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JP4845654B2 - Method for producing puffed food - Google Patents
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JP4845654B2 - Method for producing puffed food - Google Patents

Method for producing puffed food Download PDF

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JP4845654B2
JP4845654B2 JP2006248888A JP2006248888A JP4845654B2 JP 4845654 B2 JP4845654 B2 JP 4845654B2 JP 2006248888 A JP2006248888 A JP 2006248888A JP 2006248888 A JP2006248888 A JP 2006248888A JP 4845654 B2 JP4845654 B2 JP 4845654B2
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molded product
rice flour
extruder
puffed food
powder
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JP2007111038A (en
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哲也 深谷
勝世志 木下
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Kagome Co Ltd
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Description

本発明は膨化食品の製造方法に関し、更に詳しくは例えばお湯を注ぐことにより短時間で本来の食品と同等の好ましい形状や食感等を有するものとなる膨化食品を製造する方法に関する。   The present invention relates to a method for producing a puffed food, and more particularly to a method for producing a puffed food that has a preferable shape and texture equivalent to that of the original food in a short time by pouring hot water, for example.

従来、前記のような膨化食品の製造方法として、米粉含有食用粉と水とをエクストルーダーに供して、これらを加圧加熱処理することにより該米粉含有食用粉に含まれる澱粉質をα化しつつ押出し成形すると同時に成形物を膨化することが行なわれている(例えば特許文献1〜3参照)。これらの従来法では、押出し成形した成形物を延伸したり、また米粉含有食用粉として米粉の他にこんにゃく精粉を含有するものを用いること等も行なわれているが、いずれも、米粉含有食用粉と水との混練物を比較的高温高圧下のエクストルーダーから低圧雰囲気下へ押出すときの相応に激しい水分の気化により押出し成形物を多孔質状のものに膨化している。   Conventionally, as a method for producing a puffed food as described above, rice flour-containing edible powder and water are subjected to an extruder, and these are subjected to pressure heat treatment, while the starch contained in the rice flour-containing edible powder is being alphatized. At the same time as extrusion molding, the molded product is expanded (see, for example, Patent Documents 1 to 3). In these conventional methods, an extruded molded product is stretched, or a rice flour-containing edible powder is used that contains konjac refined powder in addition to rice flour. When extruding a kneaded product of powder and water from an extruder under a relatively high temperature and high pressure into a low pressure atmosphere, the extrudate is expanded into a porous one by virtue of vigorous water vaporization.

しかし、かかる従来の製造方法には、押出し成形物の膨化品として得られる膨化食品に例えばお湯を注いで膨潤させると、形状が崩れ易く、また所謂へたった状態の食感の悪いものになってしまうという問題がある。
特開昭63−226246号公報 特開平5−123121号公報 特開2001−292730号公報
However, in such a conventional production method, for example, when hot water is poured into a puffed food obtained as a puffed product of an extrudate and swollen, the shape tends to collapse and the so-called stale texture is poor. There is a problem of end.
Japanese Unexamined Patent Publication No. 63-226246 JP-A-5-123121 JP 2001-292730 A

本発明が解決しようとする課題は、例えばお湯を注ぐことにより短時間で本来の食品と同等の好ましい形状や食感を有するものとなる膨化食品を製造する方法を提供する処にある。   The problem to be solved by the present invention is to provide a method for producing a puffed food having a preferable shape and texture equivalent to those of the original food in a short time by pouring hot water, for example.

前記の課題を解決する本発明は、平均粒径70〜150μmの米粉/こんにゃく精粉=90/10〜70/30(質量比)の割合で含有する米粉含有食用粉と水とを、米粉含有食用粉/水=80/20〜70/30(質量比)の割合でエクストルーダーに供して、これらを加圧加熱処理することにより該米粉含有食用粉に含まれる澱粉質をα化しつつ、得られる成形物が膨化しないよう該エクストルーダーから50〜85℃で押出し成形し、成形物を乾燥した後、膨化処理することを特徴とする膨化食品の製造方法に係る。   This invention which solves the above-mentioned subject contains rice flour containing rice flour-containing edible flour and water containing a ratio of rice flour / konnyaku refined powder having an average particle size of 70 to 150 μm = 90/10 to 70/30 (mass ratio). Edible powder / water = 80/20 to 70/30 (mass ratio), obtained by subjecting them to an extruder and subjecting them to pressurization and heat treatment, thereby converting the starch contained in the rice flour-containing edible powder into α. The present invention relates to a method for producing a puffed food, which is extruded from the extruder at 50 to 85 ° C. so as to prevent the puffed product from being puffed, dried, and then puffed.

