るに充分な速さでおく方法である。この方法に
よると、米飯の膨化と米飯中の水分の自己氷結と
はほとんど瞬時に起ることになる。
第2の方法は、米飯の膨化と米飯中の水分の自
己氷結を2段階で行う方法、即ち米飯を膨化が起
るに充分な速さで減圧下(米飯中の水分が自己氷
結するに充分な減圧度に至らない程度の減圧下)
において米飯を膨化させ、その後減圧程度を米飯
中の水分が自己氷結するに充分な減圧下にまで下
げる方法がある。この方法によると、米飯の膨化
と米飯中の水分の自己氷結とは別個に時間的経緯
を経て起ることになる。
本発明の目的を達成する上からは上記いずれの
方法を用いても何ら差し支えなく、本発明の減圧
状態には両者とも含まれる。米飯中の水分を自己
氷結させた後は伝熱加熱、赤外線加熱、マイクロ
波加熱等の常法の加熱手段によつて加熱乾燥する
が、該加熱乾燥処理の開始時期としては、米飯中
の水分が自己氷結した後直ちにあるいは20分以内
好ましくは2〜7以内である。米飯中の水分が自
己氷結したか否かは、米飯の中心品温の変遷をみ
ることによつて容易に確認することができる。第
1図は減圧膨化処理時の米飯の中心品温の経時的
推移の概略を示すものである。第1図に示す如
く、米飯を減圧膨化処理条件で処理すると、米飯
の中心品温は急速に低下して過冷却状態となる
が、その後、上記米飯の中心品温はやや上昇す
る。そして、その上昇が停止した時が米飯中の水
分が氷結した時である。これとは別に米飯が略完
全に白濁したか否かで外観的に判断することもで
きる。即ち、米飯中の水分が自己氷結していくに
したがつて米飯は徐々に白濁していく。米飯中の
水分の自己氷結の終了時期は、主に減圧度と減圧
速度に依存するが、減圧を開始した後約3分程度
で米飯中の水分は概ね自己氷結する。従つて、上
記加熱乾燥の開始時期を別の見方からすると、減
圧開始後3〜23分間程度好ましくは5〜10分間程
度経過した時ということになる。加熱乾燥の開始
時期が早すぎると、自己氷結が完全に終了してい
ないにもかかわらず乾燥されることになるために
乾燥やせが顕著に現われてくることになる。反対
に、加熱乾燥の開始時期が遅すぎると、自己氷結
による米粒どうしの付着が強くなると共にその表
面が徐々に乾燥していくことになり、その結果乾
燥して得られた乾燥米粒どうしの付着が強く少し
の衝撃では容易に壊れなくなつてくる。
この加熱乾燥によつて米飯中の氷結した水分を
除去させるが、この場合米飯の中心品温の昇温速
度をできる限り速くすることが本発明の目的を達
成する上で極めて重要である。即ち、米飯の中心
品温を急速に上昇させて該米飯中の水分を急激に
蒸散させることによつて、米飯内部に多きな空洞
を形成させると共に、該米飯を乾燥する。
このようにして得られた乾燥米飯は、塊状にな
つているものでも、その米粒間の付着程度が弱
く、わずかの外的衝撃によつて容易に単一粒状に
崩壊することができる。
尚、本発明における米飯の中心品温とは、米飯
に温度センサーを挿入し、その温度センサーによ
つて検知された温度をいう。
こうした効果を有する乾燥米飯を得るに当つて
の上記加熱乾燥条件としては、米飯に焦げが発生
しない程度で極力高温で実施する方が好ましく、
具体的には米飯の中心品温が100〜150℃好ましく
は120〜140℃になるまで実施する。中心品温が
100℃に至る前に加熱乾燥を終了すると、乾燥や
せが現われてくることになる。反対に中心品温が
150℃以上になつてくると、米飯に焦げが著しく
発生してくる。上記条件による加熱乾燥を実施す
るに当つては、米飯の中心品温の昇温速度はでき
るだけ速い方がよく、具体的には5〜7℃/分で
あることが好ましい。
米飯の中心品温が100〜150℃になつた後は米飯
が焦げない条件でその水分含量が10重量%以下に
なるまで保持する。これにより乾燥米飯の長期間
の保存が可能となる。この場合、加熱手段として
伝熱加熱を採用する場合は、熱源を停止してもか
なりの高温状態が持続されることになり、結果的
に米飯の焦げが生ずる原因になる可能性があるの
で、適宜手段によつて強制的に冷却する方が好ま
しい。
上記の如くして加熱乾燥を終了した後常圧に戻
して即席乾燥米飯を得る。
次に本発明方法を実施するに当り使用し得る具
体的装置の一例について第2図を基に説明する。
1は乾燥室を示し、乾燥室1の内部には処理物
Aを置くための棚2が設けられている。棚2の下
方および上方にはヒーター3,4が設置されてい
る。乾燥室1の側壁にはパイプ5を介してコール
ドトラツプ6が接続されており、該コールドトラ
ツプ6はパイプ7を介して真空ポンプ8と接続さ
れている。一方、前記パイプ5,7にはバルブ
9,10が設けられており、該パイプ5の前後に
はパイプ11,12を介してリザーバータンク1
3が接続されている。そして、該パイプ11,1
2にはそれぞれバルブ14,15が設けられてい
る。乾燥処理後、乾燥室1を常圧に戻すための空
気供給パイプ16は、該乾燥室1の上面に設置さ
れており、該空気供給パイプ16にはニードルバ
ルブ17が設けられている。
上記装置を使用して以下のとおり実施した。
実施例 1
粳米200gを30分間水浸漬し、常法通り電気釜
で炊飯した。このようにして得られた米飯100g
をトレイに入れ、ニードルバルブ17を閉じた状
態で乾燥室1の棚2上に置いた。これとは別にバ
ルブ9,14を閉じ、バルブ10,15を開いた
状態で真空ポンプ8を稼働せしめてリザーバータ
ンク13内を約30パスカルにまで減圧にする。そ
の後、バルブ15を閉じバルブ14を開いて乾燥
室1内を瞬時に約400パスカルにまで減圧した。
その後、バルブ14,15を閉じ、バルブ9,1
0を開の状態にして真空ポンプ8によつて乾燥室
1内の真空度を約40パスカルにした。減圧開始後
