JP2016198089A - Smoked food - Google Patents
Smoked food Download PDFInfo
- Publication number
- JP2016198089A JP2016198089A JP2016074577A JP2016074577A JP2016198089A JP 2016198089 A JP2016198089 A JP 2016198089A JP 2016074577 A JP2016074577 A JP 2016074577A JP 2016074577 A JP2016074577 A JP 2016074577A JP 2016198089 A JP2016198089 A JP 2016198089A
- Authority
- JP
- Japan
- Prior art keywords
- smoked
- smoke
- food
- heating
- temperature
- 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.)
- Granted
Links
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Abstract
Description
本発明は、燻製食品に関し、詳細には植物原料の種類を変更することなく製造でき、かつ、加熱されても香りが減弱及び消失しにくい燻製食品に関する。 The present invention relates to a smoked food, and more particularly to a smoked food that can be produced without changing the type of plant raw material and that does not easily lose or lose its fragrance even when heated.
燻製は元来、食品の保存性を高めることが目的であったが、食品保存技術が発達した現在では、食品に燻煙由来の好ましい風味を付与することが主目的となっている。そのため、燻製食品の風味に大きく影響する燻煙の質をコントロールすることが、非常に重要となっている。 Smoked food was originally intended to improve the preservability of foods, but now that food preservation technology has been developed, the main purpose is to give foods a favorable flavor derived from smoke. Therefore, it is very important to control the quality of smoke that greatly affects the flavor of smoked foods.
燻煙の質をコントロールする方法に関し、植物原料の燃焼、不完全燃焼又は熱分解によって発生させた燻煙を加熱することにより、燻煙の質をコントロールし、且つベンツピレン等の有害成分を低減させ、燻製食品に好ましい風味を付与できることが報告されている（特許文献１）。 Concerning methods for controlling the quality of soot, heating the soot generated by burning, incomplete combustion or pyrolysis of plant raw materials to control the quality of soot and reduce harmful components such as benzpyrene It has been reported that a preferred flavor can be imparted to smoked foods (Patent Document 1).
一方、特許文献２には、１−ペンテン−３−オール等の香料を添加した魚節の製造方法が記載されている。 On the other hand, Patent Document 2 describes a method for producing fish clauses to which a fragrance such as 1-penten-3-ol is added.
特許文献３には、（Ｅ，Ｚ，Ｚ）−２，４，７−トリデカトリエナールを有効成分とする魚節香味改善剤が記載されている。 Patent Document 3 describes a fish-blossom flavor improving agent containing (E, Z, Z) -2,4,7-tridecatrienal as an active ingredient.
非特許文献１には、鰹節の香気成分の、焙乾中の変化が記載されている。 Non-Patent Document 1 describes changes during roasting of the aroma component of bonito.
燻製食品は、食品や調味料の原料として用いられ得るが、燻製食品の香りは加熱によって減弱又は消失しやすいという問題がある。そのため、例えば、長時間の加熱調理によって製造される食品（例、煮込み料理等）や調理後に再加熱される食品等は、燻製食品を原料として用いても、最終的に喫食する際には、燻製食品の香りは殆ど感じられない。 Smoked foods can be used as a raw material for foods and seasonings, but there is a problem that the scent of smoked foods tends to be attenuated or disappeared by heating. Therefore, for example, foods produced by cooking for a long time (e.g., stewed dishes), foods reheated after cooking, etc., even when smoked foods are used as raw materials, The smell of smoked food is hardly felt.
植物原料を燃焼、不完全燃焼、又は熱分解して発生させた燻煙を、原料食品に接触又は付着させた燻製食品において、植物原料の種類を変えることで、燃焼等により発生する燻煙の質を変えることは可能である。しかし、製造に用いる植物原料の種類を変更すると、目的とする好ましい香りの質が損なわれてしまい、香りの質が大きく異なる燻製食品になってしまう場合もあるという課題がある。従って、燻煙由来の好ましい香りを有し、かつ、加熱されても香りが減弱及び消失しにくい燻製食品の実現は極めて困難であった。 In smoked foods produced by burning, incompletely burning, or pyrolyzing plant materials, and contacting or adhering to the raw material foods, changing the type of plant material changes the type of smoke generated by combustion, etc. It is possible to change the quality. However, when the kind of plant raw material used for manufacture is changed, there is a problem that the desired desirable scent quality is impaired, and the smoked food may be greatly different in scent quality. Therefore, it has been extremely difficult to realize a smoked food having a preferable scent derived from smoke and having a fragrance that is not easily attenuated or lost even when heated.
本発明の目的は、植物原料の種類を変更することなく製造でき、かつ、加熱されても香りが減弱及び消失しにくい燻製食品を提供することにある。 An object of the present invention is to provide a smoked food that can be produced without changing the type of plant raw material and that does not easily lose or lose its fragrance even when heated.
本発明者らは、上記課題に対して鋭意検討した結果、驚くべきことに、燻製食品の揮発性成分のガスクロマトグラムにおける、ケトン類、フェノール類及び窒素化合物のピーク面積の各総和が特定の比率である燻製食品は、植物原料の種類を変更せずに製造でき、かつ、加熱しても香りが減弱及び消失しにくいことを見出し、かかる知見に基づいてさらに研究を進めることによって本発明を完成するに至った。
即ち、本発明は以下の通りである。
As a result of intensive studies on the above problems, the present inventors have surprisingly found that the sum of peak areas of ketones, phenols and nitrogen compounds in a gas chromatogram of volatile components of smoked foods has a specific ratio. Smoked foods that can be produced without changing the type of plant raw material, and the scent is less likely to be attenuated and disappear even when heated, and the present invention is completed by further research based on this knowledge It came to do.
That is, the present invention is as follows.
［１］燻製食品の揮発性成分のガスクロマトグラムにおける、ケトン類のピーク面積の総和をＡとし、フェノール類のピーク面積の総和をＢとし、且つ窒素化合物のピーク面積の総和をＣとするとき、
Ａ：（Ｂ＋Ｃ）が、１５〜３５：４５〜７５である、燻製食品。
［２］更に、燻製食品の揮発性成分のガスクロマトグラムにおける、炭化水素類のピーク面積の総和をＤとするとき、
Ａ：Ｄが、１５〜３５：５〜１０である、［１］記載の燻製食品。
［３］燻製食品の揮発性成分のガスクロマトグラムにおける全成分のピーク面積の総和に占める前記Ａの割合が、１５〜３５％である、［１］又は［２］記載の燻製食品。
［４］魚を原料とする、［１］〜［３］のいずれか１つに記載の燻製食品。
［５］魚節である、［１］〜［４］のいずれか１つに記載の燻製食品。
[1] When the sum of the peak areas of ketones in the gas chromatogram of volatile components of smoked food is A, the sum of the peak areas of phenols is B, and the sum of the peak areas of nitrogen compounds is C,
A: (B + C) is 15-35: 45-75 smoked food.
[2] Furthermore, when the sum total of the peak areas of hydrocarbons in the gas chromatogram of volatile components of smoked food is D,
The smoked food according to [1], wherein A: D is 15 to 35: 5 to 10.
[3] The smoked food according to [1] or [2], wherein the ratio of A to the total peak area of all components in the gas chromatogram of volatile components of the smoked food is 15 to 35%.
[4] The smoked food according to any one of [1] to [3], using fish as a raw material.
[5] The smoked food according to any one of [1] to [4], which is a fish clause.
本発明によれば、加熱されても香りが減弱及び消失しにくい燻製食品を提供することができる。特に、本発明により提供される加熱されても香りが減弱及び消失しにくい燻製食品は、使用する植物原料の種類を変更することなく製造し得るため、目的とする好ましい香りの質が損なわれることなく、燻煙由来の好ましい香りを有し得る。 ADVANTAGE OF THE INVENTION According to this invention, the smoked food which a fragrance is hard to attenuate and lose | disappear even if heated can be provided. In particular, the smoked food provided by the present invention that does not weaken and disappear even when heated can be produced without changing the type of plant material used, so that the desired fragrance quality is impaired. And may have a preferred scent derived from smoke.
本発明の燻製食品の揮発性成分のガスクロマトグラムにおける、ケトン類のピーク面積の総和をＡとし、フェノール類のピーク面積の総和をＢとし、且つ窒素化合物のピーク面積の総和をＣとするとき、Ａ：（Ｂ＋Ｃ）は、好ましくは１５〜３５：４５〜７５であり、より好ましくは２０〜３０：５０〜７０である。当該Ａ：（Ｂ＋Ｃ）が、上記の範囲内であることにより、加熱後においても、加熱前の燻煙由来の好ましい香りを維持することができ、かつ当該香りが減弱及び消失しにくい燻製食品を提供できることとなる。
本発明の燻製食品の揮発性成分のガスクロマトグラムにおける、ケトン類のピーク面積の総和をＡとし、フェノール類のピーク面積の総和をＢとし、且つ窒素化合物のピーク面積の総和をＣとするとき、全揮発性成分のピーク面積の総和は１００とすることが好ましい。
In the gas chromatogram of the volatile components of the smoked food of the present invention, when the sum of the peak areas of ketones is A, the sum of the peak areas of phenols is B, and the sum of the peak areas of nitrogen compounds is C, A: (B + C) is preferably 15 to 35:45 to 75, and more preferably 20 to 30:50 to 70. By the said A: (B + C) being in said range, the smoked food which can maintain the preferable fragrance derived from the smoke before heating, and the said fragrance is hard to attenuate and lose | disappear after heating. It can be provided.
In the gas chromatogram of the volatile components of the smoked food of the present invention, when the sum of the peak areas of ketones is A, the sum of the peak areas of phenols is B, and the sum of the peak areas of nitrogen compounds is C, The total peak area of all volatile components is preferably 100.
本発明の燻製食品の揮発性成分のケトン類は、分子内に１つ以上のケトン基を有する有機化合物をいい、例えば、２，３−ペンタンジオン、シクロペンタノン、２−メチルシクロペンタノン、２，５−ジメチル−２−シクロペンテノン、２−シクロペンテン−１−オン、２−メチル−２−シクロペンテノン、２，３−ジメチル−２−シクロペンテン−１−オン、３，４−ジメチル−２−シクロペンテン−１−オン、２，３，４−トリメチル−２−シクロペンテン−１−オン、ブチロラクトン、３−エチル−２−シクロペンテン−１−オン、３−メチルシクロヘキサノン、３−メチルアセトフェノン、１−メチルインダン−２−オン等が挙げられる。 The volatile ketones of the smoked food of the present invention refer to organic compounds having one or more ketone groups in the molecule, such as 2,3-pentanedione, cyclopentanone, 2-methylcyclopentanone, 2,5-dimethyl-2-cyclopentenone, 2-cyclopenten-1-one, 2-methyl-2-cyclopentenone, 2,3-dimethyl-2-cyclopenten-1-one, 3,4-dimethyl- 2-cyclopenten-1-one, 2,3,4-trimethyl-2-cyclopenten-1-one, butyrolactone, 3-ethyl-2-cyclopenten-1-one, 3-methylcyclohexanone, 3-methylacetophenone, 1- And methylindan-2-one.