本発明でも、米粉含有食用粉と水とをエクストルーダーに供して、これらを加圧加熱処理することにより該米粉含有食用粉に含まれる澱粉質をα化しつつ押出し成形する。本発明において、米粉含有食用粉としては、米粉とこんにゃく精粉や更には他の食材粉との混合物が挙げられ、かかる他の食材粉としては野菜粉末、海草粉末、香辛料粉末等が挙げられる。米粉とこんにゃく精粉とは、米粉/こんにゃく精粉=90/10〜70/30(質量比)の割合で含有するものを用いる。更に前記した他の食材粉をも用いるような場合には、(米粉とこんにゃく精粉との混合物)/他の食材粉=100/0〜75/25(質量比)の割合で含有するものを用いるのが好ましく、95/5〜85/15(質量比)の割合で含有するものを用いるのがより好ましい。そしていずれの場合も、米粉としては、平均粒径70〜150μmのものを用いる。   Also in the present invention, the rice flour-containing edible powder and water are subjected to an extruder and subjected to pressure and heat treatment to extrude the starch contained in the rice flour-containing edible powder while being gelatinized. In the present invention, the rice flour-containing edible powder includes a mixture of rice flour and konjac refined powder and further other food powder, and examples of such other food powder include vegetable powder, seaweed powder, and spice powder. As the rice flour and the konjac refined powder, those contained in a ratio of rice flour / konjac refined powder = 90/10 to 70/30 (mass ratio) are used. Furthermore, when using other above-mentioned foodstuff powders, what is contained in the ratio of (mixture of rice flour and konjac fine powder) / other foodstuff powder = 100/0 to 75/25 (mass ratio) It is preferable to use, and it is more preferable to use what is contained at a ratio of 95/5 to 85/15 (mass ratio). In either case, the rice flour having an average particle size of 70 to 150 μm is used.

また本発明において、米粉含有食用粉と水とは、これらを別々にエクストルーダーに供することもできるが、これらを予め混練しておいてからエクストルーダーに供するのが好ましい。そして双方は、米粉含有食用粉/水=80/20〜70/30(質量比)の割合でエクストルーダーに供する。エクストルーダーとしては、一軸、二軸又は三軸以上の多軸、更には同方向回転又は異方向回転等、各種形式のものを用いることができるが、なかでも一軸エクストルーダーを用いるのが好ましく、一軸非膨化型エクストルーダーを用いるのが特に好ましい。   In the present invention, the rice flour-containing edible powder and water can be separately supplied to an extruder, but it is preferable to knead them in advance before using them in the extruder. And both use for an extruder in the ratio of rice flour containing edible powder / water = 80 / 20-70 / 30 (mass ratio). As the extruder, it is possible to use various types such as uniaxial, biaxial or multi-axial, more than triaxial, and the same direction rotation or different direction rotation. Among them, it is preferable to use a uniaxial extruder. It is particularly preferable to use a uniaxial non-expanded extruder.

米粉含有食用粉と水とを前記したようにエクストルーダーに供して、これらを加圧加熱処理するときの加熱混練時の温度及び時間は通常40〜180℃で30〜180秒間、好ましくは90〜110℃で45〜75秒間とし、また押出し圧力(吐出圧力)は通常2〜15MPa、好ましくは4〜6MPaとする。かかる条件下で加圧加熱処理することによる押出し成形は押出しと成形とを分けて行なうこともできるが、同時に行なうのが好ましい。エクストルーダーから押出し成形して得られる成形物の形状としては、米粒状、球状、麺状、中実又は中空のショートパスタ状、シート状等、各種が挙げられる。かかる成形物の形状は、例えばエクストルーダーの押出し口に取付けるダイの形状によって変えることができる。   As described above, the rice flour-containing edible powder and water are subjected to an extruder as described above, and the temperature and time at the time of heating and kneading are usually 40 to 180 ° C. for 30 to 180 seconds, preferably 90 to 90 ° C. The temperature is 110 ° C. for 45 to 75 seconds, and the extrusion pressure (discharge pressure) is usually 2 to 15 MPa, preferably 4 to 6 MPa. Extrusion molding by pressurizing and heating under such conditions can be carried out separately from extrusion and molding, but it is preferable to perform them simultaneously. Examples of the shape of the molded product obtained by extrusion molding from an extruder include various types such as a rice granular shape, a spherical shape, a noodle shape, a solid or hollow short pasta shape, and a sheet shape. The shape of such a molded product can be changed depending on, for example, the shape of a die attached to the extrusion port of the extruder.