ほぼ3分間で自己氷結を終了し、その後2分後に
ヒーター3,4にスイツチを入れてトレイ中の自
己氷結した米飯を加熱乾燥した。この時の加熱乾
燥条件は、米飯の中心品温の昇温速度は6.5℃/
分となるような条件である。上記米飯の中心品温
が120℃になつた時に上記ヒーター3,4のスイ
ツチを切り、乾燥室1の外から冷却水を流して1
℃/分の冷却速度で40分間冷却して加熱乾燥を終
了した。この時の乾燥室1内の真空度は約80パス
カルであつた。その後、バルブ9,10を閉じ、
真空ポンプ8を停止し、乾燥室1上面のニードル
バルブ17を徐々に開いて空気供給パイプ16か
ら乾燥室1内に空気を供給して該乾燥室1内を常
圧に戻した後、該乾燥室1内からトレイを取り出
して水分含量約5重量%の即席乾燥米飯を得た。
このようにして得られた即席乾燥米飯の効果を確
認するために、以下のような比較例について実施
した。
比較例 1
減圧下における米飯の加熱乾燥条件として、米
飯の中心品温の昇温速度が1℃/分であること、
及び加熱乾燥終了時点の米飯の中心品温が50℃で
あること以外はすべて上記実施例と同一の方法お
よび条件で実施した。
比較例 2
加熱乾燥を開始する時間が自己氷結後27分後で
あること以外はすべて上記実施例と同一の方法お
よび条件で実施した。
比較例 3
加熱開始時間が自己氷結後27分後であること、
減圧下における米飯の加熱乾燥条件として、米飯
の中心品温の昇温速度が1℃/分であること、及
び加熱乾燥終了時点の米飯の中心品温が50℃であ
ること以外はすべて上記実施例と同一の方法およ
び条件で実施した。
比較結果を第1表に示す。
尚、比較項目は次の4項目である。
1 即席乾燥米飯の米粒付着程度
2 即席乾燥米飯の膨化程度
3 即席乾燥米飯の吸水速度
4 即席乾燥米飯の復元後の食感
5 即席乾燥米飯の外観
The present invention weakens the degree of adhesion of rice grains to each other after drying, making it possible to form a single rice grain with a small amount of external force, and the texture and flavor after restoration are dry by adding hot water etc. This invention relates to a method for producing instant dried rice that can be restored in a short time to almost the same texture and flavor as before. Many techniques have been developed for instant dry cooked rice that can be easily restored by adding hot water or the like. The present inventors have also developed a vacuum swelling drying method for foods as a technique for obtaining instant dried cooked rice with excellent restorability, especially texture after restoration (Japanese Patent Laid-Open Publication No. 40057/1983). The gist of the vacuum swelling and drying method for food is to place the food under a rapid vacuum state at a rate sufficient to cause the food to swell and to freeze the moisture in the food. The present invention relates to a vacuum swelling drying method for foods, which is characterized by post-heat drying and then returning to normal pressure. However, when drying rice using this method to make instant dried rice, if the rice grains stick to each other and form clumps, the clumps are broken down and the rice grains are broken down one by one. The drawback was that it was difficult to let go. The inventors of the present invention have conducted research on methods to eliminate such drawbacks. As a result, we obtained the knowledge that it is effective to pre-dry the cooked rice after washing it with water, and then apply the vacuum swelling drying method for the above-mentioned foods.
