JP3474470B2 - Dashi juice production method - Google Patents
Dashi juice production methodInfo
- Publication number
- JP3474470B2 JP3474470B2 JP36020198A JP36020198A JP3474470B2 JP 3474470 B2 JP3474470 B2 JP 3474470B2 JP 36020198 A JP36020198 A JP 36020198A JP 36020198 A JP36020198 A JP 36020198A JP 3474470 B2 JP3474470 B2 JP 3474470B2
- Authority
- JP
- Japan
- Prior art keywords
- extraction
- juice
- dashi juice
- dashi
- hot water
- 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
- 235000011389 fruit/vegetable juice Nutrition 0.000 title claims description 52
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 238000000605 extraction Methods 0.000 claims description 52
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 26
- 241000251468 Actinopterygii Species 0.000 claims description 25
- 239000002245 particle Substances 0.000 claims description 24
- 239000000463 material Substances 0.000 claims description 17
- 235000019688 fish Nutrition 0.000 description 24
- AUHDWARTFSKSAC-HEIFUQTGSA-N (2S,3R,4S,5R)-3,4-dihydroxy-5-(hydroxymethyl)-2-(6-oxo-1H-purin-9-yl)oxolane-2-carboxylic acid Chemical compound [C@]1([C@H](O)[C@H](O)[C@@H](CO)O1)(N1C=NC=2C(O)=NC=NC12)C(=O)O AUHDWARTFSKSAC-HEIFUQTGSA-N 0.000 description 15
- GRSZFWQUAKGDAV-UHFFFAOYSA-N Inosinic acid Natural products OC1C(O)C(COP(O)(O)=O)OC1N1C(NC=NC2=O)=C2N=C1 GRSZFWQUAKGDAV-UHFFFAOYSA-N 0.000 description 15
- 229940028843 inosinic acid Drugs 0.000 description 15
- 235000013902 inosinic acid Nutrition 0.000 description 15
- 239000004245 inosinic acid Substances 0.000 description 15
- 238000000034 method Methods 0.000 description 8
- 239000000796 flavoring agent Substances 0.000 description 6
- 235000019634 flavors Nutrition 0.000 description 6
- 241000269821 Scombridae Species 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 4
- 235000020640 mackerel Nutrition 0.000 description 4
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- 241000269851 Sarda sarda Species 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- 241000282858 Hyracoidea Species 0.000 description 2