本発明では、以上説明したように、米粉含有食用粉と水とをエクストルーダーに供して、これらを加圧加熱処理することにより該米粉含有食用粉に含まれる澱粉質をα化しつつ押出し成形するが、かかる押出し成形を得られる成形物が膨化しないように行なう。前記したように、従来の製造方法では、エクストルーダーから成形物を押出すと同時に該成形物を膨化している。従来の製造方法では、比較的高温高圧下のエクストルーダーから低圧雰囲気下へ成形物を押出し、このとき該成形物に相応に激しい水分の気化を起こさせて、該成形物を多孔質状のものに膨化しているが、本発明では得られる成形物が膨化しないように押出し成形するのである。本発明者らの知見によれば、得られる成形物の膨化には、成形物の押出し成形に用いる混練物の水分や該混練物の形成に用いる米粉含有食用粉の粒度等、またエクストルーダーから成形物を押出すときの圧力や温度等が影響するが、エクストルーダーによる加圧加熱処理を通常の条件下で行なう限り、エクストルーダーから成形物を押出すときの温度の影響が大きく、得られる成形物の膨化をできるだけ確実に抑えるためには、エクストルーダーから成形物を50〜85℃で押出す。   In the present invention, as described above, the rice flour-containing edible powder and water are subjected to an extruder and subjected to pressure heating treatment to extrude while starching the starch contained in the rice flour-containing edible powder. However, it is carried out so that the molded product from which such extrusion molding can be obtained does not expand. As described above, in the conventional manufacturing method, a molded product is extruded from an extruder, and at the same time, the molded product is expanded. In the conventional manufacturing method, a molded product is extruded from an extruder under a relatively high temperature and high pressure into a low pressure atmosphere, and at this time, the molded product is caused to vaporize a corresponding amount of moisture, and the molded product is porous. However, in the present invention, extrusion molding is performed so that the molded product obtained does not expand. According to the knowledge of the present inventors, for the expansion of the obtained molded product, the moisture of the kneaded product used for extrusion molding of the molded product, the particle size of the rice flour-containing edible powder used for forming the kneaded product, etc., and from the extruder The pressure and temperature when extruding the molded product are affected, but as long as the pressure heating treatment with the extruder is performed under normal conditions, the temperature is greatly affected when the molded product is extruded from the extruder. In order to suppress the expansion of the molded product as reliably as possible, the molded product is extruded from an extruder at 50 to 85 ° C.

本発明では、以上説明したようにエクストルーダーから膨化することなく押出し成形した成形物を乾燥した後、膨化処理する。乾燥は60〜70℃で成形物の水分が10〜15質量%になるまで行なうのが好ましく、また膨化処理は乾燥した成形物を熱風雰囲気下にて200〜280℃で30〜180秒間加熱する処理が好ましく、220〜240℃で45〜75秒間加熱する処理がより好ましい。かくして乾燥し、膨化処理した成形物は適宜冷却する。   In the present invention, as described above, the molded product extruded without being expanded from the extruder is dried and then expanded. Drying is preferably performed at 60 to 70 ° C. until the moisture content of the molded product becomes 10 to 15% by mass, and the expansion treatment is performed by heating the dried molded product at 200 to 280 ° C. for 30 to 180 seconds in a hot air atmosphere. A treatment is preferable, and a treatment of heating at 220 to 240 ° C. for 45 to 75 seconds is more preferable. The molded product thus dried and expanded is appropriately cooled.

本発明では、以上説明した通り、米粉含有食用粉と水とをエクストルーダーに供して、これらを加圧加熱処理することにより該米粉含有食用粉に含まれる澱粉質をα化しつつ得られる成形物が膨化しないよう押出し成形する。この段階で得られる成形物は澱粉間のつながりが密な網目構造体となる。かかる成形物を乾燥することにより澱粉質のα化を維持しつつ、更に膨化処理することにより澱粉間のつながりが密な網目構造のままで多孔質構造体とする。かくして得られる膨化食品は、多孔質構造体であるため例えば湯戻りが良く、また湯戻りしたときに澱粉間のつながりが密な網目構造であるため所謂へたり感はなく、歯ごたえが良い。   In the present invention, as described above, a molded product obtained by subjecting rice flour-containing edible powder and water to an extruder and subjecting them to pressure and heat treatment while pregelatinizing starch contained in the rice flour-containing edible powder. Extrusion molding is performed so as not to swell. The molded product obtained at this stage becomes a network structure in which the starch is closely connected. The molded product is dried to maintain a starch gelatinized, and further expanded to obtain a porous structure with a tight network structure between starches. The puffed food thus obtained has a porous structure so that it can be reconstituted with hot water, for example, and when it is reconstituted, it has a dense network structure between starches, so there is no so-called feeling of sag and good texture.