This method was previously filed as a method for producing instant dried rice (Japanese Patent Application Laid-Open No. 59-31659). However, according to this method, since the cooked rice is washed with water in advance, the flavor of the cooked rice is eluted, which slightly reduces the flavor of the final product. Therefore, after further intensive research, we came to the knowledge that the above-mentioned problems can be solved by drying under reduced pressure, especially by increasing the drying temperature, rather than pre-drying the cooked rice. Ivy. The gist of the present invention, which was completed based on these findings, is to cook cooked rice at a rate sufficient for the rice to puff up.
The rice is placed under reduced pressure to the extent that the water in the rice self-freezes, and heating and drying is started immediately or within 20 minutes after the water in the rice self-freezes, so that the core temperature of the rice is 100 to 150°C. After heating and drying the rice until it becomes dry, the moisture content is 10% by weight under conditions that do not burn the rice.
There is a method for producing instant dried cooked rice, which is characterized by holding the pressure until the pressure drops to below and then returning it to normal pressure. The method of the present invention will be explained in detail below. In the method of the present invention, rice cooked in a conventional manner is first placed under reduced pressure. However, when placing the cooked rice under reduced pressure, at least the following two conditions must be satisfied. The first condition is to subject the cooked rice to a certain reduced pressure quickly enough for puffing to occur. When cooked rice is placed under reduced pressure, the boiling point of the water in the cooked rice naturally decreases, thereby causing a phenomenon of transpiration of water, especially free water, in the cooked rice. When such a transpiration phenomenon occurs rapidly in a short period of time, the cooked rice puffs up. Therefore, the speed sufficient to cause the puffiness of cooked rice as used in the present invention refers to the speed sufficient to cause the moisture in the cooked rice to evaporate rapidly in a short period of time. Specifically, it is preferably within 1 second. The second condition is to set the specific degree of pressure reduction mentioned in the first condition to a degree of pressure reduction sufficient to cause the water in the cooked rice to self-freeze. The degree of vacuum sufficient for self-freezing of water in cooked rice as used in the present invention is generally about 609 Pascal or less, preferably about 106 Pascal or less. After the above two conditions are satisfied and the cooked rice is placed under reduced pressure, it is maintained until the water in the cooked rice self-freezes. By this process, the shape of the puffed cooked rice is maintained as it is, and the finally obtained dry cooked rice is brought into a puffed state, thereby making it possible to speed up the restoration using hot water or the like. There are the following two methods of reducing pressure to satisfy the above two conditions. The first method involves puffing the cooked rice and self-freezing of the water in the cooked rice in one step. In other words, the rice is heated under a reduced pressure sufficient to cause the water in the cooked rice to self-freeze. This is a fast method. According to this method, the swelling of the rice and the self-freezing of the water in the rice occur almost instantly. The second method involves puffing the rice and self-freezing of the water in the cooked rice in two stages, i.e., the rice is cooked under reduced pressure at a rate sufficient to cause puffing (but not enough to cause the water in the rice to self-freeze). (under reduced pressure that does not reach the degree of reduced pressure)
There is a method in which the cooked rice is expanded, and then the pressure is reduced to a level sufficient to cause the water in the cooked rice to self-freeze. According to this method, the swelling of the rice and the self-freezing of the water in the rice occur separately over time. From the viewpoint of achieving the object of the present invention, there is no problem in using any of the above methods, and both are included in the reduced pressure state of the present invention. After the water in the cooked rice is self-frozen, it is heated and dried using conventional heating methods such as heat transfer heating, infrared heating, and microwave heating. Immediately or within 20 minutes, preferably within 2 to 7 