- 102220547770 Inducible T-cell costimulator_A23L_mutation Human genes 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 241001504592 Trachurus trachurus Species 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000004128 high performance liquid chromatography Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 235000015206 pear juice Nutrition 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 235000014347 soups Nutrition 0.000 description 2
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 2
- 241000555825 Clupeidae Species 0.000 description 1
- DJJCXFVJDGTHFX-UHFFFAOYSA-N Uridinemonophosphate Natural products OC1C(O)C(COP(O)(O)=O)OC1N1C(=O)NC(=O)C=C1 DJJCXFVJDGTHFX-UHFFFAOYSA-N 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 150000007523 nucleic acids Chemical class 0.000 description 1
- 102000039446 nucleic acids Human genes 0.000 description 1
- 108020004707 nucleic acids Proteins 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 229910000160 potassium phosphate Inorganic materials 0.000 description 1
- 235000011009 potassium phosphates Nutrition 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 235000019512 sardine Nutrition 0.000 description 1
- 235000019583 umami taste Nutrition 0.000 description 1
- DJJCXFVJDGTHFX-XVFCMESISA-N uridine 5'-monophosphate Chemical group O[C@@H]1[C@H](O)[C@@H](COP(O)(O)=O)O[C@H]1N1C(=O)NC(=O)C=C1 DJJCXFVJDGTHFX-XVFCMESISA-N 0.000 description 1
Landscapes
- Seeds, Soups, And Other Foods (AREA)
- Meat, Egg Or Seafood Products (AREA)
- Seasonings (AREA)
Description
【発明の詳細な説明】
【0001】
【発明の属する技術分野】本発明は魚節類の粉砕物を熱
水で抽出して得るダシ汁の製造方法であり、特定の粒度
の魚節類の粉砕物を用いることによりダシ汁の抽出時間
が短縮されるダシ汁の製造方法に関する。
【0002】
【従来の技術】魚節類に熱水を接触させてダシ汁を抽出
して得る方法において、魚節類は熱水との接触面積を大
きくするために、通常、粉砕物や薄く削られたものが用
いられ、工業的な規模でダシ汁を抽出する場合には、一
般に粉砕物が用いられる。従来、この魚節類の粉砕物
は、粗砕しただけのものであるため、魚節類の粉砕物の
粒度が大きく、しかも不均一である。このため、これを
用いて熱水と接触させてダシ汁を抽出すると、抽出時間
を一定に設定した場合には抽出操作毎に抽出率が変動し
て得られるダシ汁の風味がバラバラとなり、また逆に抽
出率を一定にしようとすると抽出時間がまちまちとな
る。このため短時間で抽出率が高く、しかも抽出率が一
定であり、かつ風味の優れたダシ汁を得ることが求めら
れている。
【0003】
【発明が解決しようとする課題】本発明は、魚節類の粉
砕物を熱水で抽出して得るダシ汁の製造方法において、
風味の優れた高抽出率のダシ汁を短時間で得ることを目
的とする。
【0004】
【課題を解決するための手段】本発明者らは、上記課題
を解決するために鋭意研究した結果、魚節類の粉砕物の
粒度を該魚節類の粉砕物全体の80重量%以上が粒径
0.25mm〜4mmとしたものを用いて熱水でダシ汁
を抽出したときは、従来の魚節類の粉砕物を用いて得る
ダシ汁に較べて短時間で風味の優れた高抽出率のダシ汁
が得られること、また該粉砕物の1〜10重量倍の熱水
を用いて向流多段抽出すると濃厚なダシが得られるこ
と、熱水の温度は85〜95℃、抽出時間は5〜50分
が好ましいことを知り、これらの知見に基づいて本発明
を完成した。すなわち本発明は、魚節類の粉砕物に熱水
を接触させてダシ汁を抽出するダシ汁の製造方法におい
て、該粉砕物が該粉砕物全体の80重量%以上が粒径
0.25mm〜4mmであり、該ダシ汁の抽出が該粉砕
物に1〜10重量倍の熱水を接触させ、温度85〜95