本発明によると、例えばお湯を注ぐことにより短時間で本来の食品と同等の好ましい形状や食感を有するものとなる膨化食品を製造することができる。   According to the present invention, a puffed food that has a preferable shape and texture equivalent to that of the original food can be produced in a short time by pouring hot water, for example.

試験区分1(膨化食品の製造)
参考例1
平均粒径125μmの米粉75kgと水25kgとをミキサーで混練し、その混練物100kgを一軸エクストルーダー(エヌピー食品社製のMC−1102型)に供して加圧加熱処理することにより、米粉に含まれる澱粉質をα化しつつ、得られる成形物が膨化しないよう所定形状のダイを介して米粒状に押出し成形した。エクストルーダーの条件は、加熱混練時の温度及び時間を100℃で60秒間とし、また押出し圧力(吐出圧力)を5MPaとした。そして押出し成形部側(吐出部側)を冷却して押出し温度(吐出温度)を80℃とした。かくして押出し成形した成形物を多段乾燥機を用いて70℃で90分間乾燥し、水分を12質量%とした後、乾燥した成形物を熱風式オーブンを用いて230℃で60秒間熱風加熱することにより膨化処理し、室温まで冷却して、参考例1の膨化食品を製造した。
Test Category 1 (Manufacturing of puffed food)
Reference example 1
Included in rice flour by kneading 75 kg of rice flour with an average particle size of 125 μm and 25 kg of water with a mixer, and subjecting 100 kg of the kneaded product to a uniaxial extruder (MC 1102 manufactured by NP Foods) and pressurizing and heating. The resulting starchy product was extruded into a rice granule through a die having a predetermined shape so as to prevent the resulting molded product from expanding. Extruder conditions were such that the temperature and time during heat-kneading were 100 ° C. for 60 seconds, and the extrusion pressure (discharge pressure) was 5 MPa. And the extrusion molding part side (discharge part side) was cooled, and extrusion temperature (discharge temperature) was 80 degreeC. The molded product thus extruded is dried at 70 ° C. for 90 minutes using a multi-stage dryer to make the moisture content 12% by mass, and then the dried molded product is heated with hot air at 230 ° C. for 60 seconds using a hot air oven. The puffed food of Reference Example 1 was produced by puffing and cooling to room temperature.

参考例2
平均粒径125μmの米粉95kgとこんにゃく精粉5kgとをミキサーで混合した後、その混合物75kgと水25kgとをミキサーで混練し、その混練物100kgを一軸エクストルーダー(エヌピー食品社製のMC−1102型)に供して加圧加熱処理することにより、米粉に含まれる澱粉質をα化しつつ、得られる成形物が膨化しないよう所定形状のダイを介して米粒状に押出し成形した。エクストルーダーの条件は、加熱混練時の温度及び時間を100℃で60秒間とし、また押出し圧力(吐出圧力)を5MPaとした。そして押出し成形部側(吐出部側)を冷却して押出し温度(吐出温度)を80℃とした。かくして押出し成形した成形物を多段乾燥機を用いて70℃で90分間乾燥し、水分を12質量%とした後、乾燥した成形物を熱風式オーブンを用いて230℃で60秒間熱風加熱することにより膨化処理し、室温まで冷却して、参考例2の膨化食品を製造した。
Reference example 2
After mixing 95 kg of rice flour with an average particle size of 125 μm and 5 kg of konjac flour with a mixer, 75 kg of the mixture and 25 kg of water were kneaded with a mixer, and 100 kg of the kneaded product was uniaxial extruder (MC 1102 manufactured by NP Foods Co., Ltd.). The starch was included in the rice flour and was subjected to pressure and heat treatment, and the resulting starch was extruded into a rice granule through a die having a predetermined shape so as not to expand. Extruder conditions were such that the temperature and time during heat-kneading were 100 ° C. for 60 seconds, and the extrusion pressure (discharge pressure) was 5 MPa. And the extrusion molding part side (discharge part side) was cooled, and extrusion temperature (discharge temperature) was 80 degreeC. The molded product thus extruded is dried at 70 ° C. for 90 minutes using a multi-stage dryer to make the moisture content 12% by mass, and then the dried molded product is heated with hot air at 230 ° C. for 60 seconds using a hot air oven. The puffed food of Reference Example 2 was produced by puffing and cooling to room temperature.