minutes, after self-freezing. Whether or not the water in the cooked rice has self-frozen can be easily confirmed by observing changes in the temperature of the center of the cooked rice. FIG. 1 schematically shows the change in core temperature of cooked rice over time during vacuum expansion treatment. As shown in FIG. 1, when cooked rice is treated under reduced pressure and expansion conditions, the temperature of the center of the cooked rice rapidly decreases to a supercooled state, but after that, the temperature of the center of the cooked rice rises slightly. The moment when the rise stops is when the water in the cooked rice freezes. Apart from this, it is also possible to judge from the appearance whether the cooked rice has become almost completely cloudy or not. That is, as the water in the cooked rice self-freezes, the cooked rice gradually becomes cloudy. The time when the water in the cooked rice self-freezes depends mainly on the degree of pressure reduction and the rate of pressure reduction, but the water in the cooked rice generally self-freezes about 3 minutes after the start of pressure reduction. Therefore, from another perspective, the timing of starting the heat drying is about 3 to 23 minutes, preferably about 5 to 10 minutes after the start of decompression. If heat drying is started too early, drying will occur even though self-freezing has not completely completed, resulting in noticeable dry thinning. On the other hand, if heating and drying is started too late, the adhesion of rice grains to each other due to self-freezing will become stronger and the surface will gradually dry, resulting in less adhesion between the dried rice grains. It becomes strong and does not break easily with a slight impact. This heating and drying removes frozen water from the cooked rice, and in this case, it is extremely important to increase the temperature of the core of the cooked rice as quickly as possible in order to achieve the object of the present invention. That is, by rapidly raising the temperature of the core of the cooked rice and rapidly evaporating the water in the cooked rice, many cavities are formed inside the cooked rice and the cooked rice is dried. Even if the dry cooked rice obtained in this manner is in the form of lumps, the degree of adhesion between the rice grains is weak and can be easily disintegrated into single grains by a slight external impact. Note that the core temperature of cooked rice in the present invention refers to the temperature detected by a temperature sensor inserted into the cooked rice. In order to obtain dried cooked rice having such an effect, it is preferable to carry out the heating drying at as high a temperature as possible without causing burnt rice.
Specifically, it is carried out until the temperature of the center of the cooked rice reaches 100 to 150°C, preferably 120 to 140°C. Center product temperature
If heating drying is terminated before the temperature reaches 100°C, dry thinning will appear. On the other hand, the center product temperature
When the temperature reaches 150 degrees Celsius or higher, the rice becomes noticeably burnt. When carrying out heat drying under the above conditions, it is better to increase the temperature of the core of the cooked rice as fast as possible, and specifically, it is preferably 5 to 7°C/min. After the core temperature of the cooked rice reaches 100 to 150°C, it is maintained under conditions that do not burn the rice until its water content becomes 10% by weight or less. This enables long-term storage of dried cooked rice. In this case, if heat conduction heating is used as the heating means, the considerably high temperature will continue even if the heat source is stopped, which may result in the rice becoming burnt. It is preferable to perform forced cooling by appropriate means. After completing heating and drying as described above, the pressure is returned to normal to obtain instant dried cooked rice. Next, an example of a specific apparatus that can be used to carry out the method of the present invention will be explained based on FIG. 2. Reference numeral 1 indicates a drying chamber, and inside the drying chamber 1, a shelf 2 for placing the processed material A is provided. Heaters 3 and 4 are installed below and above the shelf 2. A cold trap 6 is connected to the side wall of the drying chamber 1 via a pipe 5, and the cold trap 6 is connected to a vacuum pump 8 via a pipe 7. On the other hand, the pipes 5 and 7 are provided with valves 9 and 10, and a reservoir tank 1 is connected to the front and back of the pipe 5 via pipes 11 and 12.