℃で5〜50分処理する向流多段抽出であることを特徴
とするダシ汁の製造方法である。
【0005】
【発明の実施の形態】本発明に用いる魚節類の粉砕物
は、例えば鰹節、宗田節、鮪節、鯖節、鯵節、鰯節など
の粉砕物が挙げられる。また例えば鰯、鯖、鯵などを干
して乾燥した煮干し類の粉砕物も挙げられる。そしてこ
れらの1種又は2種以上が用いられる。
【0006】本発明の魚節類の粉砕物の粒度は、魚節類
の粉砕物全体の80重量%以上が粒径0.25mm〜4
mmである。この粒度分布の魚節類の粉砕物を用いるこ
とにより、短時間で風味の優れた高抽出率のダシ汁が得
られる。一方、粒径0.25mm未満の粒径の粉砕物の
割合が増加して粒径0.25mm〜4mmの魚節類の粉
砕物の割合が魚節類の粉砕物全体の80重量%未満とな
ったものを用いて熱水と接触させると、熱水の上面に浮
いてしまう粉砕物が増加し、熱水との接触頻度が低下し
たり、連続式の向流抽出であると熱水と接触せずに流出
してしまい抽出率が低下する。また、粒径4mmを越え
る粒径の粉砕物の割合が増加して粒径0.25mm〜4
mmの魚節類の粉砕物の割合が魚節類の粉砕物全体の8
0重量%未満となったものを用いると、この粉砕物の表
面積が小さくなり抽出時間が長くなる。
【0007】本発明の特定粒度の魚節類の粉砕物を得る
方法は、通常の魚節類を粉砕できるものであればいずれ
でもよく、例えば、スイングカッタ−、ハンマ−ミル、
ロ−ルミル、ロッドミル、ピンミルなどで粉砕して所望
の粒度に調整することが好適な方法として挙げられる。
【0008】本発明の特定粒度の魚節類の粉砕物に接触
させる熱水の温度は、通常のダシ汁を抽出する温度であ
り、70〜98℃、好ましくは85〜95℃である。ま
た、ダシ汁を抽出する熱水の量は魚節類の粉砕物の重量
に対して1〜30倍の重量の熱水が用いられ、特に1〜
10倍量の熱水量で抽出すると濃厚なダシ汁が得られる
ので好ましい。そして、これの抽出時間は魚節類の種
類、使用量および熱水の量などにより異なるが5〜50
分である。
【0009】そして本発明の抽出操作はタンクなどを用
いた回分方式でもよいが、本発明は風味良好なダシ汁を
短時間に抽出して得ることが目的であるため、連続又は
半連続の向流多段抽出方式が好ましく、抽出時の香気成
分の飛散を防ぐために密閉式がより好ましい。
【0010】次いで上記方法で得られる抽出処理物を、
通常おこなわれている布などによる濾過や遠心分離など
により抽出残さを取り除き本発明のダシ汁を得る。この
ようにして風味に富んだダシ汁が短時間で得られる。
【0011】次に本発明の方法が従来の粒度を用いた抽
出方法と較べて短時間に良好なダシ汁が得られることを
実験例で示す。ダシ汁成分の代表的な旨味成分であるイ
ノシン酸量をダシ汁の抽出率の指標として、抽出時のダ
シ汁中のイノシン酸量の経時的変化を比較した。
(実験例)
(本発明例)「粉砕物全体の84重量%が粒径0.25
mm〜4mmである、鰹節の粉砕物10gを冷却管を付
けた150mlの三角フラスコに入れ、そこに熱水60
g(6倍重量)を加えてすばやく撹拌して、300ワッ
トの電熱器で抽出温度92〜94℃の還流加熱抽出をお
こなう」系を7系列作成し、抽出開始から、それぞれ1
0分後、15分後、20分後、25分後、30分後、3
5分後、40分後に1系列ずつ抽出処理を終了し、これ
らを濾紙濾過して各抽出時間毎のダシ汁を得て、これら
のダシ汁のイノシン酸量を測定した。
【0012】(従来の方法)「粒径4mmを越える粉砕
物の割合が39%で粉砕物全体の53重量%が粒径0.
25mm〜4mmである粉砕された鰹節10gを、上記
本発明例の実験で用いたものと同様な冷却管を付けた1
50mlの三角フラスコに入れ、次いでこれに熱水60
g(6倍重量)を加えて300ワットの電熱器で抽出温
度92〜94℃の還流加熱抽出をおこなう」系を7系列
作成し、還流加熱抽出開始10分後、15分後、20分
後、25分後、30分後、35分後、40分後に1系列
ずつ抽出処理を終了し、これらを濾紙濾過して各抽出時
間毎のダシ汁を得て、これらのダシ汁のイノシン酸量を
測定した。
【0013】上記実験例で得られた本発明と従来の方法
で得られたダシ汁中のイノシン酸量の経時的な変化を図
1に示す。なお、イノシン酸量の測定は高速液体クロマ
トグラフィ−を用いておこない、その測定条件は通常お
こなわれている核酸類の分析方法に準じておこなった。
すなわち、日本分光株式会社製の高速液体クロマトグラ
フィ−を用い、カラムをPolyamine II(Y
MC社製)とし、30mMリン酸第一カリウム:アセト
ニトリル=8:2を移動相として室温で、流速1ml/
min、波長254nmの吸光度により検出した。内部
標準物質は5´−UMP(シグマ社製)である。
【0014】図1に示すように従来の抽出方法ではイノ
シン酸量が0.58mg/ml以上となるダシ汁を得る
ためには30分以上の抽出時間を要することが判る。こ
れに対して本発明は抽出時間20分で同程度のイノシン
酸量のダシ汁が得られることが判る。このように本発明
の方法は従来の方法に較べて良好なダシ汁が短時間で得
られることが判る。
【0015】
【実施例】次に、実施例を挙げて本発明を説明する。
【0016】(実施例1)密閉式のパドル型連続向流抽