実施例又は参考例3〜11
米粉含有食用粉として米粉とこんにゃく精粉とを用い、製造条件を表1記載のように変えたこと以外は参考例2と同様にして、実施例又は参考例3〜11の膨化食品を製造した。
Examples or Reference Examples 3 to 11
A puffed food of Examples or Reference Examples 3 to 11 was manufactured in the same manner as in Reference Example 2 except that rice flour and konjac refined powder were used as the rice flour-containing edible powder and the manufacturing conditions were changed as shown in Table 1. .

比較例1
平均粒径125μmの米粉75kgとこんにゃく精粉25kgとをミキサーで混合した後、その混合物75kgと水25kgとをミキサーで混練し、その混練物100kgを一軸エクストルーダー(エヌピー食品社製のMC−1102型)に供して加圧加熱処理することにより、米粉に含まれる澱粉質をα化しつつ、所定形状のダイを介して米粒状に押出し成形すると同時に成形物を膨化した。エクストルーダーの条件は、加熱混練時の温度及び時間を150℃で45秒間とし、また押出し圧力(吐出圧力)を7MPaとして、更に押出し温度(吐出温度)を加熱混練時の温度のままで150℃とした。かくして押出し成形すると同時に膨化した成形物を室温まで冷却して、比較例1の膨化食品を製造した。
Comparative Example 1
After mixing 75 kg of rice flour with an average particle size of 125 μm and 25 kg of konjac flour with a mixer, 75 kg of the mixture and 25 kg of water were kneaded with a mixer, and 100 kg of the kneaded product was uniaxial extruder (MC 1102 manufactured by NP Foods Co., Ltd.). By subjecting it to pressure and heat treatment, the starch was contained in the rice flour, and while extruding into a rice grain through a die having a predetermined shape, the molded product was expanded. The conditions of the extruder are as follows: the temperature and time during heating and kneading are set to 150 ° C. for 45 seconds, the extrusion pressure (discharge pressure) is set to 7 MPa, and the extrusion temperature (discharge temperature) is maintained at the same temperature as during heating and kneading. It was. Thus, the expanded product simultaneously with extrusion molding was cooled to room temperature, and the expanded food of Comparative Example 1 was produced.

参考例12
参考例1と同様にして参考例12の膨化食品を製造した。但しここでは、エクストルーダーから押出し成形して得られる成形物が膨化しないよう所定形状のダイを介して直径が2mmの球状に押出し成形した。
Reference Example 12
The puffed food of Reference Example 12 was produced in the same manner as Reference Example 1. However, in this case, the molded product obtained by extrusion molding from an extruder was extruded into a spherical shape having a diameter of 2 mm through a die having a predetermined shape.

実施例13
参考例2と同様にして実施例13の膨化食品を製造した。但しここでは、平均粒径125μmの米粉75kgとこんにゃく精粉25kgとをミキサーで混合した後、その混合物75kgと水25kgとをミキサーで混練し、その混練物100kgを一軸エクストルーダーに供して加圧加熱処理することにより、米粉に含まれる澱粉質をα化しつつ、得られる成形物が膨化しないよう所定形状のダイを介して直径が2mmの球状に押出し成形した。
Example 13
The puffed food of Example 13 was produced in the same manner as in Reference Example 2. However, here, 75 kg of rice flour having an average particle diameter of 125 μm and 25 kg of konjac flour are mixed with a mixer, and then 75 kg of the mixture and 25 kg of water are kneaded with a mixer, and 100 kg of the kneaded product is subjected to pressure using a uniaxial extruder. By heat-treating, the starch contained in the rice flour was converted into α and extruded into a spherical shape having a diameter of 2 mm through a die having a predetermined shape so that the resulting molded product did not expand.

比較例2
比較例1と同様にして比較例2の膨化食品を製造した。但しここでは、エクストルーダーに取付けた所定形状のダイを介して直径が2mmの球状に押出し成形すると同時にその成形物を膨化した。
Comparative Example 2
The puffed food of Comparative Example 2 was produced in the same manner as Comparative Example 1. However, in this case, the molded product was expanded at the same time as being extruded into a spherical shape having a diameter of 2 mm through a die having a predetermined shape attached to the extruder.

参考例14
参考例1と同様にして参考例14の膨化食品を製造した。但しここでは、エクストルーダーから押出し成形して得られる成形物が膨化しないよう所定形状のダイを介して直径が1.6mmで長さが20cmの麺状に押出し成形した。
Reference Example 14
The puffed food of Reference Example 14 was produced in the same manner as Reference Example 1. However, in this case, the molded product obtained by extrusion molding from an extruder was extruded into a noodle shape having a diameter of 1.6 mm and a length of 20 cm through a die having a predetermined shape.