本発明の燻製食品の揮発性成分のフェノール類は、芳香族置換基上に１つ以上のヒドロキシ基を有する有機化合物をいい、例えば、フェノール、２−エチルフェノール、３−エチルフェノール、２−メチルフェノール、グアイアコール、２−エチル−５−メチルフェノール、２−メトキシ−３−メチルフェノール、２−メトキシ−５−メチルフェノール、２，３−ジメチルフェノール、２，６−ジメチルフェノール、３，５−ジメチルフェノール、２，６−ジメトキシフェノール等が挙げられる。 The volatile component phenols of the smoked food of the present invention refers to an organic compound having one or more hydroxy groups on an aromatic substituent, for example, phenol, 2-ethylphenol, 3-ethylphenol, 2-methyl. Phenol, guaiacol, 2-ethyl-5-methylphenol, 2-methoxy-3-methylphenol, 2-methoxy-5-methylphenol, 2,3-dimethylphenol, 2,6-dimethylphenol, 3,5-dimethyl Examples include phenol and 2,6-dimethoxyphenol.
本発明の燻製食品の揮発性成分の窒素化合物は、分子内に１つ以上の窒素原子を有する化合物をいい、例えば、ピリジン、３−メトキシピリジン、２−エチル−５−メチルピラジン、２−エチル−６−メチルピラジン、２，５−ジメチルピラジン、２，６−ジメチルピラジン、２，３，５−トリメチルピラジン等が挙げられる。 The volatile component nitrogen compound of the smoked food of the present invention refers to a compound having one or more nitrogen atoms in the molecule, such as pyridine, 3-methoxypyridine, 2-ethyl-5-methylpyrazine, 2-ethyl. -6-methylpyrazine, 2,5-dimethylpyrazine, 2,6-dimethylpyrazine, 2,3,5-trimethylpyrazine and the like can be mentioned.
本発明の燻製食品の揮発性成分のガスクロマトグラムにおける、炭化水素類のピーク面積の総和をＤとするとき、Ａ：Ｄは、好ましくは１５〜３５：５〜１０であり、より好ましくは２０〜３０：６〜９である。当該Ａ：Ｄが、上記の範囲内であることにより、加熱後においても、加熱前の官能品質を維持することができ、かつ燻煙由来の好ましい香りが減弱又は消失しにくい燻製食品を提供できることとなる。 When the sum of the peak areas of hydrocarbons in the gas chromatogram of the volatile component of the smoked food of the present invention is D, A: D is preferably 15 to 35: 5 to 10, more preferably 20 to 30: 6-9. When A: D is within the above range, it is possible to maintain a sensory quality before heating even after heating, and to provide a smoked food in which a preferable scent derived from smoke does not easily attenuate or disappear. It becomes.
本発明の燻製食品の揮発性成分の炭化水素類は、炭素原子及び水素原子のみから構成される有機化合物をいい、例えば、エチルベンゼン、ｍ−キシレン、ｏ−キシレン、１，２，３−トリメチルベンゼン、３，４−ジメトキシトルエン、３，５−ジメトキシトルエン、ナフタレン等が挙げられる。 The volatile hydrocarbons of the smoked food of the present invention refer to organic compounds composed of only carbon atoms and hydrogen atoms, such as ethylbenzene, m-xylene, o-xylene, 1,2,3-trimethylbenzene. 3,4-dimethoxytoluene, 3,5-dimethoxytoluene, naphthalene and the like.
本発明の燻製食品の揮発性成分のガスクロマトグラムにおける全成分のピーク面積の総和に占める前記Ａの割合は、好ましくは１５〜３５％であり、より好ましくは２０〜３０％である。 The proportion of A in the total peak area of all components in the gas chromatogram of the volatile components of the smoked food of the present invention is preferably 15 to 35%, more preferably 20 to 30%.
本発明の燻製食品の揮発性成分のガスクロマトグラムにおける全成分のピーク面積の総和に占める前記Ｂ及びＣの合計（Ｂ＋Ｃ）の割合は、好ましくは４５〜７５％であり、より好ましくは５０〜７０％であり、さらに好ましくは５０．１〜６７．９％であり、特に好ましくは５２．６〜６４．５％である。 The ratio of the total of B and C (B + C) in the total sum of peak areas of all components in the gas chromatogram of the volatile components of the smoked food of the present invention is preferably 45 to 75%, more preferably 50 to 70. %, More preferably 50.1 to 67.9%, and particularly preferably 52.6 to 64.5%.
本発明の燻製食品の揮発性成分のガスクロマトグラムにおける全成分のピーク面積の総和に占める前記Ｂの割合は、好ましくは４２〜５７％であり、より好ましくは４４〜５４％である。 The proportion of B in the total peak area of all components in the gas chromatogram of volatile components of the smoked food of the present invention is preferably 42 to 57%, more preferably 44 to 54%.
本発明の燻製食品の揮発性成分のガスクロマトグラムにおける全成分のピーク面積の総和に占める前記Ｃの割合は、好ましくは８．１〜１０．９％であり、より好ましくは８．６〜１０．５％である。 The ratio of C in the total peak area of all components in the gas chromatogram of the volatile components of the smoked food of the present invention is preferably 8.1 to 10.9%, more preferably 8.6 to 10. 5%.
本発明の燻製食品の揮発性成分のガスクロマトグラムにおける全成分のピーク面積の総和に占める前記Ｄの割合は、好ましくは６．６〜８．９％であり、より好ましくは７〜８．６％である。 The ratio of D in the total peak area of all components in the gas chromatogram of volatile components of the smoked food of the present invention is preferably 6.6 to 8.9%, more preferably 7 to 8.6%. It is.
本発明において、燻製食品の揮発性成分のガスクロマトグラムにおける、ケトン類、フェノール類、窒素化合物、炭化水素類及び全成分の各ピーク面積の総和は、燻製食品の揮発性成分をダイナミックヘッドスペース（ＤＨＳ）法により捕集後、ＧＣ／ＭＳ法（カラム：ＤＢ−ＷＡＸ ６０ｍ×０．２５ｍｍ径、膜厚０．２５μｍ）により得られるトータルイオンクロマトグラム（ＴＩＣ）から測定される値である。測定条件の詳細は、後掲の実施例の通りである。 In the present invention, the sum of the peak areas of ketones, phenols, nitrogen compounds, hydrocarbons, and all components in the gas chromatogram of volatile components of smoked foods is calculated using the dynamic headspace (DHS) ) Method after collection by the GC / MS method (column: DB-WAX 60 m × 0.25 mm diameter, film thickness 0.25 μm) is a value measured from a total ion chromatogram (TIC) obtained. Details of the measurement conditions are as in the examples described later.
本発明の燻製食品の原料（原料食品）は、燻臭が付与されることを所望される食品であれば特に制限されないが、例えば、魚、貝、イカ、エビ等の魚介類；牛肉、豚肉、羊肉等の畜肉；鶏肉、アヒル肉等の家禽肉；チーズ等の乳製品；卵等が挙げられ、好ましくは魚介類であり、より好ましくは魚である。 The raw material (raw raw material) of the smoked food of the present invention is not particularly limited as long as it is a food that is desired to be given a odor. For example, fish and shellfish such as fish, shellfish, squid, and shrimp; beef and pork Livestock meat such as mutton; poultry meat such as chicken and duck meat; dairy products such as cheese; eggs and the like, preferably seafood, more preferably fish.
本発明の燻製食品の種類は特に制限されないが、例えば、鰹節、宗田鰹節、鮪節、鯖節、鰯節、鯵節等の魚節；燻製貝柱、スモークサーモン、燻製牡蠣、燻製いか、燻製かまぼこ等の燻製魚介類；ハム、ソーセージ、ベーコン等の畜肉燻製品；スモークチーズ等の燻製乳製品；燻製卵；燻煙濃縮物である燻液等が挙げられ、好ましくは魚節である。 The type of the smoked food of the present invention is not particularly limited. Smoked fish and shellfishes such as ham, sausage, bacon, etc .; smoked dairy products such as smoked cheese; smoked eggs;
本発明の燻製食品中の３，４−ベンツピレンの濃度は、好ましくは２０ｐｐｂ以下であり、より好ましくは１０ｐｐｂ以下であり、特に好ましくは検出限界以下である。
ここで、燻製食品中の３，４−ベンツピレンの濃度は、食品衛生検査指針ベンゾ（ａ）ピレン試験法によって測定される値である。
The concentration of 3,4-benzpyrene in the smoked food of the present invention is preferably 20 ppb or less, more preferably 10 ppb or less, and particularly preferably the detection limit or less.
Here, the density | concentration of 3, 4- benzpyrene in smoked food is a value measured by the food hygiene inspection guideline benzo (a) pyrene test method.
本発明の燻製食品は、（ａ）植物原料を炭化槽内で熱分解して燻煙を発生させることと、（ｂ）当該燻煙を加熱することと、（ｃ）加熱後の燻煙又はその有効成分を原料食品に接触又は付着させることとを含む製造方法により製造することができる。以下、当該製造方法について説明する。 The smoked food of the present invention includes (a) pyrolyzing a plant raw material in a carbonization tank to generate smoke, (b) heating the smoke, and (c) smoke after heating or The active ingredient can be produced by a production method including contacting or adhering the active ingredient to the raw material food. Hereinafter, the manufacturing method will be described.
［（ａ）植物原料の熱分解］
植物原料は、異臭を発しないものであれば特に制限されないが、例えば、木材、竹材、果実、草花、藁、椰子殻、籾殻等が挙げられ、好ましくは木材である。植物原料として用いる木材の種類は、原料食品の種類等に応じて適宜選択すればよいが、例えば、原料食品が魚である場合、ナラ、ブナ、クヌギ、サクラ等が挙げられる。植物原料の形態は特に制限されないが、例えば、薪、チップ、おが粉、スモークウッド等が挙げられ、表面積が大きく、効率良く熱分解を行い得ることから、チップ又はおが粉が好ましい。
[(A) Thermal decomposition of plant material]
The plant raw material is not particularly limited as long as it does not give off a strange odor, and examples thereof include wood, bamboo, fruit, flower, cocoon, coconut shell, rice husk and the like, preferably wood. The type of wood used as the plant raw material may be appropriately selected according to the type of the raw material food. For example, when the raw material food is fish, oak, beech, kunugi, cherry and the like can be mentioned. The form of the plant raw material is not particularly limited, and examples thereof include straw, chips, sawdust, smoked wood and the like. Chips or sawdust are preferred because they have a large surface area and can be efficiently thermally decomposed.
植物原料の使用量は、原料食品１重量部に対して、好ましくは０．１５〜０．３重量部であり、より好ましくは０．２〜０．２８重量部である。 The amount of the plant raw material used is preferably 0.15 to 0.3 part by weight, more preferably 0.2 to 0.28 part by weight with respect to 1 part by weight of the raw material food.
炭化槽は、その内部において植物原料の熱分解を行うことができれば、その大きさ及び形状等は特に制限されない。炭化槽は、高温、高圧に耐性の容器であることが好ましく、例えば、ガラス、耐熱性の樹脂、磁器、金属等の容器が好ましい。熱分解を開始する前の炭化槽内の雰囲気は、空気であることが工業上は好ましいが、他の気体（例、窒素、又はそれらの混合物等）が空気に導入されていてもよい。 The size and shape of the carbonization tank are not particularly limited as long as the plant raw material can be pyrolyzed inside. The carbonization tank is preferably a container that is resistant to high temperatures and high pressures. For example, glass, heat-resistant resin, porcelain, metal, and the like are preferable. Although it is industrially preferable that the atmosphere in the carbonization tank before starting thermal decomposition is air, other gas (for example, nitrogen, or a mixture thereof) may be introduced into the air.
熱分解の開始前の炭化槽内の二酸化炭素濃度は、好ましくは１％以下であり、より好ましくは０．１％以下である。炭化槽内の二酸化炭素濃度は、通常、熱分解の開始直後から上昇して最高濃度（通常、６８〜７５％）に達し、その後は熱分解が進むにつれて徐々に低下する（例えば、図６に示されるように推移する）。 The carbon dioxide concentration in the carbonization tank before the start of thermal decomposition is preferably 1% or less, more preferably 0.1% or less. The carbon dioxide concentration in the carbonization tank usually increases immediately after the start of thermal decomposition, reaches a maximum concentration (usually 68 to 75%), and then gradually decreases as the thermal decomposition proceeds (for example, in FIG. 6). As indicated)).
熱分解の開始前の炭化槽内の一酸化炭素濃度は、好ましくは１％以下であり、より好ましくは０．１％以下である。炭化槽内の一酸化炭素濃度は、通常、熱分解の開始直後から上昇して最高濃度（通常、２０〜２７％）に達し、その後は熱分解が進んでも殆ど低下せず、一定の濃度が維持される（例えば、図６に示されるように推移する）。 The carbon monoxide concentration in the carbonization tank before the start of thermal decomposition is preferably 1% or less, more preferably 0.1% or less. The carbon monoxide concentration in the carbonization tank usually increases immediately after the start of pyrolysis and reaches the maximum concentration (usually 20 to 27%). Maintained (eg, transition as shown in FIG. 6).
熱分解の開始前の炭化槽内の酸素濃度は、好ましくは１〜２１％であり、より好ましくは１〜１８％である。 The oxygen concentration in the carbonization tank before the start of thermal decomposition is preferably 1 to 21%, more preferably 1 to 18%.
本発明において、炭化槽内の二酸化炭素濃度、一酸化炭素濃度及び酸素濃度は、いずれも株式会社リエロ・ジャパン製の排ガス分析計「ＡＵＴＯ４．１」によって測定される値である。 In the present invention, the carbon dioxide concentration, carbon monoxide concentration, and oxygen concentration in the carbonization tank are values measured by an exhaust gas analyzer “AUTO 4.1” manufactured by Liero Japan Co., Ltd.
熱分解の方法は、植物原料から燻煙を発生させることができれば特に制限されないが、例えば、炭化槽を固体熱媒体（例、電熱コイル、電気ヒーター等）、バーナーの炎等で加熱することにより植物原料を加熱する方法、炭化槽内に設置した固体熱媒体（例、電熱コイル、電気ヒーター等）により植物原料を加熱する方法、炭化槽内に高温の気体（例、高温ガス、過熱水蒸気等）を導入して植物原料を加熱する方法等が挙げられ、温度制御が容易であることから、炭化槽を加熱することにより植物原料を加熱する方法が好ましい。固体熱媒体による炭化槽又は植物原料の加熱は、固体熱媒体と炭化槽又は植物原料とを接触させることにより行うものであっても、固体熱媒体の放射熱により行うものであってもよい。 The pyrolysis method is not particularly limited as long as smoke can be generated from plant raw materials. For example, the carbonization tank is heated by a solid heat medium (eg, an electric heating coil, an electric heater, etc.), a flame of a burner, or the like. A method of heating plant materials, a method of heating plant materials with a solid heat medium (eg, electric heating coil, electric heater, etc.) installed in the carbonization tank, a high-temperature gas (eg, high-temperature gas, superheated steam, etc.) in the carbonization tank ) Is introduced and the plant material is heated, and the temperature control is easy. Therefore, the method of heating the plant material by heating the carbonization tank is preferable. The heating of the carbonization tank or the plant material with the solid heat medium may be performed by bringing the solid heat medium into contact with the carbonization tank or the plant material, or may be performed by radiant heat of the solid heat medium.
熱分解温度は、好ましく６００℃以下であり、ベンツピレン等の有害成分の生成を完全に抑制するため、より好ましくは４２５℃以下である。当該温度が６００℃を超えると、ベンツピレン等の有害成分の生成が増加する傾向がある。熱分解温度の下限は、植物原料から燻煙を発生させ得れば特に制限されないが、十分な量の燻煙を発生させるため、熱分解温度は、好ましくは２４０℃以上である。 The thermal decomposition temperature is preferably 600 ° C. or lower, and more preferably 425 ° C. or lower in order to completely suppress the generation of harmful components such as benzpyrene. When the temperature exceeds 600 ° C., generation of harmful components such as benzpyrene tends to increase. The lower limit of the thermal decomposition temperature is not particularly limited as long as smoke can be generated from plant raw materials, but in order to generate a sufficient amount of smoke, the thermal decomposition temperature is preferably 240 ° C. or higher.
植物原料の熱分解は、炭化槽内の二酸化炭素濃度が特定の濃度に低下するまで行うこと（即ち、炭化槽内の二酸化炭素濃度が特定の濃度に低下するまでは、植物原料の熱分解を止めないこと）が好ましい。植物原料の熱分解を、炭化槽内の二酸化炭素濃度が特定の濃度に低下するまで行うことで、植物原料の熱分解の程度を把握し、好ましい香りの質を維持しつつ、加熱されても香りが減弱又は消失しにくい燻煙を得ることができる。
具体的には、植物原料の熱分解は、炭化槽内の二酸化炭素濃度が３５〜５８％に低下するまで行うことが好ましく、３７〜５６％に低下するまで行うことがより好ましい。
尚、言うまでもないが「炭化槽内の二酸化炭素濃度がＸ％に低下する」とは、炭化槽内の二酸化炭素濃度がＸ％を超える濃度からＸ％になることを意味し、Ｘ％未満の濃度からＸ％になることではない。
The thermal decomposition of the plant raw material is performed until the carbon dioxide concentration in the carbonization tank is lowered to a specific concentration (that is, the pyrolysis of the plant raw material is performed until the carbon dioxide concentration in the carbonization tank is reduced to a specific concentration. It is preferable not to stop. By performing pyrolysis of plant raw material until the carbon dioxide concentration in the carbonization tank decreases to a specific concentration, it is possible to grasp the degree of thermal decomposition of the plant raw material and maintain a desirable scent quality while being heated. It is possible to obtain smoke that does not easily attenuate or disappear.
Specifically, the thermal decomposition of the plant raw material is preferably performed until the carbon dioxide concentration in the carbonization tank is reduced to 35 to 58%, and more preferably is decreased to 37 to 56%.
Needless to say, “the carbon dioxide concentration in the carbonization tank is reduced to X%” means that the carbon dioxide concentration in the carbonization tank is changed from a concentration exceeding X% to X%, and less than X%. It is not X% from the concentration.
［（ｂ）燻煙の加熱（２次加熱）］
植物原料より発生した燻煙を加熱すること（２次加熱）により、燻煙の香りを改質し得る。燻煙を加熱する方法としては、例えば、固体熱媒体（例、熱交換機、電気ヒーター等）により加熱する方法、酸素を含まない高温の気体（例、高温不活性ガス、過熱水蒸気等）により加熱する方法、バーナー等の炎により加熱する方法、燻煙に少量の酸素を導入して、燻煙を燃焼させ、その燃焼熱により加熱する方法等が挙げられるが、温度制御が容易であることや燻煙の濃度を薄めることがないことから、固体熱媒体により加熱する方法が好ましい。固体熱媒体による燻煙の加熱は、固体熱媒体と燻煙とを接触させることにより行うものであっても、又は固体熱媒体の放射熱により行うものであってもよいが、より精度高く燻煙の温度制御が可能で設備保全がしやすいという観点から、固体熱媒体と燻煙とを接触させることにより行うことが好ましい。
[(B) Smoke heating (secondary heating)]
By heating the smoke generated from the plant material (secondary heating), the scent of the smoke can be modified. Examples of methods for heating soot include heating by a solid heat medium (eg, heat exchanger, electric heater, etc.), heating by a high-temperature gas not containing oxygen (eg, high-temperature inert gas, superheated steam, etc.) A method of heating with a flame such as a burner, a method of introducing a small amount of oxygen into the soot, burning the soot, and heating with the heat of combustion, etc. A method of heating with a solid heat medium is preferable because the concentration of soot is not reduced. The heating of the smoke by the solid heat medium may be performed by bringing the solid heat medium and the smoke into contact with each other or by the radiant heat of the solid heat medium. From the viewpoint that the temperature of the smoke can be controlled and the maintenance of the equipment is easy, it is preferable to carry out by bringing the solid heat medium into contact with the smoke.
燻煙の加熱温度は、３００℃以上８００℃未満に保持すること（即ち、３００℃以上８００℃未満の範囲外としないこと）が好ましい。３００℃以上で燻煙を加熱することにより、燻煙の香りが改質され、温度の上昇とともに、甘い香りから刺激的な香りに変化し、またタール臭や木の異風味等の好ましくない香りが低減する。一方、加熱温度が８００℃を超えると、燻煙中の低沸点炭化水素等が無臭成分にまで分解され、燻煙の香りは改質されるものの、香り全体の強さとしては弱くなる傾向がある。燻煙の加熱温度は、４００〜７００℃に保持することがより好ましく、４００〜６００℃に保持することが特に好ましい。 The heating temperature of the soot is preferably kept at 300 ° C. or higher and lower than 800 ° C. (that is, not outside the range of 300 ° C. or higher and lower than 800 ° C.). By heating the smoke at 300 ° C or higher, the smoke scent is modified, and as the temperature rises, it changes from a sweet scent to an irritating scent. Is reduced. On the other hand, when the heating temperature exceeds 800 ° C., low-boiling hydrocarbons and the like in the smoke are decomposed to odorless components and the odor of smoke is improved, but the overall strength of the fragrance tends to be weakened. is there. As for the heating temperature of soot, it is more preferable to hold | maintain at 400-700 degreeC, and it is especially preferable to hold | maintain at 400-600 degreeC.
燻煙の加熱温度は、炭化槽内の二酸化炭素濃度に対する一酸化炭素濃度の比（ＣＯ／ＣＯ２）が０．４を超えた後は、二酸化炭素濃度の低下に応じて下げることが好ましい。そのように燻煙の加熱温度を下げることで、発生した煙成分を過度に分解することなく、好ましい香りの質を維持しつつ、加熱されても香りが減弱又は消失しにくい燻煙を得ることができる。
具体的には、燻煙の加熱温度は、二酸化炭素濃度１％低下当たり５〜３５℃下げることが好ましく、１０〜２５℃下げることがより好ましい。
本発明において、燻煙の加熱温度を「二酸化炭素濃度１％低下当たりＸ℃下げる」とは、燻煙の加熱温度を、炭化槽内の二酸化炭素濃度が１％低下する間に、Ｘ℃下げることを意味する。炭化槽内の二酸化炭素濃度は最高濃度に到達した後は徐々に低下するが、燻煙の加熱温度は、それに合わせて徐々に（即ち、連続的に）下げてもよく、又は炭化槽内の二酸化炭素濃度が１％低下する毎に段階的に下げてもよい。
燻煙の加熱温度は、炭化槽内の二酸化炭素濃度に対する一酸化炭素濃度の比（ＣＯ／ＣＯ２）が０．４を超えたと同時に下げ始めなくてもよいが、当該比が０．５になるまでには下げ始めることが好ましい。
燻煙の加熱温度は、最終的に３００℃以上になるように下げることが好ましく、４００℃以上になるように下げることがより好ましい。
The heating temperature of the soot is preferably lowered according to the decrease in the carbon dioxide concentration after the ratio of the carbon monoxide concentration to the carbon dioxide concentration in the carbonization tank (CO / CO 2 ) exceeds 0.4. Thus, by reducing the heating temperature of the soot, it is possible to obtain a soot that does not weaken or disappear even when heated, while maintaining a desirable scent quality without excessively decomposing the generated smoke component Can do.
Specifically, the heating temperature of soot is preferably lowered by 5 to 35 ° C., more preferably 10 to 25 ° C. per 1% decrease in carbon dioxide concentration.
In the present invention, the soot heating temperature is “XC reduced per 1% decrease in carbon dioxide concentration” means that the soot heating temperature is decreased by X ° C while the carbon dioxide concentration in the carbonization tank is decreased by 1%. Means that. Although the carbon dioxide concentration in the carbonization tank gradually decreases after reaching the maximum concentration, the heating temperature of the soot may be gradually decreased (that is, continuously) or in the carbonization tank. Each time the carbon dioxide concentration decreases by 1%, it may be lowered stepwise.
The heating temperature of the smoke does not have to start decreasing at the same time as the ratio of the carbon monoxide concentration to the carbon dioxide concentration in the carbonization tank (CO / CO 2 ) exceeds 0.4, but the ratio becomes 0.5. It is preferable to start lowering until it becomes.
The heating temperature of the soot is preferably lowered so as to be finally 300 ° C. or higher, and more preferably lowered to be 400 ° C. or higher.
燻煙を加熱するとき、追加の気体を供給してもよい。追加の気体を供給することにより、燻煙の香りを、単に加熱するだけでは得られない質に改質できるようになる。追加の気体としては、例えば、酸素、空気等の酸素供給源となる気体；水素、水蒸気等の水素供給源となる気体；メタノール、エタノール、プロパン、ブタン、エチレン、アセチレン等の炭化水素供給源となる気体；窒素、アルゴン等が挙げられる。 Additional gas may be supplied when heating the soot. By supplying additional gas, the scent of smoke can be modified to a quality that cannot be obtained simply by heating. Examples of the additional gas include: a gas serving as an oxygen supply source such as oxygen and air; a gas serving as a hydrogen supply source such as hydrogen and water vapor; and a hydrocarbon source such as methanol, ethanol, propane, butane, ethylene, and acetylene And a gas such as nitrogen and argon.
燻煙を加熱するとき、紫外線等の波長の短い光線を燻煙に照射してもよい。また、燻煙を加熱するとき、反応助剤（例、ラジカル等）、触媒（例、白金等）を燻煙に添加してもよい。これらによっても、燻煙の香りの質を変えることができる。 When heating the smoke, the smoke may be irradiated with light having a short wavelength such as ultraviolet rays. In addition, when heating the soot, a reaction aid (eg, radical) or a catalyst (eg, platinum) may be added to the soot. These also change the quality of the scent of smoke.
加熱後の燻煙は、原料食品に接触等させる前に冷却してよい。燻煙を冷却する方法としては、例えば、燻煙加熱装置と燻製室の間に煙滞留管や熱交換機を設置することによって燻煙の冷却温度を調整する方法等が挙げられる。 The smoke after heating may be cooled before contacting the raw material food. As a method for cooling the soot, for example, a method for adjusting the cooling temperature of the soot by installing a smoke retention pipe or a heat exchanger between the soot heating device and the smoke producing chamber can be mentioned.
冷却後の燻煙の温度は、好ましくは５０〜２５０℃であり、より好ましくは８０〜２００℃であり、さらに好ましくは１００〜２００℃である。 The temperature of the smoke after cooling is preferably 50 to 250 ° C, more preferably 80 to 200 ° C, and further preferably 100 to 200 ° C.
［（ｃ）燻付け］
加熱後の燻煙又はその有効成分を原料食品に接触又は付着させること（燻付け）により、原料食品に燻煙由来の好ましい風味が付与される。
[(C) Brazing]
By contacting or adhering the smoked smoke after heating or its active ingredient to the raw material food (glazing), a preferred flavor derived from the smoke is imparted to the raw material food.
本発明の一実施態様として、原料食品が魚である場合、該魚は煮熟されていることが好ましく、さらに該魚は、煮熟後に乾燥されていることがより好ましい。魚を煮熟する方法は特に制限されず、自体公知の方法で行えばよい。また煮熟された魚の乾燥方法も特に制限されないが、例えば、熱風で魚を加熱することにより乾燥させる方法（熱風乾燥）、遠赤外線を魚に放射することにより乾燥させる方法（遠赤外線乾燥）及び高周波を魚に照射することにより乾燥させる方法（高周波乾燥）等が挙げられ、多量の魚を均一に乾燥でき、また簡便であることから、熱風乾燥が好ましい。これらの乾燥方法は、適宜組み合わせてもよい。 As one embodiment of the present invention, when the raw food is fish, the fish is preferably boiled, and more preferably, the fish is dried after ripening. The method for boiling and ripening the fish is not particularly limited, and may be performed by a method known per se. The method for drying the boiled fish is not particularly limited. For example, a method of drying the fish by heating with hot air (hot air drying), a method of drying by radiating far infrared rays to the fish (far infrared drying) and A method of drying by irradiating fish with high frequency (high frequency drying) and the like can be mentioned, and a large amount of fish can be uniformly dried, and since it is simple, hot air drying is preferable. These drying methods may be appropriately combined.
熱風乾燥の熱源は、煮熟された魚に異風味、有害成分を付与するものでなければ特に制限されないが、温度制御が容易であることから、ＬＰＧ（液化石油ガス）及びＬＮＧ（液化天然ガス）等のガスを燃焼させ、その際に発生する熱風で乾燥することが好ましい。熱風乾燥の方式は特にされないが、煮熟された魚に並行に熱風を送る方式（並行流）が好ましい。並行流で乾燥する場合、送風方向は常に一定であってもよいが、均一な乾燥のために、適当な時間間隔で切り替えること（交互流）が好ましい。熱風とする気体は、乾燥空気を用いればよいが、魚肉中の脂質の酸化を防止するために、煙を導入してもよい。あるいは、酸素濃度の低い燃焼空気を利用してもよいし、窒素置換等により酸素濃度を低くしてもよい。 The heat source for hot air drying is not particularly limited as long as it does not impart a different flavor or harmful components to the boiled fish, but since temperature control is easy, LPG (liquefied petroleum gas) and LNG (liquefied natural gas) It is preferable to burn the gas such as) and dry with hot air generated at that time. The method of hot air drying is not particularly limited, but a method of sending hot air in parallel to boiled fish (parallel flow) is preferable. When drying in parallel flow, the air blowing direction may be always constant, but switching at an appropriate time interval (alternate flow) is preferable for uniform drying. As the gas used as hot air, dry air may be used, but smoke may be introduced in order to prevent oxidation of lipids in fish meat. Alternatively, combustion air having a low oxygen concentration may be used, or the oxygen concentration may be lowered by nitrogen replacement or the like.
熱風の温度は、短時間で乾燥させるためにできるだけ高温であることが好ましいが、高温で乾燥させ続けると、煮熟された魚の表面が過度に乾燥し、好ましくない焦げ臭が発生する場合があるため、熱風温度は高温から経時的に下げることが好ましい。熱風温度は、連続的に下げてもよく、又は適当な時間間隔で段階的に下げてもよい。
具体的な熱風の温度は、乾燥開始時は、好ましくは１２０℃以上であり、より好ましくは１４０℃以上であり、さらに好ましくは１６０℃以上である。乾燥開始時の温度が１２０℃未満であると、乾燥に長時間を要するようになり、また乾燥後の魚に生臭さが残ることがある。一方、乾燥開始時の温度は２００℃以上であってもよいが、焦げ臭が発生しやすく、速やかに温度を下げる必要があるため、２００℃未満であることが好ましい。乾燥終了時の温度は、好ましくは１２０℃未満であり、より好ましくは１１０℃以下であり、さらに好ましくは１００℃以下である。乾燥終了時の温度の下限は特に制限されないが、通常８０℃である。
The temperature of the hot air is preferably as high as possible for drying in a short time, but if the drying is continued at a high temperature, the surface of the boiled fish may be excessively dried, and an undesired burnt odor may be generated. Therefore, the hot air temperature is preferably lowered over time from a high temperature. The hot air temperature may be continuously decreased, or may be gradually decreased at an appropriate time interval.
The specific temperature of the hot air is preferably 120 ° C. or higher, more preferably 140 ° C. or higher, and further preferably 160 ° C. or higher at the start of drying. When the temperature at the start of drying is less than 120 ° C., it takes a long time to dry, and a fresh odor may remain in the fish after drying. On the other hand, the temperature at the start of drying may be 200 ° C. or higher, but it is preferably less than 200 ° C. because a burning odor is likely to occur and the temperature needs to be quickly lowered. The temperature at the end of drying is preferably less than 120 ° C, more preferably 110 ° C or less, and even more preferably 100 ° C or less. The lower limit of the temperature at the end of drying is not particularly limited, but is usually 80 ° C.
煮熟された魚は、腐敗及び微生物の増殖を防止する観点から、その水分含量が３０重量％以下となるように乾燥することが好ましく、１６重量％以下となるように乾燥することがより好ましい。当該水分含量の下限は特に制限されないが、通常５重量％であり、好ましくは１０重量％である。
本発明において、魚の水分含量は、常圧乾燥法（１０５℃、４時間）により測定される値である。
The boiled fish is preferably dried so that its water content is 30% by weight or less, more preferably 16% by weight or less, from the viewpoint of preventing spoilage and microbial growth. . The lower limit of the water content is not particularly limited, but is usually 5% by weight, preferably 10% by weight.
In the present invention, the water content of fish is a value measured by an atmospheric drying method (105 ° C., 4 hours).
煮熟された魚は、そのままの形状で乾燥してよいが、乾燥する前に所定の形状に切断してもよい。あるいは、煮熟された魚をそのままの形状で乾燥した後に、所定の形状に切断してもよい。煮熟された魚の切断後の形状及び大きさは、特に制限されないが、例えば、煮熟された魚を乾燥前に切断する場合は、長辺（最も長い部分）が２０〜２００ｍｍで、厚み（最も短い部分）が５〜２０ｍｍであるフレーク状が好ましく、長辺２０〜１００ｍｍで、厚みが５〜１５ｍｍであるフレーク状がより好ましい。このようなフレーク状に切断することによって、その後の乾燥を短時間で効率よく行うことができる。また、この場合の切断物には、長辺が２０ｍｍ以下、又は厚みが５ｍｍ以下のものが含まれていてもよいが、その重量割合は、切断物全量に対して、好ましくは２０％以下である。 The boiled fish may be dried as it is, but may be cut into a predetermined shape before drying. Alternatively, the boiled fish may be dried as it is and then cut into a predetermined shape. The shape and size of the boiled fish after cutting are not particularly limited. For example, when cutting the boiled fish before drying, the long side (longest part) is 20 to 200 mm in thickness ( A flake shape having a shortest portion of 5 to 20 mm is preferable, and a flake shape having a long side of 20 to 100 mm and a thickness of 5 to 15 mm is more preferable. By cutting into such flakes, subsequent drying can be performed efficiently in a short time. Further, the cut product in this case may include those having a long side of 20 mm or less or a thickness of 5 mm or less, and the weight ratio thereof is preferably 20% or less with respect to the total amount of the cut product. is there.
加熱後の燻煙又はその有効成分を、原料食品に接触又は付着させる方法は特に制限されず、自体公知の方法で行えばよい。当該方法としては、例えば、原料食品を加熱後の燻煙雰囲気下に存在させる方法、加熱後の燻煙の有効成分を水に溶解し、得られた溶液（燻液）に原料食品を浸漬するか、又は燻液を原料食品に吹き付けた後、乾燥させる方法（液燻法）、燻煙室内に高電圧の電流を流して電場を作ることにより、原料食品への加熱後の燻煙の有効成分の付着を促進する方法（電燻法）等が挙げられる。中でも、原料食品への加熱後の燻煙又はその有効成分の接触又は付着は、設備の整備、維持、および品質管理方法の簡便さの観点から、原料食品を加熱後の燻煙雰囲気下に存在させることにより行うことが好ましい。 The method for bringing the soot after heating or its active ingredient into contact with or adhering to the raw food is not particularly limited, and may be carried out by a method known per se. As the method, for example, a method in which the raw food is present in a smoke atmosphere after heating, an active ingredient of the smoke after heating is dissolved in water, and the raw food is immersed in the obtained solution (salt liquid) Or after spraying smoked liquid on the raw food, drying method (liquid smoke method), by applying a high voltage current in the smoke chamber and creating an electric field, the effectiveness of smoke after heating to the raw food Examples thereof include a method for promoting adhesion of components (electroplating method). Above all, the contact or adhesion of soot or its active ingredients after heating to the raw food is present in the soot atmosphere after heating the raw food from the viewpoint of facility maintenance, maintenance, and the quality control method. It is preferable to carry out.
原料食品への加熱後の燻煙又はその有効成分の接触又は付着を、原料食品を加熱後の燻煙雰囲気下に存在させることにより行う場合、燻煙雰囲気の温度は特に制限されず、例えば１６〜２０℃（冷燻法）、２５〜４５℃（温燻法）及び５０〜９０℃（熱燻法）等のいずれであってもよいが、燻煙雰囲気は低温であることが好ましく、具体的には５０〜８０℃が好ましい。燻煙雰囲気を低温にする場合は、原料食品は予め乾燥していることが好ましい。また燻煙雰囲気の温度は変動させてもよく、例えば、１００℃程度から開始して最終的に５０〜８０℃に低下させてもよい。 When the contact or adhesion of the soot after heating to the raw material food or its active ingredient is performed by making the raw material food exist in the soot atmosphere after heating, the temperature of the soot atmosphere is not particularly limited, for example, 16 Although it may be any of -20 ° C. (cooling method), 25-45 ° C. (hot-bath method), 50-90 ° C. (hot-bath method), etc., the smoke atmosphere is preferably a low temperature. Specifically, 50-80 degreeC is preferable. When making the smoke atmosphere low, it is preferable that the raw food is dried in advance. Further, the temperature of the smoke atmosphere may be varied, for example, starting from about 100 ° C. and finally decreasing to 50-80 ° C.
原料食品への加熱後の燻煙又はその有効成分の接触又は付着を、原料食品を加熱後の燻煙雰囲気下に存在させることにより行う場合、燻煙雰囲気の風速は、燻煙雰囲気が均一な温度になりさえすれば特に制限されないが、燻煙雰囲気の風速が大きいほど、短時間で燻煙雰囲気が均一な温度になることから、燻煙雰囲気の風速は、好ましくは０．５ｍ／秒以上であり、より好ましくは１．８ｍ／秒以上である。燻煙雰囲気の風速の上限は、通常２ｍ／秒である。
ここで、燻煙雰囲気の風速は、「ＫＡＮＯＭＡＸ ＡＮＥＭＯＭＡＳＴＥＲ モデル６１１４」（日本カノマックス株式会社製）等の風速計を用いることにより測定可能である。
When contact or adhesion of soot or its active ingredients after heating to the raw food is carried out by allowing the raw food to exist in a soot atmosphere after heating, the soot atmosphere has a uniform wind speed. The temperature of the smoke atmosphere is not particularly limited as long as the temperature is reached, but the higher the wind speed of the smoke atmosphere, the more uniform the temperature of the smoke atmosphere in a short time. Therefore, the wind speed of the smoke atmosphere is preferably 0.5 m / second or more. More preferably, it is 1.8 m / sec or more. The upper limit of the wind speed in the soot atmosphere is usually 2 m / sec.
Here, the wind speed in the soot atmosphere can be measured by using an anemometer such as “KANOMAX AEMOMASTER model 6114” (manufactured by Nippon Kanomax Co., Ltd.).
原料食品への加熱後の燻煙又はその有効成分の接触又は付着を、原料食品を加熱後の燻煙雰囲気下に存在させることにより行う場合、原料食品を加熱後の燻煙雰囲気下に存在させる時間は、通常２〜１０時間であり、好ましくは３〜７時間である。 When the raw food is brought into contact with or adhered to the smoked food or its active ingredients by allowing the raw food to be present in the smoked atmosphere after heating, the raw food is present in the smoked atmosphere after heating. The time is usually 2 to 10 hours, preferably 3 to 7 hours.
加熱後の燻煙の有効成分は、燻煙の香りを付与し得る成分であり、その具体例としてはグワヤコール、４−メチルグワヤコール、２，６−ジメトキシフェノール等のフェノール類；２，３−ペンタジオン、シクロペンタノン、２-メチルシクロペンタノン等のケトン類；ピリジン、３−メトキシピリジン、２−エチル−５−メチルピラジン等の含窒素化合物類；エチルベンゼン、ｍ−キシレン、１，２，３−トリメチルベンゼン等の炭化水素類等が挙げられる。 The active component of the smoke after heating is a component capable of imparting a scent of smoke, and specific examples thereof include phenols such as guaiacol, 4-methyl guaiacol, 2,6-dimethoxyphenol; -Ketones such as pentadione, cyclopentanone, 2-methylcyclopentanone; nitrogen-containing compounds such as pyridine, 3-methoxypyridine, 2-ethyl-5-methylpyrazine; ethylbenzene, m-xylene, 1, 2, Examples thereof include hydrocarbons such as 3-trimethylbenzene.
本発明の燻製食品を製造するための装置は、少なくとも、植物原料を熱分解して燻煙を発生させる機構（燻煙発生部）と、当該燻煙を加熱する機構（２次加熱部）と、加熱後の燻煙又はその有効成分を原料食品に接触又は付着させる機構（燻製部）とを備えていることが好ましい。当該装置は、加熱後の燻煙を冷却する機構（冷却部）を更に備えていてよい。２次加熱部は、燻煙の加熱温度及び／又は滞留時間を調整する機構、追加の気体を供給する機構を備えていることが好ましい。燻製部は、原料食品を乾燥（例、熱風乾燥等）する機構も兼ね備えた乾燥燻製部であることが、省力化の観点から好ましい。
本発明の燻製食品を製造するための装置としては、例えば、国際公開第２００７／１４２０８６号に記載の装置等が挙げられる。
The apparatus for producing the smoked food of the present invention includes at least a mechanism for pyrolyzing the plant raw material to generate smoke (a smoke generating part), and a mechanism for heating the smoke (secondary heating part). It is preferable to include a mechanism (smoked portion) for contacting or adhering the smoked smoke after heating or its active ingredient to the raw food. The said apparatus may further be equipped with the mechanism (cooling part) which cools the smoke after heating. The secondary heating unit preferably includes a mechanism for adjusting the heating temperature and / or residence time of the soot and a mechanism for supplying additional gas. It is preferable from the viewpoint of labor saving that the smoked portion is a dried smoked portion that also has a mechanism for drying the raw material food (eg, hot air drying).
Examples of the apparatus for producing the smoked food of the present invention include the apparatus described in International Publication No. 2007/142086.
図１は、本発明の燻製食品を製造するための典型的な装置例を示した図（正面断面図）である。以下において、当該図を参照しながら本発明を説明するが、本発明の燻製食品を製造するための装置はこれに限定されず、他の装置（例えば、図２に示される装置等）を用いて実施してもよい。 FIG. 1 is a diagram (front sectional view) showing a typical apparatus for producing the smoked food of the present invention. Hereinafter, the present invention will be described with reference to the drawings. However, the apparatus for producing the smoked food of the present invention is not limited to this, and other apparatuses (for example, the apparatus shown in FIG. 2) are used. May be implemented.
図１に示される装置は、燻煙発生部３２と、燻煙を加熱する熱交換器２からなる２次加熱部と、燻煙を冷却する熱交換器３からなる冷却部と、乾燥燻製部４とから構成されている。 The apparatus shown in FIG. 1 includes a soot generation unit 32, a secondary heating unit composed of a heat exchanger 2 that heats soot, a cooling unit composed of a heat exchanger 3 that cools soot, and a dry smoke producing unit. 4.
（燻煙発生部）
燻煙発生部３２は、バーナーＢ１、炭化槽４８、温度センサーＴ１を備えている。温度センサーＴ１は、炭化槽４８の底面と接し、その中心部の温度を測定することができ、炭化槽内の植物原料が所定の温度になるよう、炭化槽４８をバーナーＢ１で加熱し得る。
(Smoke generating part)
The soot generation unit 32 includes a burner B1, a carbonization tank 48, and a temperature sensor T1. The temperature sensor T1 is in contact with the bottom surface of the carbonization tank 48, can measure the temperature at the center thereof, and can heat the carbonization tank 48 with the burner B1 so that the plant raw material in the carbonization tank has a predetermined temperature.
（２次加熱部）
熱交換器２は、任意の位置（例えば、熱交換器出口部等）に温度センサーＴ２を備え、これにより燻煙の温度を検出し得る。熱交換器２は、温度センサーＴ２と電気ヒーター３３とにより、燻煙を所定の温度で加熱するように調整し得る。例えば、温度センサーＴ２が燻煙の温度を検出して信号を発し、当該信号に基づき、温度指示制御器（図示せず）が、電気ヒーター３３の出力を調節し得る。
熱交換器２は、滞留管の長さ、径を変えることで、燻煙の流速、２次加熱部における燻煙の滞留時間を調整することができる。２次加熱部における燻煙の滞留時間は特に制限されないが、通常０．０２〜３０秒間であり、過加熱による、燻煙成分の過剰な熱分解を抑制できるという観点から、好ましくは、０．１〜３秒間である。
追加のガスを供給する場合、２次加熱部（熱交換器２）の任意の位置に当該ガスの供給口を設け、これを介して追加のガスの供給用ガスボンベ等を装着し得る。
(Secondary heating part)
The heat exchanger 2 is provided with a temperature sensor T2 at an arbitrary position (for example, a heat exchanger outlet), thereby detecting the temperature of the smoke. The heat exchanger 2 can be adjusted by the temperature sensor T2 and the electric heater 33 so as to heat the smoke at a predetermined temperature. For example, the temperature sensor T <b> 2 detects the smoke temperature and generates a signal, and based on the signal, a temperature indication controller (not shown) can adjust the output of the electric heater 33.
The heat exchanger 2 can adjust the flow rate of smoke and the residence time of smoke in the secondary heating section by changing the length and diameter of the residence tube. The residence time of the soot in the secondary heating section is not particularly limited, but is usually 0.02 to 30 seconds, and preferably from the viewpoint that excessive thermal decomposition of the soot component due to overheating can be suppressed. 1 to 3 seconds.
When supplying an additional gas, a supply port for the gas can be provided at an arbitrary position of the secondary heating unit (heat exchanger 2), and a gas cylinder for supplying an additional gas or the like can be mounted via the gas supply port.
（冷却部）
熱交換器３は、任意の位置（例えば、熱交換器出口部等）に温度センサーＴ３を備え、これにより燻煙の温度を検出し得、燻煙を所定の温度で冷却するように調整し得る。
熱交換器３は、滞留管の長さ、径を変えることで、燻煙の流速、冷却部における燻煙の滞留時間を調整することができる。冷却部における燻煙の滞留時間は特に制限されないが、通常０．０２〜３０秒間であり、燻煙成分中のタール分の析出防止の観点から、好ましくは、０．１〜３秒間である。
熱交換器３は、ダンパーＤＰ４を備え、これを調整することにより、燻煙発生部３２から燻煙を引き込む圧力を調整し得る 。
本発明の燻製食品を製造するための装置は、少なくとも燻煙発生部と、２次加熱部と、燻製部とを備えていることが好ましいが、冷却部は必ずしも備えていなくてもよい。冷却部を備えていない装置（例えば、図２に示される装置等）により、本発明の燻製食品を製造する場合、２次加熱部において加熱された燻煙は、例えば、乾燥燻製部４までの配管を通る間に自然に温度を低下させること等により冷却し得る。
(Cooling section)
The heat exchanger 3 is provided with a temperature sensor T3 at an arbitrary position (for example, a heat exchanger outlet, etc.), thereby detecting the temperature of the smoke, and adjusting so as to cool the smoke at a predetermined temperature. obtain.
The heat exchanger 3 can adjust the flow rate of smoke and the residence time of smoke in the cooling section by changing the length and diameter of the residence tube. The residence time of the soot in the cooling part is not particularly limited, but is usually 0.02 to 30 seconds, and preferably 0.1 to 3 seconds from the viewpoint of preventing precipitation of tar components in the smoke component.
The heat exchanger 3 includes a damper DP4, and by adjusting this, the pressure at which the soot is drawn from the soot generation unit 32 can be adjusted.
Although the apparatus for producing the smoked food of the present invention preferably includes at least a smoke generating part, a secondary heating part, and a smoked part, the cooling part is not necessarily provided. When the smoked food of the present invention is produced by an apparatus not provided with a cooling unit (for example, the apparatus shown in FIG. 2), the smoke smoke heated in the secondary heating unit is, for example, up to the dry smoked part 4 Cooling can be achieved by naturally lowering the temperature while passing through the piping.
（乾燥燻製部）
乾燥燻製部４は、循環ファン４５及び４６、排気ファン４７、バーナーＢ２、温度センサーＴ４及びＴ５を備え、原料食品の熱風乾燥及び燻付けを行うことができる。
循環ファン４５及び４６は、風速や送風方向を調整するインバーターを備えていることが好ましい。循環ファン４５及び４６の運転を交互に切り替えることにより、送風方向を切り替えることができる。あるいは、循環ファンを一つのみにして、ダンパーを開閉することや循環ファンを逆回転にすることにより、送風方向を切り替え得る。
排気ファン４７は、ダンパーＤＰ５を備え、これを調整することにより、燻煙発生部３２から燻煙を引き込む圧力を調整し得る。
温度センサーＴ４及びＴ５は、燻煙雰囲気の温度を測定することができる。
(Dry Smoked Department)
The dried smoked part 4 includes circulation fans 45 and 46, an exhaust fan 47, a burner B2, and temperature sensors T4 and T5, and can dry and braze the raw food.
It is preferable that the circulation fans 45 and 46 include an inverter that adjusts the wind speed and the blowing direction. By alternately switching the operation of the circulation fans 45 and 46, the blowing direction can be switched. Alternatively, the air blowing direction can be switched by using only one circulation fan and opening / closing the damper or rotating the circulation fan in the reverse direction.
The exhaust fan 47 includes a damper DP5, and by adjusting this, the pressure at which soot is drawn from the soot generator 32 can be adjusted.
The temperature sensors T4 and T5 can measure the temperature of the smoke atmosphere.
本発明の燻製食品は、ケトン類、フェノール類、窒素化合物及び炭化水素類を、燻製食品の揮発性成分のガスクロマトグラムにおける上記Ａ〜Ｄが、上記の特定の比率になるように、燻製食品に添加することによっても製造することができる。 The smoked food of the present invention is obtained by adding ketones, phenols, nitrogen compounds and hydrocarbons to the smoked food so that the above A to D in the gas chromatogram of the volatile components of the smoked food have the above-mentioned specific ratio. It can also be manufactured by adding.
本発明の燻製食品は、食品及び調味料の原料として用いることができる。従って、本発明は、本発明の燻製食品を原料とする食品又は調味料、並びに、本発明の燻製食品を原料として用いることを含む、食品又は調味料の製造方法も提供する。 The smoked food of the present invention can be used as a raw material for foods and seasonings. Therefore, this invention also provides the manufacturing method of a foodstuff or a seasoning including using the smoked foodstuff of this invention as a raw material and the foodstuff or seasoning which uses the smoked foodstuff of this invention as a raw material.
本発明の燻製食品を原料とする食品は、燻煙由来の風味が付与されることを所望される食品であれば特に制限されないが、例えば、煮物料理、炒め物料理、焼き物料理、揚げ物料理、ソース、スープ及びこれらの加工品（例、電子レンジ調理用飲食品、インスタント食品、冷凍食品、乾燥食品等）等が挙げられる。
本発明の燻製食品を原料とする調味料は、燻煙由来の風味が付与されることを所望される食品であれば特に限定されないが、具体的には天然系調味料と風味調味料とが例示される。天然系調味料としては、例えば、鰹エキス、鰹節エキス、鰹枯節エキス、宗田鰹節エキス、宗田鰹枯節エキス、鯖エキスなどの各種魚介エキス類；鰹節エキス、鰹枯節エキス、宗田鰹節エキス、宗田鰹枯節エキス、鯖節エキス、グチエキスなどの各種節エキス類；酵母エキス類；各種タンパク加水分解物；醤油、魚醤、蝦醤、味噌などの各種発酵調味料等が挙げられる。また、風味調味料としては、例えば、鰹風味調味料、合わせだし風味調味料、昆布風味調味料、節原料または各種天然調味料を配合しただしパックなどの各種魚介風味調味料等が挙げられる。また、本発明の燻製食品を原料とする調味料の例としては、基礎調味料である、塩、うま味調味料等も挙げられる。
The food using the smoked food of the present invention as a raw material is not particularly limited as long as it is desired to be provided with a smoke-derived flavor. Examples include sauces, soups, and processed products thereof (eg, food and drink for microwave cooking, instant foods, frozen foods, dried foods, etc.).
The seasoning made from the smoked food of the present invention is not particularly limited as long as it is desired to be given a smoke-derived flavor. Specifically, natural seasonings and flavor seasonings include Illustrated. Examples of natural seasonings include various seafood extracts such as bonito extract, bonito extract, bonito extract, soda bonito extract, soda bonito extract, bonito extract; Examples include various knot extracts such as dried bonito extract, koji mushroom extract, guchi extract; yeast extracts; various protein hydrolysates; various fermented seasonings such as soy sauce, fish sauce, koji sauce, miso. Examples of the flavor seasoning include salmon flavor seasoning, soup seasoning seasoning, kelp flavor seasoning, saving ingredients, or various natural seasonings, but various seafood flavor seasonings such as packs. Examples of seasonings made from the smoked food of the present invention include basic seasonings such as salt and umami seasonings.
本発明の燻製食品は、加工することなく、そのまま食品及び調味料の原料として用いてよいが、例えば粉砕、粉末化及びペースト化等の加工を施したものを用いてもよい。また、燻製食品から抽出されたエキス画分を使用してもよい。燻製食品からエキス画分を抽出する方法としては、例えば、液化炭酸ガス抽出法、超臨界ガス抽出法、アルコール抽出法、熱水抽出法等が挙げられる。エキス画分は液状のまま使用し得るが、粉末化して使用してもよい。エキス画分を粉末化する方法としては、例えば、真空乾燥法、凍結乾燥法、スプレードライ法、ドラムドライヤー法、真空ドラムドライヤー法、マイクロ波乾燥法等が挙げられる。またエキス画分を粉末化するとき、必要に応じて賦形剤を添加してもよい。賦形剤の例としては、デキストリン、乳糖、食塩、グルタミン酸ナトリウム、グラニュー糖、ゼラチン等が挙げられる。 The smoked food of the present invention may be used as it is as a raw material for foods and seasonings without being processed, but may be used after processing such as pulverization, pulverization and pasting. Moreover, you may use the extract fraction extracted from the smoked food. Examples of the method for extracting the extract fraction from the smoked food include a liquefied carbon dioxide extraction method, a supercritical gas extraction method, an alcohol extraction method, and a hot water extraction method. The extract fraction can be used in a liquid state, but may be used in the form of powder. Examples of the method for pulverizing the extract fraction include a vacuum drying method, a freeze drying method, a spray drying method, a drum dryer method, a vacuum drum dryer method, and a microwave drying method. Moreover, when pulverizing an extract fraction, you may add an excipient | filler as needed. Examples of excipients include dextrin, lactose, sodium chloride, sodium glutamate, granulated sugar, gelatin and the like.
以下の実施例において本発明を更に具体的に説明するが、本発明はこれらの例によってなんら限定されるものではない。 The present invention will be described more specifically in the following examples, but the present invention is not limited to these examples.
（原料食品の製造）
鰹を常法により煮熟した後に、長辺が２０〜１００ｍｍで、厚みが５〜１５ｍｍであるフレーク状に切削して鰹フレークを得、次いで鰹フレーク１００ｋｇに対し、図２に示される装置を使用して、その乾燥燻製部４にて熱風乾燥を８時間行い、原料食品（乾燥した鰹フレーク）を製造した。熱風の温度は、乾燥開始時は１７０℃とし、２０℃／時間の速度で９０℃まで低下させた後、一定（９０℃）に保持した。熱風の風速は２．０ｍ／秒とした。得られた原料食品（乾燥した鰹フレーク）の水分含量は、１６％であった。ここで原料食品の水分含量は、常圧乾燥法（１０５℃、４時間）により測定した。
(Manufacture of raw food)
After simmering the cocoon by a conventional method, the long side is 20 to 100 mm and the thickness is 5 to 15 mm to obtain a cocoon flake, and then the apparatus shown in FIG. Then, hot air drying was performed for 8 hours in the dried smoked part 4 to produce a raw material food (dried potato flakes). The temperature of the hot air was set to 170 ° C. at the start of drying, decreased to 90 ° C. at a rate of 20 ° C./hour, and then kept constant (90 ° C.). The wind speed of the hot air was 2.0 m / sec. The water content of the obtained raw material food (dried rice cake flakes) was 16%. Here, the moisture content of the raw food was measured by a normal pressure drying method (105 ° C., 4 hours).
（実施例１の燻製食品の製造）
実施例１の燻製食品（鰹節）の製造は、図２に示される装置を使用して、下記の手順で行った。
前記原料食品の製造後、植物原料としてナラのチップ（３３０ｋｇ）を炭化槽４８に収容し、該炭化槽４８をバーナーＢ１で加熱して植物原料（ナラのチップ）を熱分解させ、燻煙を発生させた。熱分解温度は熱分解時間内で平均して３００℃に維持した。発生した燻煙を、２次加熱部の熱交換器２により５５０〜６００℃で加熱した。冷却後の燻煙を乾燥燻製部４内に導入して、原料食品（乾燥した鰹フレーク）を燻煙雰囲気下に存在させることにより、燻煙を原料食品に接触させた。尚、２次加熱部と乾燥燻製部４とをつなぐ配管内の燻煙の温度は１００〜２００℃であった。乾燥燻製部４の雰囲気温度は５０〜８０℃に維持した。炭化槽内の二酸化炭素濃度に対する一酸化炭素濃度の比（ＣＯ／ＣＯ２）が０．４を超えた後（ＣＯ濃度＝２２．５％、ＣＯ２濃度＝５０．３％、ＣＯ／ＣＯ２＝０．４５）は、２次加熱部の熱交換器２による燻煙の加熱温度（５９６℃）を、炭化槽内の二酸化炭素濃度１％低下当たり１６℃下げた。炭化槽内の二酸化炭素濃度が３９．２％に低下した時点で植物原料の熱分解を止め、装置の運転を停止し、燻製食品の製造を終了した。炭化槽内の二酸化炭素濃度が３９．２％に低下した時点の、燻煙の加熱温度は４２４℃であった。
(Production of smoked food of Example 1)
Production of the smoked food product (boiled bonito) of Example 1 was performed by the following procedure using the apparatus shown in FIG.
After production of the raw material food, oak chips (330 kg) are stored in a carbonization tank 48 as a plant raw material, and the carbonization tank 48 is heated by a burner B1 to thermally decompose the plant raw material (oak chips), and soot is produced. Generated. The thermal decomposition temperature was maintained at 300 ° C. on average within the thermal decomposition time. The generated smoke was heated at 550 to 600 ° C. by the heat exchanger 2 of the secondary heating unit. The smoked smoke after being cooled was introduced into the dried smoked part 4, and the raw food (dried smoked flakes) was present in the smoked atmosphere, so that the smoked smoke was brought into contact with the raw food. In addition, the temperature of the smoke in the piping which connects a secondary heating part and the dry smoked part 4 was 100-200 degreeC. The atmospheric temperature of the dried smoked part 4 was maintained at 50-80 ° C. After the ratio of carbon monoxide concentration to carbon dioxide concentration in the carbonization tank (CO / CO 2 ) exceeds 0.4 (CO concentration = 22.5%, CO 2 concentration = 50.3%, CO / CO 2 = 0.45), the soot heating temperature (596 ° C.) by the heat exchanger 2 of the secondary heating unit was reduced by 16 ° C. per 1% decrease in the carbon dioxide concentration in the carbonization tank. When the carbon dioxide concentration in the carbonization tank dropped to 39.2%, the thermal decomposition of the plant raw material was stopped, the operation of the apparatus was stopped, and the production of the smoked food was completed. The heating temperature of the smoke was 424 ° C. when the carbon dioxide concentration in the carbonization tank was reduced to 39.2%.
（比較例１の燻製食品の製造）
炭化槽内の二酸化炭素濃度に対する一酸化炭素濃度の比（ＣＯ／ＣＯ２）が０．４を超えた後も、２次加熱部の熱交換器２による燻煙の加熱温度を下げずに５５０〜６００℃に維持したこと、及び、炭化槽内の二酸化炭素濃度が約６０％に低下した時点で植物原料の熱分解を止めたこと以外は、実施例１と同様の手順で、比較例１の燻製食品の製造を行った。
(Production of smoked food of Comparative Example 1)
Even after the ratio of the carbon monoxide concentration to the carbon dioxide concentration in the carbonization tank (CO / CO 2 ) exceeds 0.4, the heating temperature of the soot smoke by the heat exchanger 2 of the secondary heating unit is not lowered 550. Comparative Example 1 was carried out in the same procedure as in Example 1 except that it was maintained at ˜600 ° C. and the thermal decomposition of the plant material was stopped when the carbon dioxide concentration in the carbonization tank was reduced to about 60%. Smoked food was manufactured.
（燻製食品の揮発性成分の分析）
実施例１及び比較例１において製造した燻製食品（鰹節）の揮発性成分の捕集（分析サンプルの調製）は、ダイナミックヘッドスペース（ＤＨＳ）法により行った。具体的には、以下の手順で、実施例１及び比較例１の燻製食品の揮発性成分を捕集し、分析サンプルを調製した。
［分析サンプルの調製方法］
燻製食品（鰹節）を２ｇ秤取し、１００℃のお湯２００ｇを加え、よく撹拌したのち、１０分間静置する。得られた溶液をフィルターでろ過し、室温まで氷冷した後、ろ液２ｍｌを１０ｍｌスクリューキャップバイアルに正確にとり、栓をする。
(Analysis of volatile components in smoked foods)
The collection (analysis sample preparation) of volatile components of the smoked food (bamboo shoots) produced in Example 1 and Comparative Example 1 was performed by a dynamic headspace (DHS) method. Specifically, the volatile components of the smoked foods of Example 1 and Comparative Example 1 were collected by the following procedure to prepare an analysis sample.
[Preparation method of analysis sample]
Weigh 2 g of smoked food (boiled bonito), add 200 g of 100 ° C. hot water, stir well, and let stand for 10 minutes. The resulting solution is filtered through a filter and cooled with ice to room temperature. Then, 2 ml of the filtrate is accurately taken into a 10 ml screw cap vial and stoppered.
調製した分析サンプルの揮発性成分は、ＧＣ−ＭＳ装置により分析した。
ＤＨＳ法でのサンプル導入にはオートサンプラと加熱脱着装置および昇温気化型注入口を組み合わせて用いた。
＜ＤＨＳ条件＞
使用機器：ＤＨＳオプション付オートサンプラ ＭＰＳ２（ＧＥＲＳＴＥＬ社製）
使用トラップ管：Ｔｅｎａｘ ＴＡ（ＧＥＲＳＴＥＬ社製） 内径４ｍｍ、長さ６０ｍｍ
サンプル温度：３７℃
予備加熱時間：１０ｍｉｎ
トラップ管温度：３７℃
トラップ流量：５０ｍＬ／ｍｉｎ（１２ｍｉｎ）
ドライパージ温度：４０℃
ドライパージ流量：５０ｍＬ／ｍｉｎ（２０ｍｉｎ）
＜加熱脱着装置条件＞
使用装置：ＴＤＵ（ＧＥＲＳＴＥＬ社製）
昇温条件：３０℃（０．２ｍｉｎ保持）→７２０℃／ｍｉｎ昇温→２８０℃（３ｍｉｎ保持）
＜昇温気化型注入口条件＞
使用装置：ＣＩＳ４（ＧＥＲＳＴＥＬ社製）
使用ライナー：Ｔｅｎａｘ ＴＡ（ＧＥＲＳＴＥＬ社製）
トラップ温度：３７℃
スプリットベント流量：２０ｍＬ／ｍｉｎ（２ｍｉｎ）
注入温度：２５０℃
＜ＧＣ条件＞
使用機器：７８９０Ａ（Ａｇｉｌｅｎｔ Ｔｅｃｈｎｏｌｏｇｉｅｓ社製）
使用カラム：ＤＢ−ＷＡＸ（Ｊ＆Ｗ社製） 内径０．２５ｍｍ、長さ６０ｍ、膜厚０．２５μｍ
キャリアガス：Ｈｅ
キャリアガス流量：１．５ｍＬ／ｍｉｎ（コンスタントフローモード）
オーブン温度：４０℃（２ｍｉｎ保持）→４℃／ｍｉｎ昇温→２２０℃（５ｍｉｎ保持）
＜ＭＳ条件＞
使用機器：５９７５Ｃ（Ａｇｉｌｅｎｔ Ｔｅｃｈｎｏｌｏｇｉｅｓ社製）
イオン化モード：ＥＩ
イオン化電圧：７０ｅＶ
測定モード：Ｓｃａｎ（２９〜３００ａｍｕ）
The volatile component of the prepared analytical sample was analyzed with a GC-MS apparatus.
For sample introduction by the DHS method, an autosampler, a heat desorption apparatus, and a temperature rising vaporization type inlet were used in combination.
<DHS conditions>
Equipment used: Autosampler with DHS option MPS2 (manufactured by GERSTEL)
Trap tube used: Tenax TA (manufactured by GERSTEL) ID 4 mm, length 60 mm
Sample temperature: 37 ° C
Preheating time: 10 min
Trap tube temperature: 37 ° C
Trap flow rate: 50 mL / min (12 min)
Dry purge temperature: 40 ° C
Dry purge flow rate: 50 mL / min (20 min)
<Heat desorption equipment conditions>
Equipment used: TDU (manufactured by GERSTEL)
Temperature rise condition: 30 ° C. (0.2 min hold) → 720 ° C./min temperature rise → 280 ° C. (3 min hold)
<Temperature rise type inlet conditions>
Equipment used: CIS4 (GERSTEL)
Liner used: Tenax TA (manufactured by GERSTEL)
Trap temperature: 37 ° C
Split vent flow rate: 20 mL / min (2 min)
Injection temperature: 250 ° C
<GC conditions>
Equipment used: 7890A (manufactured by Agilent Technologies)
Column used: DB-WAX (manufactured by J & W) Inner diameter 0.25 mm, length 60 m, film thickness 0.25 μm
Carrier gas: He
Carrier gas flow rate: 1.5mL / min (constant flow mode)
Oven temperature: 40 ° C. (2 min hold) → 4 ° C./min temperature rise → 220 ° C. (5 min hold)
<MS conditions>
Equipment used: 5975C (manufactured by Agilent Technologies)
Ionization mode: EI
Ionization voltage: 70 eV
Measurement mode: Scan (29-300 amu)
得られたトータルイオンクロマトグラム（ＴＩＣ）から、ケトン類のピーク面積の総和（Ａ）、フェノール類のピーク面積の総和（Ｂ）、窒素化合物のピーク面積の総和（Ｃ）、炭化水素類のピーク面積の総和（Ｄ）及び全成分の各ピーク面積の総和をそれぞれ測定し、全成分のピーク面積の総和に占めるＡ〜Ｄの各割合を算出した。実施例１の結果を表１に、比較例１の結果を表２それぞれに示す。 From the obtained total ion chromatogram (TIC), the sum of peak areas of ketones (A), the sum of peak areas of phenols (B), the sum of peak areas of nitrogen compounds (C), and the peak of hydrocarbons The total area (D) and the total sum of the peak areas of all components were measured, and each ratio of A to D in the total peak area of all components was calculated. The results of Example 1 are shown in Table 1, and the results of Comparative Example 1 are shown in Table 2, respectively.
（燻製食品の官能評価）
実施例１及び比較例１において製造した燻製食品（鰹節、２０ｇ）をそれぞれミキサーで粉砕した後、１００℃のお湯（２，０００ｇ）に溶解し、１％熱水溶液を評価サンプルとして作製した。
各評価サンプルを１０分間、１００℃で加熱した後、８名の訓練されたパネルが、加熱前及び加熱後の評価サンプルを飲み、それぞれの燻香（燻煙由来の香り）の強度を評価した。評価は、加熱前の燻香の強度を５点、全く燻香がない状態を０点とする評点法により行った。実施例１及び比較例１の加熱前の評価サンプルの燻香の強度は、ほぼ同等であった。
結果（８名のパネルの評点の平均、標準偏差）を表３に示す。また比較例１の結果を図４に、実施例１の結果を図５にそれぞれ示す。
(Sensory evaluation of smoked foods)
The smoked foods produced in Example 1 and Comparative Example 1 (bonito, 20 g) were each pulverized with a mixer and then dissolved in 100 ° C. hot water (2,000 g) to prepare a 1% hot aqueous solution as an evaluation sample.
After each evaluation sample was heated at 100 ° C. for 10 minutes, 8 trained panels swallowed the evaluation samples before and after heating and evaluated the strength of each smoke (smoke derived scent). . The evaluation was performed by a scoring method in which the intensity of musk before heating was 5 points, and the state where no musk was present was 0 points. The intensity | strength of the musk of the evaluation sample before a heating of Example 1 and Comparative Example 1 was substantially equivalent.
The results (average score of 8 panels, standard deviation) are shown in Table 3. The results of Comparative Example 1 are shown in FIG. 4, and the results of Example 1 are shown in FIG.
表３、図４及び図５に示す結果から明らかなように、本発明の実施例１の燻製食品は、比較例１の燻製食品に比べ、加熱後も燻香が維持されることが示された。 As is apparent from the results shown in Table 3, FIG. 4 and FIG. 5, the smoked food of Example 1 of the present invention shows that the smoked smoke is maintained after heating as compared with the smoked food of Comparative Example 1. It was.
本発明によれば、加熱されても香りが減弱及び消失しにくい燻製食品を提供することができる。特に、本発明により提供される加熱されても香りが減弱及び消失しにくい燻製食品は、使用する植物原料の種類を変更することなく製造し得るため、目的とする好ましい香りの質が損なわれることなく、燻煙由来の好ましい香りを有し得る。 ADVANTAGE OF THE INVENTION According to this invention, the smoked food which a fragrance is hard to attenuate and lose | disappear even if heated can be provided. In particular, the smoked food provided by the present invention that does not weaken and disappear even when heated can be produced without changing the type of plant material used, so that the desired fragrance quality is impaired. And may have a preferred scent derived from smoke.
２、３ 熱交換機
４ 乾燥燻煙部
３２ 燻煙発生部
３３ 電気ヒーター
４４ トレイ
４５、４６ 循環ファン
４７ 排気ファン
４８ 炭化槽
ＤＰ４、ＤＰ５ ダンパー
Ｔ１、Ｔ２、Ｔ３、Ｔ４、Ｔ５ 温度センサー
Ｂ１、Ｂ２ バーナー
2, 3 Heat exchanger 4 Dry smoke section 32 Smoke generation section 33 Electric heater 44 Tray 45, 46 Circulation fan 47 Exhaust fan 48 Carbonization tank DP4, DP5 Damper T1, T2, T3, T4, T5 Temperature sensors B1, B2 Burner
Claims (5)
Ａ：（Ｂ＋Ｃ）が、１５〜３５：４５〜７５である、燻製食品。 In the gas chromatogram of the volatile components of smoked food, when the sum of peak areas of ketones is A, the sum of peak areas of phenols is B, and the sum of peak areas of nitrogen compounds is C,
A: (B + C) is 15-35: 45-75 smoked food.
Ａ：Ｄが、１５〜３５：５〜１０である、請求項１記載の燻製食品。 Furthermore, when the sum of the peak areas of hydrocarbons in the gas chromatogram of the volatile components of smoked food is D,
The smoked food according to claim 1, wherein A: D is 15 to 35: 5 to 10.
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| JP2015078538 | 2015-04-07 | ||
| JP2015078538 | 2015-04-07 |
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007142086A1 (en) * | 2006-06-07 | 2007-12-13 | Ajinomoto Co., Inc. | Method and apparatus for modifying smoke smell and method and apparatus for producing smoked food |
| JP2011250743A (en) * | 2010-06-02 | 2011-12-15 | Ajinomoto Co Inc | Smoke generation material |
| JP2016198002A (en) * | 2015-04-07 | 2016-12-01 | 味の素株式会社 | Method for producing smoked food |
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007142086A1 (en) * | 2006-06-07 | 2007-12-13 | Ajinomoto Co., Inc. | Method and apparatus for modifying smoke smell and method and apparatus for producing smoked food |
| JP2011250743A (en) * | 2010-06-02 | 2011-12-15 | Ajinomoto Co Inc | Smoke generation material |
| JP2016198002A (en) * | 2015-04-07 | 2016-12-01 | 味の素株式会社 | Method for producing smoked food |
Non-Patent Citations (2)
| Title |
|---|
| POHLMANN, M. ET AL., MEAT SCIENCE, vol. 90, JPN6019007647, 2012, pages 176 - 184, ISSN: 0004386256 * |
| 第350回 ガスクロマトグラフィー研究講演会, JPN7020003647, 2017, ISSN: 0004386255 * |
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