出機を用いて、粉砕物全体の82重量%が粒径0.25
mm〜4mmである粉砕された宗田節30Kg対して、
熱水240Kg(8倍重量)を92〜95℃で20分向
流接触させ、抽出処理をおこない、次いでこれを遠心分
離して抽出残さを除去して229Kgの風味の優れたダ
シ汁を得た。このダシ汁のイノシン酸量は0.68mg
/mlであった。
【0017】(比較例1)密閉式のパドル型連続向流抽
出機を用いて、粒径4mmを越える大きさの粉砕物の割
合が28%であり粉砕物全体の62重量%が粒径0.2
5mm〜4mmである粉砕された宗田節30Kgに熱水
240Kg(8倍重量)を92〜95℃で向流接触させ
て20分抽出処理をおこない、次いでこれを遠心分離し
て抽出残さを除去して230Kgのダシ汁を得た。この
ダシ汁のイノシン酸量は0.48mg/mlであった。
【0018】(実施例2)密閉式のパドル型連続向流抽
出機を用いて、粉砕物全体の93重量%が粒径0.25
mm〜4mmである粉砕された鯖節20Kgに対して熱
水200Kg(10倍重量)を92〜95℃で20分向
流接触させ抽出処理をおこない、次いでこれを遠心分離
して抽出残さを除去して191Kgの風味の優れたダシ
汁を得た。このダシ汁のイノシン酸量は0.61mg/
mlであった。
【0019】(比較例2)密閉式のパドル型連続向流抽
出機を用いて、粒径0.25mm未満の大きさの粉砕物
の割合が24%であり粉砕物全体の68重量%が粒径
0.25mm〜4mmである粉砕された鯖節20Kgに
対して、熱水200Kg(10倍重量)を92〜95℃
で20分向流接触させ抽出処理をおこない、次いでこれ
を遠心分離して抽出残さを除去して190Kgの風味の
優れたダシ汁を得た。このダシ汁のイノシン酸量は0.
49mg/mlであった。
【0020】このように実施例1及び比較例1で得たダ
シ汁のイノシン酸量の差、また実施例2及び比較例2で
得たダシ汁のイノシン酸量の差であきらかなように本発
明により高抽出率の良好なダシ汁が短時間で得られるこ
とが判る。
【0021】
【発明の効果】本発明によれば、風味の優れた高抽出率
のダシ汁が短時間に得られる。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing dashi soup obtained by extracting ground fish knots with hot water. The present invention relates to a method for producing dashi juice in which extraction time of dashi juice is reduced by using a ground product. [0002] In a method of extracting dashi juice by bringing hot water into contact with fish segments, the fish segments are usually crushed or thinned in order to increase the contact area with hot water. In the case of extracting dashi juice on an industrial scale, a ground material is generally used. Conventionally, since the crushed fish knots are merely coarsely crushed, the particle size of the crushed fish knots is large and non-uniform. For this reason, when using this to extract the dashi juice by contacting with hot water, if the extraction time is set to be constant, the flavor of the dashi juice obtained by varying the extraction rate for each extraction operation will vary, and Conversely, if the extraction rate is to be kept constant, the extraction time will vary. For this reason, it is required to obtain a dashi juice having a high extraction rate in a short time, a constant extraction rate, and excellent flavor. [0003] The present invention relates to a method for producing dashi juice obtained by extracting ground fish segments with hot water.
An object is to obtain a high-extraction rate dashi juice with excellent flavor in a short time. Means for Solving the Problems The inventors of the present invention have conducted intensive studies in order to solve the above-mentioned problems, and as a result, found that the particle size of the crushed fish knots was 80% by weight of the whole crushed fish knots. when extracting the broth juice at% or more with those having a particle diameter 0.25mm~4mm hot water, excellent flavor in a short time compared with the soup juice obtained using pulverized conventional smoked fish such Sashimi juice with a high extraction rate, and hot water 1 to 10 times the weight of the ground material.
Can be used to obtain a rich dashi.
And the hot water temperature is 85-95 ° C, and the extraction time is 5-50 minutes
Know it is preferred, the present invention has been completed based on these findings. That is, the present invention relates to a method for producing a dashi juice in which hot water is brought into contact with ground pulverized fish to extract dashi juice, wherein at least 80% by weight of the pulverized material has a particle size of 0.25 mm or more. 4 mm , and the extraction of the dashi juice is
1 to 10 times by weight of hot water is brought into contact with
A method for producing dashi juice, which is countercurrent multistage extraction at 5 ° C. for 5 to 50 minutes . DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Examples of crushed fish knots used in the present invention include crushed bonito, soda knot, tuna knot, saba knot, mackerel knot and horse mackerel knot. In addition, for example, pulverized dried sardines, mackerel, horse mackerel and the like may be used. One or two or more of these are used. The particle size of the crushed fish segments of the present invention is such that 80% by weight or more of the whole crushed fish segments has a particle size of 0.25 mm to 4%.
mm. By using the crushed fish knots having such a particle size distribution, a dashi juice having an excellent flavor and a high extraction rate can be obtained in a short time. On the other hand, the ratio of the crushed material having a particle size of less than 0.25 mm is increased so that the ratio of the crushed fish segments having a particle size of 0.25 mm to 4 mm is less than 80% by weight of the whole crushed fish segment. When it comes into contact with hot water, the amount of crushed material that floats on the top surface of hot water increases, the frequency of contact with hot water decreases, or if continuous countercurrent extraction is used, hot water It flows out without contact and the extraction rate decreases. In addition, the ratio of the pulverized material having a particle size exceeding 4 mm increases, and
mm of fish crushed fish is 8% of the total crushed fish
If less than 0% by weight is used, the surface area of the pulverized material becomes smaller and the extraction time becomes longer. The method of the present invention for obtaining a crushed fish knot of a specific particle size may be any method which can grind ordinary fish knots, such as a swing cutter, a hammer mill, and the like.
As a suitable method, pulverization with a roll mill, a rod mill, a pin mill or the like to adjust the particle size to a desired value can be mentioned. [0008] The temperature of the hot water to be brought into contact with the pulverized fish knots of a specific particle size according to the present invention is a temperature at which ordinary dashi juice is extracted, and is 70 to 98 ° C, preferably 85 to 95 ° C. In addition, the amount of hot water for extracting the dashi juice is 1 to 30 times the weight of the weight of the crushed fish knots, and particularly 1 to 30 times.
Extraction with 10 times the amount of hot water is preferable because a thick dashi juice can be obtained. The extraction time varies depending on the type of fish knot, the amount used, the amount of hot water, and the like.
Minutes. The extraction operation of the present invention may be performed in a batch system using a tank or the like. However, since the present invention aims to extract flavored dashi juice in a short period of time, continuous or semi-continuous extraction is desired. A flow multistage extraction system is preferable, and a closed system is more preferable in order to prevent fragrance components from scattering at the time of extraction. Next, the extracted product obtained by the above method is
The extraction residue is removed by the usual filtration using a cloth or the like or centrifugation to obtain the dashi juice of the present invention. In this way, a flavorful dashi juice can be obtained in a short time. Next, experimental examples show that the method of the present invention can provide a good pear juice in a short time as compared with the conventional extraction method using particle size. Using the amount of inosinic acid, which is a representative umami component of the dash juice component, as an index of the extraction rate of the dash juice, the change over time in the amount of inosinic acid in the dash juice during extraction was compared. (Experimental example) (Example of the present invention) "84% by weight of the whole pulverized material has a particle size of 0.25.