実施例15
参考例2と同様にして実施例15の膨化食品を製造した。但しここでは、平均粒径125μmの米粉75kgとこんにゃく精粉25kgとをミキサーで混合した後、その混合物75kgと水25kgとをミキサーで混練し、その混練物100kgを一軸エクストルーダーに供して加圧加熱処理することにより、米粉に含まれる澱粉質をα化しつつ、得られる成形物が膨化しないよう所定形状のダイを介して直径が1.6mmで長さが20cmの麺状に押出し成形した。
Example 15
The expanded food of Example 15 was produced in the same manner as in Reference Example 2. However, here, 75 kg of rice flour having an average particle diameter of 125 μm and 25 kg of konjac flour are mixed with a mixer, and then 75 kg of the mixture and 25 kg of water are kneaded with a mixer, and 100 kg of the kneaded product is subjected to pressure using a uniaxial extruder. By heat-treating the starch contained in the rice flour, it was extruded into a noodle shape having a diameter of 1.6 mm and a length of 20 cm through a die having a predetermined shape so that the resulting molded product did not expand.

比較例3
比較例1と同様にして比較例3の膨化食品を製造した。但しここでは、エクストルーダーに取付けた所定形状のダイを介して直径が1.6mmで長さが20cmの麺状に押出し成形すると同時にその成形物を膨化した。
Comparative Example 3
The puffed food of Comparative Example 3 was produced in the same manner as Comparative Example 1. However, here, the molded product was expanded by simultaneously extruding into a noodle shape having a diameter of 1.6 mm and a length of 20 cm through a die having a predetermined shape attached to an extruder.

参考例16
参考例1と同様にして参考例16の膨化食品を製造した。但しここでは、エクストルーダーから押出し成形して得られる成形物が膨化しないよう所定形状のダイを介して長さが3cmのフジッリ(中実ショートパスタ)状に押出し成形した。
Reference Example 16
The puffed food of Reference Example 16 was produced in the same manner as Reference Example 1. However, here, the molded product obtained by extrusion molding from an extruder was extruded into a 3 cm long fusilli (solid short pasta) shape through a die having a predetermined shape.

実施例17
参考例2と同様にして実施例17の膨化食品を製造した。但しここでは、平均粒径125μmの米粉75kgとこんにゃく精粉25kgとをミキサーで混合した後、その混合物75kgと水25kgとをミキサーで混練し、その混練物100kgを一軸エクストルーダーに供して加圧加熱処理することにより、米粉に含まれる澱粉質をα化しつつ、得られる成形物が膨化しないよう所定形状のダイを介して長さが3cmのフジッリ(中実ショートパスタ)状に押出し成形した。
Example 17
The puffed food of Example 17 was produced in the same manner as in Reference Example 2. However, here, 75 kg of rice flour having an average particle diameter of 125 μm and 25 kg of konjac flour are mixed with a mixer, and then 75 kg of the mixture and 25 kg of water are kneaded with a mixer, and 100 kg of the kneaded product is subjected to pressure using a uniaxial extruder. By heat-treating, the starch contained in the rice flour was converted into α and extruded into a 3 cm long fusilli (solid short pasta) shape through a die having a predetermined shape so that the resulting molded product would not expand.

比較例4
比較例1と同様にして比較例4の膨化食品を製造した。但しここでは、エクストルーダーに取付けた所定形状のダイを介して長さが3cmのフジッリ(中実ショートパスタ)状に押出し成形すると同時にその成形物を膨化した。
Comparative Example 4
The puffed food of Comparative Example 4 was produced in the same manner as Comparative Example 1. However, here, the molded product was expanded at the same time as being extruded into a 3 cm long fusilli (solid short pasta) shape through a die having a predetermined shape attached to the extruder.

参考例18
参考例1と同様にして参考例18の膨化食品を製造した。但しここでは、エクストルーダーから押出し成形して得られる成形物が膨化しないよう所定形状のダイを介して長さが3cmのペンネ(中空ショートパスタ)状に押出し成形した。
Reference Example 18
The puffed food of Reference Example 18 was produced in the same manner as Reference Example 1. However, in this case, the molded product obtained by extrusion molding from an extruder was extruded into a penne (hollow short pasta) shape having a length of 3 cm through a die having a predetermined shape.