3 is connected. And the pipe 11,1
2 are provided with valves 14 and 15, respectively. After the drying process, an air supply pipe 16 for returning the drying chamber 1 to normal pressure is installed on the top surface of the drying chamber 1, and the air supply pipe 16 is provided with a needle valve 17. The experiment was carried out as follows using the above apparatus. Example 1 200 g of glutinous rice was soaked in water for 30 minutes and cooked in an electric pot in the usual manner. 100g of cooked rice obtained in this way
was placed in a tray and placed on the shelf 2 of the drying chamber 1 with the needle valve 17 closed. Separately, the valves 9 and 14 are closed, and the vacuum pump 8 is operated with the valves 10 and 15 open to reduce the pressure in the reservoir tank 13 to about 30 Pascals. Thereafter, the valve 15 was closed and the valve 14 was opened to instantly reduce the pressure inside the drying chamber 1 to about 400 Pascals.
After that, valves 14 and 15 are closed, and valves 9 and 1 are closed.
0 was opened, and the degree of vacuum in the drying chamber 1 was brought to about 40 Pascal using the vacuum pump 8. Self-freezing was completed approximately 3 minutes after the start of decompression, and 2 minutes later, heaters 3 and 4 were turned on to heat and dry the self-frozen cooked rice in the tray. The heating and drying conditions at this time are as follows: The heating rate of the central part of the cooked rice is 6.5℃/
The conditions are such that the When the temperature of the center of the cooked rice reaches 120℃, turn off the heaters 3 and 4, and run cooling water from outside the drying chamber 1.
The heat drying was completed by cooling for 40 minutes at a cooling rate of °C/min. At this time, the degree of vacuum in the drying chamber 1 was approximately 80 Pascals. After that, close the valves 9 and 10,
After stopping the vacuum pump 8 and gradually opening the needle valve 17 on the top of the drying chamber 1 to supply air into the drying chamber 1 from the air supply pipe 16 to return the inside of the drying chamber 1 to normal pressure, the drying The tray was taken out from chamber 1 to obtain instant dried cooked rice with a water content of about 5% by weight.
In order to confirm the effects of the instant dry cooked rice obtained in this way, the following comparative examples were conducted. Comparative Example 1 The conditions for heating and drying cooked rice under reduced pressure are that the rate of increase in the temperature of the central part of the cooked rice is 1°C/min;
The test was carried out in the same manner and under the same conditions as in the above example except that the temperature of the center of the cooked rice at the end of heating and drying was 50°C. Comparative Example 2 All the methods and conditions were the same as in the above example except that the heat drying was started 27 minutes after self-freezing. Comparative Example 3 The heating start time is 27 minutes after self-freezing,
The conditions for heating and drying the cooked rice under reduced pressure were as follows: except that the rate of increase in the temperature of the center of the cooked rice was 1°C/min, and that the temperature of the center of the cooked rice at the end of the heating and drying was 50°C. It was carried out using the same method and conditions as in the example. The comparison results are shown in Table 1. The comparison items are the following four items. 1 Degree of rice grain adhesion in instant dried rice 2 Degree of swelling in instant dried rice 3 Water absorption rate of instant dried rice 4 Texture of instant dried rice after restoration 5 Appearance of instant dried rice
【表】
水分含量を測定した。
測定条件は105℃、16時間である。
第1表の実施例1と比較例1とを対比すること
により、自己氷結させた米飯の乾燥条件として米
飯の中心品温の昇温速度が速く且つ該米飯の乾燥
終了時点の中心品温を高くすることによつて、乾
燥時の米飯の縮みを防止することができる、とい
うことが明白になる。次に、実施例1と比較例2
とを対比することによつて、自己氷結させた米飯
の加熱乾燥開始時期を速くすることによつて、米
粒どうしの付着程度を弱くすることができるとい
うことが明白になる。次に、実施例1と比較例3
とを対比することによつて、自己氷結させた米飯
の乾燥開始時を速くし且つ米飯の中心品温の昇温
速度を速くすること、更には該米飯の乾燥終了時
の中心品温を高くすることによつて、米粒の付
着、膨化程度、復元性、復元後食感の全てを満足
することができる、ということが明らかとなる。
次に第3図〜第6図は実施例1と比較例3とに
よつて得られた即席乾燥米飯の米粒の断面組織の
電子顕微鏡写真である。第3図は実施例1の即席
乾燥米飯の米粒の断面組織全体を示すものであ
り、第4図はその部分的拡大写真である。第5図
は比較例3の即席乾燥米飯の米粒の断面組織全体
を示すものであり、第6図はこの部分的拡大図で
ある。
まず、第3図と第5図とを対比すると、米粒内
の空洞は実施例1の方が比較例3よりも大きくな
つている。このことから本発明の方が比較例3よ
りも吸水性・保水性に優れていること、その結果
復元性に優れている、ということが明確になる。
次に、第4図と第6図とを対比すると、実施例1
の方が米粒表面の肉厚が薄く且つ緻密になつてお
り、このことから、本発明の方が吸水性に優れて
いると共に復元後の食感に弾力性を付与し得る、
ということが明確になる。
以上のように、本発明の方法によつて得られる
即席乾燥米飯は、乾燥後における米粒どうしの付
着程度が弱く、少しの外力によつて一粒ずつの米
粒にすることが可能となり、且つ熱水等の注加に
より、復元後の食感、風味が乾燥前の米飯の食
感、風味とほとんど変わらない状態に短時間で復
元することができる。[Table] Moisture content was measured.