10 g of crushed bonito flakes having a size of 4 mm to 4 mm are put into a 150 ml Erlenmeyer flask equipped with a cooling tube, and hot water 60
g (6 times the weight), and rapidly agitate, and perform reflux heating extraction at an extraction temperature of 92 to 94 ° C. with a 300-watt electric heater.
0 minutes, 15 minutes, 20 minutes, 25 minutes, 30 minutes, 3 minutes
After 5 minutes and 40 minutes, the extraction process was terminated one line at a time, and these were filtered through filter paper to obtain dassi juice for each extraction time, and the inosinic acid content of the dasi juice was measured. (Conventional method) "The proportion of the pulverized material having a particle size exceeding 4 mm is 39%, and 53% by weight of the whole pulverized material has a particle size of 0.3%.
10 g of the ground bonito having a size of 25 mm to 4 mm was provided with a cooling pipe similar to the one used in the experiment of the present invention.
Place in a 50 ml Erlenmeyer flask, then add hot water 60
g (6 times the weight), and perform a reflux heating extraction at an extraction temperature of 92 to 94 ° C. using a 300-watt electric heater. ”7 systems were prepared, and 10 minutes, 15 minutes, and 20 minutes after the reflux heating extraction was started. After 25 minutes, 30 minutes, 35 minutes, and 40 minutes, the extraction process was terminated for each line, and these were filtered through filter paper to obtain dassi juice for each extraction time, and the amount of inosinic acid in these dasi juices was determined. Was measured. FIG. 1 shows the change over time in the amount of inosinic acid in dashi juice obtained by the present invention and the conventional method obtained in the above experimental examples. The measurement of the amount of inosinic acid was carried out by using high performance liquid chromatography, and the measurement conditions were carried out in accordance with the usual method of analyzing nucleic acids.
That is, using high performance liquid chromatography manufactured by JASCO Corporation, the column was made of Polyamine II (Y
MC) and 30 mM potassium phosphate: acetonitrile = 8: 2 as a mobile phase at room temperature at a flow rate of 1 ml /
min, detected by absorbance at a wavelength of 254 nm. The internal standard is 5'-UMP (manufactured by Sigma). As shown in FIG. 1, it can be seen that in the conventional extraction method, an extraction time of 30 minutes or more is required to obtain a dashi juice having an inosinic acid content of 0.58 mg / ml or more. On the other hand, it can be seen that the present invention provides a dashi juice having the same amount of inosinic acid in an extraction time of 20 minutes. Thus, it can be seen that the method of the present invention can provide better dashi juice in a shorter time than the conventional method. Next, the present invention will be described with reference to examples. (Example 1) Using a closed paddle type continuous countercurrent extractor, 82% by weight of the whole pulverized product had a particle size of 0.25.
crushed Soda Section 30 kg that is 4 mm to 4 mm,
240 Kg (8 times the weight) of hot water was brought into countercurrent contact at 92 to 95 ° C. for 20 minutes to perform an extraction treatment, and then centrifuged to remove the extraction residue to obtain 229 Kg of flavored dashi juice. . The inosinic acid content of this dashi juice is 0.68mg
/ Ml. (Comparative Example 1) Using a closed paddle type continuous countercurrent extractor, the ratio of pulverized material having a particle size exceeding 4 mm was 28%, and 62% by weight of the whole pulverized material was 0% in particle size. .2
240 kg (8 times the weight) of hot water is brought into countercurrent contact with 30 kg of crushed Muneda knots of 5 mm to 4 mm at 92 to 95 ° C. to perform extraction processing for 20 minutes, and then centrifuged to remove extraction residues. 230 kg of pear juice was obtained. The amount of inosinic acid in this dashi juice was 0.48 mg / ml. (Example 2) Using a closed paddle type continuous countercurrent extractor, 93% by weight of the whole pulverized product had a particle size of 0.25.
200 kg (10 times the weight) of hot water is contacted countercurrently at 20 to 95 ° C. for 20 minutes with 20 kg of ground mackerel, which is 4 mm to 4 mm, to perform extraction processing, and then centrifuged to remove extraction residues. As a result, 191 kg of an excellent flavored dashi juice was obtained. The inosinic acid content of this dashi juice is 0.61 mg /
ml. (Comparative Example 2) Using a closed paddle type continuous countercurrent extractor, the ratio of pulverized material having a particle size of less than 0.25 mm was 24%, and 68% by weight of the whole pulverized material was particles. 200 kg of hot water (10 times weight) is added to 92-95 ° C. with respect to 20 kg of ground pulverized mackerel having a diameter of 0.25 mm to 4 mm.
And then subjected to extraction treatment for 20 minutes, and then centrifuged to remove extraction residues to obtain 190 kg of flavored dashi juice. The amount of inosinic acid in this dashi juice is 0.
It was 49 mg / ml. Thus, the difference in the amount of inosinic acid in the dashi juice obtained in Example 1 and Comparative Example 1 and the difference in the amount of inosinic acid in the dashi juice obtained in Example 2 and Comparative Example 2 were clearly determined. It can be seen that the invention makes it possible to obtain good dashi juice with a high extraction rate in a short time. According to the present invention, dashi juice having excellent flavor and high extraction rate can be obtained in a short time.
【図面の簡単な説明】
【図1】本発明と従来法との、ダシ汁抽出時のダシ汁中
のイノシン酸量の経時的変化の比較を表す。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 shows a comparison of the change over time in the amount of inosinic acid in dashi juice during extraction of dashi juice between the present invention and the conventional method.
フロントページの続き (56)参考文献 特開 平10−14525(JP,A) 特開 平9−308455(JP,A) 特開 昭56−154977(JP,A) (58)調査した分野(Int.Cl.7,DB名) A23L 1/22 - 1/221 A23L 1/39 - 1/40 Continuation of the front page (56) References JP-A-10-14525 (JP, A) JP-A-9-308455 (JP, A) JP-A-56-154977 (JP, A) (58) Fields investigated (Int) .Cl. 7 , DB name) A23L 1/22-1/221 A23L 1/39-1/40
Claims (1)
を抽出するダシ汁の製造方法において、該粉砕物が該粉
砕物全体の80重量%以上が粒径0.25mm〜4mm
であり、該ダシ汁の抽出が該粉砕物に1〜10重量倍の
熱水を接触させ、温度85〜95℃で5〜50分処理す
る向流多段抽出であることを特徴とするダシ汁の製造方
法。(57) [Claims 1] In a method for producing dashi juice, wherein hot water is brought into contact with ground pulverized fish pieces to extract dashi juice, the pulverized material is 80% by weight of the whole pulverized material. % Is the particle size of 0.25mm ~ 4mm
The extraction of the dashi juice is 1 to 10 times the weight of the pulverized material.
Contact with hot water and treat at 85-95 ° C for 5-50 minutes
A method for producing dashi juice, comprising multi-stage countercurrent extraction .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP36020198A JP3474470B2 (en) | 1998-12-18 | 1998-12-18 | Dashi juice production method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP36020198A JP3474470B2 (en) | 1998-12-18 | 1998-12-18 | Dashi juice production method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000175652A JP2000175652A (en) | 2000-06-27 |
| JP3474470B2 true JP3474470B2 (en) | 2003-12-08 |
Family
ID=18468347
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP36020198A Expired - Lifetime JP3474470B2 (en) | 1998-12-18 | 1998-12-18 | Dashi juice production method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3474470B2 (en) |
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1998
- 1998-12-18 JP JP36020198A patent/JP3474470B2/en not_active Expired - Lifetime
Also Published As
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|---|---|
| JP2000175652A (en) | 2000-06-27 |
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