実施例19
参考例2と同様にして実施例19の膨化食品を製造した。但しここでは、平均粒径125μmの米粉75kgとこんにゃく精粉25kgとをミキサーで混合した後、その混合物75kgと水25kgとをミキサーで混練し、その混練物100kgを一軸エクストルーダーに供して加圧加熱処理することにより、米粉に含まれる澱粉質をα化しつつ、得られる成形物が膨化しないよう所定形状のダイを介して長さが3cmのペンネ(中空ショートパスタ)状に押出し成形した。
Example 19
The puffed food of Example 19 was produced in the same manner as in Reference Example 2. However, here, 75 kg of rice flour having an average particle diameter of 125 μm and 25 kg of konjac flour are mixed with a mixer, and then 75 kg of the mixture and 25 kg of water are kneaded with a mixer, and 100 kg of the kneaded product is subjected to pressure using a uniaxial extruder. By heat-treating, the starch contained in the rice flour was converted into α, and extruded into a penne (hollow short pasta) having a length of 3 cm through a die having a predetermined shape so that the resulting molded product did not expand.

比較例5
比較例1と同様にして比較例5の膨化食品を製造した。但しここでは、エクストルーダーに取付けた所定形状のダイを介して長さが3cmのペンネ(中空ショートパスタ)状に押出し成形すると同時にその成形物を膨化した。
Comparative Example 5
The puffed food of Comparative Example 5 was produced in the same manner as Comparative Example 1. However, here, the molded product was expanded at the same time as it was extruded into a 3 cm long penne (hollow short pasta) shape through a die having a predetermined shape attached to the extruder.

参考例20
参考例1と同様にして参考例20の膨化食品を製造した。但しここでは、エクストルーダーから押出し成形して得られる成形物が膨化しないよう所定形状のダイを介して厚さが2mmで縦及び横が各10cmの正方形のワンタン皮状に押出し成形した。
Reference Example 20
The puffed food of Reference Example 20 was produced in the same manner as Reference Example 1. However, in this case, the molded product obtained by extrusion molding from an extruder was extruded through a die having a predetermined shape into a square wonton skin shape having a thickness of 2 mm and a length and width of 10 cm each.

実施例21
参考例2と同様にして実施例21の膨化食品を製造した。但しここでは、平均粒径125μmの米粉75kgとこんにゃく精粉25kgとをミキサーで混合した後、その混合物75kgと水25kgとをミキサーで混練し、その混練物100kgを一軸エクストルーダーに供して加圧加熱処理することにより、米粉に含まれる澱粉質をα化しつつ、得られる成形物が膨化しないよう所定形状のダイを介して厚さが2mmで縦及び横が各10cmの正方形のワンタン皮状に押出し成形した。
Example 21
The puffed food of Example 21 was produced in the same manner as in Reference Example 2. However, here, 75 kg of rice flour having an average particle diameter of 125 μm and 25 kg of konjac flour are mixed with a mixer, and then 75 kg of the mixture and 25 kg of water are kneaded with a mixer, and 100 kg of the kneaded product is subjected to pressure using a uniaxial extruder. By heat-treating the starch contained in the rice flour into α, while the resulting molded product does not swell, it is formed into a square wonton skin with a thickness of 2 mm and a length and width of 10 cm each through a die having a predetermined shape. Extruded.

比較例6
比較例1と同様にして比較例6の膨化食品を製造した。但しここでは、エクストルーダーに取付けた所定形状のダイを介して厚さが2mmで縦及び横が各10cmの正方形のワンタン皮状に押出し成形すると同時にその成形物を膨化した。
以上の各例における製造条件を表1にまとめて示した。

























Comparative Example 6
The puffed food of Comparative Example 6 was produced in the same manner as Comparative Example 1. However, in this case, it was extruded into a square oneton skin shape having a thickness of 2 mm and a length and width of 10 cm each through a die having a predetermined shape attached to an extruder, and at the same time, the molding was expanded.
The production conditions in each of the above examples are summarized in Table 1.

























Figure 0004845654
Figure 0004845654

試験区分2(評価)
試験区分1で製造した各例の膨化食品について、テクスチャ評価及び官能評価を次のように行ない、総合評価した。結果を表2にまとめて示した。
Test category 2 (evaluation)
About the puffed food of each example manufactured by the test category 1, texture evaluation and sensory evaluation were performed as follows, and were comprehensively evaluated. The results are summarized in Table 2.

テクスチャ評価
各例の膨化食品15gに90℃のお湯200mlを加えてから3分後又は10分後のものについてテクスチャを全研社製の商品名TEXTUROMETER GTX−2(プランジャー:アクリル樹脂製の直径18mm、クリアランス0.3mm)を用いて測定した。
Texture Evaluation For 15 g of each example of puffed food, 200 ml of 90 ° C. hot water was added, and after 3 minutes or 10 minutes, the texture was given to the product name TEXTUROMETER GTX-2 (plunger: diameter made of acrylic resin) 18 mm, clearance 0.3 mm).

官能評価
各例の膨化食品15gに90℃のお湯200mlを加えてから3分後のものについて、男性10名及び女性10名の合計20名の官能評価員により、各参考例又は各実施例とこれらに対応する比較例との2点比較でどちらが好ましいかを評価した。具体的には、参考例又は実施例1〜11対比較例1、参考例12及び実施例13対比較例2、参考例14及び実施例15対比較例3、参考例16及び実施例17対比較例4、参考例18及び実施例19対比較例5、参考例20及び実施例21対比較例6の関係で2点比較した。表2には、各実施例を好ましいとした人数を記載した。尚、**は1%の危険率で有意であることを示し、また*は5%の危険率で有意であることを示す。
Sensory evaluation About 15 minutes after adding 200 ml of 90 ° C hot water to 15 g of puffed food of each example, a total of 20 sensory evaluators of 10 males and 10 females made each reference example or each example Which was preferable was evaluated by a two-point comparison with a comparative example corresponding to these. Specifically, Reference Example or Examples 1 to 11 vs. Comparative Example 1, Reference Example 12 and Example 13 vs. Comparative Example 2, Reference Example 14 and Example 15 vs. Comparative Example 3, Reference Example 16 and Example 17 vs. Two points were compared in the relationship of Comparative Example 4, Reference Example 18 and Example 19 vs. Comparative Example 5, Reference Example 20 and Example 21 vs. Comparative Example 6. Table 2 lists the number of persons preferred for each example. In addition, ** indicates that it is significant at a risk rate of 1%, and * indicates that it is significant at a risk rate of 5%.

総合評価
下記の基準で評価した。
◎:3分後及び10分後のテクスチャが2.5〜2.9kgの範囲内にあり、且つ官能評価の人数が18人以上。
○:3分後及び10分後のテクスチャが2.0〜2.4kg又は3.0〜3.4kgの範囲内にあり、且つ官能評価の人数が15〜17人。
△:3分後及び10分後のテクスチャが1.5〜1.9kg又は3.5kg以上。
×:3分後及び10分後のテクスチャが1.4kg以下。
Comprehensive evaluation The following criteria evaluated.
A: The texture after 3 minutes and 10 minutes is in the range of 2.5 to 2.9 kg, and the number of sensory evaluations is 18 or more.
○: The texture after 3 minutes and 10 minutes is in the range of 2.0 to 2.4 kg or 3.0 to 3.4 kg, and the number of sensory evaluations is 15 to 17 people.
(Triangle | delta): The texture after 3 minutes and 10 minutes is 1.5-1.9 kg or 3.5 kg or more.
X: The texture after 3 minutes and 10 minutes is 1.4 kg or less.

Figure 0004845654
Figure 0004845654

Claims (3)

平均粒径70〜150μmの米粉/こんにゃく精粉=90/10〜70/30(質量比)の割合で含有する米粉含有食用粉と水とを、米粉含有食用粉/水=80/20〜70/30(質量比)の割合でエクストルーダーに供して、これらを加圧加熱処理することにより該米粉含有食用粉に含まれる澱粉質をα化しつつ、得られる成形物が膨化しないよう該エクストルーダーから50〜85℃で押出し成形し、成形物を乾燥した後、膨化処理することを特徴とする膨化食品の製造方法。 Rice flour-containing edible powder and water containing rice flour / konnyaku refined powder with an average particle size of 70 to 150 μm = 90/10 to 70/30 (mass ratio) and rice flour-containing edible powder / water = 80/20 to 70/30 is subjected to the proportion in d custo ruder (mass ratio), One One turned into α the starch contained in該米powder containing edible powder by these heat treatment pressurized and, molded product obtained is not puffed cormorants the extruder molding press out at 50 to 85 ° C. from the chromatography, after drying the molded product, the production method of the puffed food, characterized in that the swelling process. 膨化処理が、乾燥した成形物を熱風雰囲気下にて200〜280℃で30〜180秒間加熱する処理である請求項1記載の膨化食品の製造方法。 Swelling process, method for producing puffed food of claim 1 Symbol mounting the dried molded product is a process to heat for 30 to 180 seconds at 200 to 280 ° C. under a hot air atmosphere. 成形物が米粒状物である請求項1又は2記載の膨化食品の製造方法。 The method for producing a puffed food according to claim 1 or 2 , wherein the molded product is a rice granule.
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