The measurement conditions were 105°C and 16 hours.
By comparing Example 1 and Comparative Example 1 in Table 1, it was found that the drying conditions for self-frozen cooked rice were such that the rate of temperature rise of the center part of the cooked rice was fast and the temperature of the center part at the end of drying of the cooked rice was It becomes clear that by increasing the height, it is possible to prevent the cooked rice from shrinking during drying. Next, Example 1 and Comparative Example 2
By comparing the above, it becomes clear that by accelerating the start of heating and drying of self-frozen cooked rice, the degree of adhesion of rice grains to each other can be weakened. Next, Example 1 and Comparative Example 3
By contrasting this with By doing so, it becomes clear that all of the requirements of rice grain adhesion, swelling degree, restorability, and texture after restoration can be satisfied. Next, FIGS. 3 to 6 are electron micrographs of cross-sectional structures of rice grains of instant dried cooked rice obtained in Example 1 and Comparative Example 3. FIG. 3 shows the entire cross-sectional structure of the rice grains of the instant dried cooked rice of Example 1, and FIG. 4 is a partially enlarged photograph thereof. FIG. 5 shows the entire cross-sectional structure of the rice grains of the instant dry cooked rice of Comparative Example 3, and FIG. 6 is a partially enlarged view of this. First, when comparing FIG. 3 and FIG. 5, the cavities inside the rice grains are larger in Example 1 than in Comparative Example 3. From this, it is clear that the present invention is superior to Comparative Example 3 in water absorption and water retention, and as a result, is superior in restorability.
Next, when comparing FIG. 4 and FIG. 6, Example 1
The surface of the rice grain is thinner and denser, and for this reason, the rice grain of the present invention has better water absorption and can impart elasticity to the texture after restoration.
That becomes clear. As described above, in the instant dried cooked rice obtained by the method of the present invention, the degree of adhesion of the rice grains to each other after drying is weak, and it is possible to separate the rice grains one by one with a small amount of external force. By adding water or the like, the texture and flavor after restoration can be restored in a short time to a state that is almost the same as the texture and flavor of cooked rice before drying.
第1図は減圧膨化処理時の米飯の中心品温の経
時的推移の概略を示す図面である。第2図は本発
明を実施するに当り使用し得る具体的装置の一例
を示す。第3図及び第4図は実施例1で得られた
即席乾燥米飯内部の繊維の形状を示す電子顕微鏡
写真であり、その倍率は第3図が30倍、第4図が
150倍である。第5図及び第6図は比較例3で得
られた即席乾燥米飯内部の繊維の形状を示す電子
顕微鏡写真であり、その倍率は第5図が30倍、第
6図が150倍である。
1……乾燥室、2……棚、3,4……ヒータ
ー、5,7,11,12……パイプ、6……コー
ルドトラツプ、8……真空ポンプ、9,10,1
4,15……バルブ、16……空気供給パイプ、
17……ニードルバルブ。
FIG. 1 is a diagram schematically showing the change over time in the core temperature of cooked rice during vacuum expansion treatment. FIG. 2 shows an example of a specific apparatus that may be used in carrying out the present invention. Figures 3 and 4 are electron micrographs showing the shape of the fibers inside the instant dried cooked rice obtained in Example 1, and the magnification is 30x in Figure 3 and 30x in Figure 4.
It is 150 times more. FIGS. 5 and 6 are electron micrographs showing the shape of the fibers inside the instant dried cooked rice obtained in Comparative Example 3, and the magnifications are 30x in FIG. 5 and 150x in FIG. 6. 1... Drying room, 2... Shelf, 3, 4... Heater, 5, 7, 11, 12... Pipe, 6... Cold trap, 8... Vacuum pump, 9, 10, 1
4, 15...Valve, 16...Air supply pipe,
17...Needle valve.
Claims (1)
この米飯中の水分が自己氷結する程度の減圧状態
下におき、この米飯中の水分が自己氷結した後直
ちにあるいは20分以内に加熱乾燥を開始し、その
米飯の中心品温が100〜150℃になるまで加熱乾燥
した後、米飯が焦げない条件で水分含量が10重量
%以下になるまで保持し、次いで常圧に戻すこと
を特徴とする即席乾燥米飯の製造法。 2 加熱乾燥条件が米飯の中心品温上昇が5〜7
℃/分となる条件であることを特徴とする特許請
求の範囲第1項記載の即席乾燥米飯の製造法。[Claims] 1. Cooking cooked rice at a rate sufficient to cause the cooked rice to swell.
The rice is placed under reduced pressure to the extent that the water in the rice self-freezes, and heating and drying is started immediately or within 20 minutes after the water in the rice self-freezes, so that the core temperature of the rice is 100 to 150°C. A method for producing instant dried cooked rice, which is characterized by heating and drying the rice until the rice becomes dry, then holding the rice under conditions that do not cause it to burn until the water content becomes 10% by weight or less, and then returning the pressure to normal pressure. 2 Heat drying conditions are such that the temperature of the main part of cooked rice rises between 5 and 7.
The method for producing instant dry cooked rice according to claim 1, characterized in that the conditions are such that the temperature is 0.degree. C./min.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59263869A JPS61141850A (en) | 1984-12-14 | 1984-12-14 | Production of instant dried boiled rice |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59263869A JPS61141850A (en) | 1984-12-14 | 1984-12-14 | Production of instant dried boiled rice |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61141850A JPS61141850A (en) | 1986-06-28 |
| JPH0437698B2 true JPH0437698B2 (en) | 1992-06-22 |
Family
ID=17395371
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59263869A Granted JPS61141850A (en) | 1984-12-14 | 1984-12-14 | Production of instant dried boiled rice |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61141850A (en) |
-
1984
- 1984-12-14 JP JP59263869A patent/JPS61141850A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61141850A (en) | 1986-06-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4794012A (en) | Method of manufacturing dried rice with pregelatinized starch content | |
| US2937946A (en) | Process for preparing quick cooking rice | |
| CN115191822B (en) | Rice cooking control method of pressure cooking appliance | |
| Luh | Quick-cooking rice | |
| US2720460A (en) | Production of quick-cooking rice | |
| JPH0437698B2 (en) | ||
| US3408202A (en) | Process for preparing a quick-cooking rice | |
| CN108477602A (en) | A kind of high-quality dendrobium candidum and its use changing temperature-pressure-difference and puffing drying means | |
| JPS5840057A (en) | Vacuum swelling drying method for food | |
| JPS6214255B2 (en) | ||
| JPH0154988B2 (en) | ||
| JPS6279750A (en) | Production of seasoned instant dried rice | |
| JPH0462701B2 (en) | ||
| JPS63237735A (en) | Production of fruit chips | |
| JP3220964B2 (en) | How to make fast-cooked rice | |
| JPH01153036A (en) | Production of dried carrot chip | |
| JP3252109B2 (en) | Method for producing processed brown rice | |
| JP7587899B1 (en) | Processed rice and its manufacturing method | |
| JPS63141542A (en) | Production of vegetable chips | |
| JP2759393B2 (en) | Strawberry snack manufacturing method | |
| JP2013066418A (en) | Processed rice and method for producing the same | |
| JPS59156272A (en) | Method for expanding and drying food under reduced pressure | |
| JPS59156273A (en) | Method for expanding and drying food under reduced pressure | |
| JPH09507762A (en) | Rapid rehydration beans | |
| JP2008131887A (en) | Process for producing processed rice that can be cooked in a microwave |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |