JPH0137097B2 - - Google Patents

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Publication number
JPH0137097B2
JPH0137097B2 JP22834785A JP22834785A JPH0137097B2 JP H0137097 B2 JPH0137097 B2 JP H0137097B2 JP 22834785 A JP22834785 A JP 22834785A JP 22834785 A JP22834785 A JP 22834785A JP H0137097 B2 JPH0137097 B2 JP H0137097B2
Authority
JP
Japan
Prior art keywords
sorbic acid
potassium sorbate
weight
adduct
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
Application number
JP22834785A
Other languages
Japanese (ja)
Other versions
JPS6287045A (en
Inventor
Masahiro Nakajima
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JNC Corp
Original Assignee
Chisso Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Chisso Corp filed Critical Chisso Corp
Priority to JP22834785A priority Critical patent/JPS6287045A/en
Publication of JPS6287045A publication Critical patent/JPS6287045A/en
Publication of JPH0137097B2 publication Critical patent/JPH0137097B2/ja
Granted legal-status Critical Current

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  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、かまぼこや、ソーセージ等の肉質の
練製品を製造する際に、保存剤として使用に適す
るソルビン酸−ソルビン酸カリウムの付加物又
は、ソルビン酸カリウムとソルビン酸−ソルビン
酸カリウム付加物の混合物によつて被覆されたソ
ルビン酸製剤及びその製造法に関するものであ
る。 かまぼこや、ソーセージ等の肉質の練製品を製
造する際に、貯蔵性を増大せしめる目的で防腐剤
としてソルビン酸及びその塩が一般に使用されて
いるのが、ソルビン酸は従来から食品生地のPHを
低下させて、蛋白質の凝固脱水が起こり、製品の
弾力や風味を低下させる事は良く知られている。
従つて、従来防腐剤としては、ソルビン酸カリウ
ムを添加してきたが、ソルビン酸は酸性におい
て、良く抗菌性が発揮されるものであり、ソルビ
ン酸カリウムを添加した場合は、塩基性であるが
故に抗菌作用は著しく減少する。 本発明者は、食品生地をいためず、出来上がり
製品の貯蔵性を高めるソルビン酸製剤について研
究し、練製品製造に適した添加剤の開発に成功し
たものである。 本発明者はまずソルビン酸(以下「SA」と略
記することがある。)とソルビン酸カリウム(以
下「KSA」と略記することがある。)の粉末を混
合した製剤を試み、ソルビン酸含量40重量%以上
の製剤は、練製品の保存性においてソルビン酸と
同じ効果を発揮する事を知つた。しかし、ソルビ
ン酸とソルビン酸カリウムを混合した製剤は、分
離しやすく、蒸煮前に食品生地にソルビン酸が直
接接触した部分に蛋白質の変性が見られソルビン
酸カリウムを使用した製品と比較して弾力、風味
共満足すべき結果を得ることはできなかつた。 本発明者は、ソルビン酸の粒子が直接食品生地
に接触するのを防止する為に、ソルビン酸の粒子
をソルビン酸カリウムで被覆した製剤を作ること
を思い付き、鋭意研究を進めた結果、ソルビン
酸、ソルビン酸カリウム及び水を含む混合物であ
つて前記ソルビン酸とソルビン酸カリウムの合計
量に対する水の量を30重量%を越える量とし該ソ
ルビン酸の大部分が溶解しない室温付近で十分な
接触を行なわせる事によつて、ソルビン酸と、ソ
ルビン酸カリウムが反応し、ソルビン酸−ソルビ
ン酸カリウム付加物が生成するという全く意外な
事実を発見して本発明に到達したものである。つ
まり、ある程度の水が存在すればSAの大部分が
未溶解の状態であつても、ソルビン酸とソルビン
酸カリウムの充分な接触が行なわれ接触した部分
で反応して付加物が生成してソルビン酸粒子を被
覆した製剤が製造される訳である。 以下本製剤の製造法について詳細に説明する。 本製剤の製造は、ソルビン酸、ソルビン酸カリ
ウム及び水を撹拌処理して製造するものであり、
ソルビン酸粒子の大小、ソルビン酸カリウム濃度
すなわち、ソルビン酸カリウムと水の合計量に対
するソルビン酸カリウムの割合、及びソルビン酸
とソルビン酸カリウムの割合、その他撹拌条件に
よつて製剤の品質に影響を与える。 本発明に使用するソルビン酸粒子は特に限定さ
れないが60メツシユの篩を通過し平均粒度が100
メツシユより小さいことが好ましい。60メツシユ
の篩に止まる粒子は、比表面積が小さく、被覆用
のソルビン酸カリウムが少なくて良いという利点
もあるが、反面製剤の食品生地への均一分散が困
難になる事や、被覆に用いられたソルビン酸カリ
ウムが少い為に平均PHが低下し、食品によつて
は、食品生地に変性を起こす事があつて好ましく
ない。 本製剤の製造に使用するソルビン酸カリウム濃
度は27〜62重量%が好ましく更に好ましくは、30
〜58重量%の範囲である。ソルビン酸カリウム濃
度が27重量%より小さくなるような場合は、付加
物が生成しがたく、従つて被覆が不完全になり易
い。工業的には27重量%より小さい濃度のソルビ
ン酸カリウム水溶液を用いざるを得ないようなこ
とが少なくない訳であるが、このような場合は、
水を蒸発させて濃縮して、原料として用いること
が望ましい。一方ソルビン酸カリウム濃度が62重
量%を越えるとソルビン酸とソルビン酸カリウム
の接触が通常の撹拌では十分に行い難く従つて不
均一な製剤になりやすいので好ましくない。 本製剤を製造するに当つての温度は0℃以上45
℃未満好ましくは0〜40℃更に好ましくは10〜35
℃がよい。この温度は高温になる程生成した付加
物の溶解度が上昇してSA結晶の回りに付着し難
くなる。即ち40℃より高い温度、特に45℃以上の
温度で反応させた後冷却して過し固液分離する
と、析出した付加物の結晶がSAの回りを被覆す
ることなく単独で存在する傾向が強いため被覆が
不完全になると共に不均一な製剤になり易い。又
45℃以上の温度にすることはエネルギーコストの
上からも好ましくない。更には、母液の循環を考
慮すると高温になる程母液の着色がはげしくなる
傾向があるため好ましくない。 本製剤を製造するに当つてのソルビン酸とソル
ビン酸カリウムの割合はソルビン酸1にに対して
ソルビン酸カリウムを1以上(重量比)使用する
のが好ましい。 ソルビン酸カリウムの使用量が1未満であるよ
うに少い場合には撹拌処理が困難になると共に、
被覆が不完全で目的とする製剤は製造できにく
い。本製剤を製造するにあたつての撹拌処理はホ
モミキサーやホモジナイサーその他均一に混合出
来る一般的な装置で行なわれる。均一混合が不完
全な撹拌処理を行うと、部分的にかたまりが出来
たり、又、被覆が不完全な製剤になりやすい。 なお、上記ソルビン酸カリウムは水に分散させ
たソルビン酸の一部を水酸化カリウムまたは炭酸
カリウムで中和することにより生成させてもよ
い。 以上のような条件でソルビン酸とソルビン酸カ
リウムを反応させ、ソルビン酸の回りを付加物に
よつて被覆した後、一般的な方法で過し、過剰
のソルビン酸カリウムと水とを分離する。得られ
た含水の製剤を真空乾燥や流動乾燥等によつて水
を蒸発させ目的とする製剤が製造される。この製
剤をX線回析で分析すると、大部分ソルビン酸と
付加物又は若干ソルビン酸カリウムを含有してい
る製剤であり、この製剤をアルコール−水の混合
溶媒に溶解してSAとKSAに分解して中和滴定に
より分析すると、ソルビン酸として50重量%〜70
重量%の含有量を持つ製剤が得られる。 かくして製造された製剤は水に分散しやすいと
いう特性を持ち、直接食品生地にねり込んでも、
又は一旦水に投入して分散させて使用しても、食
品生地をいためる事はなく有効に食品保存剤とし
ての働きを発揮する。 なお、この製造方法によれば、過による液
の発生があるが、再使用が可能であり、工業的に
不利益は生じない。 本発明の製剤の製造に当つて、公知の酸化防止
剤例えば、L−アスコルビン酸ソーダ、エリソル
ビン酸、BHT等を添加しても何んら支障はない。
又、親水性界面活性剤としてしよ糖脂肪酸エステ
ル等を添加しても支障は生じない。その他有機酸
塩例えばクエン酸ソーダ、酢酸ソーダ又は燐酸塩
の併用も、場合により効果を向上させる。 実施例 1 室温においてホモジナイザーで撹拌している30
重量%KSA水溶液1000g(水700g、KSA300
g)に60メツシユの篩を100%通過し、200メツシ
ユに停まる割合が84%の粒度であるSA100gを少
しづつ添加した後、30分〜1時間撹拌を続けた。
この混合液をセントルで脱液した後、ケーキを40
℃で4時間真空乾燥して粉末の製剤約165gを得
た。乾燥前後の重量差より計算してケーキは水分
14重量%を含有していた。 真空乾燥して得た製剤をアルコール水の混合溶
媒に溶解してN/2KOHで中和滴定を行うと、
SA含有量か58重量%である。 比較例 1 25重量%KSA水溶液1000g(水750g、
KSA250g)に変えた他は、実施例1と同じ方法
で行い、乾燥した粉末の製剤約95gを得た(ケー
キ含水率8重量%)。中和滴定によりSA含有率を
分析すると98重量%であり、(ほとんど被覆はさ
れず、目的とする製剤は得られなかつた。 実施例 2 分級型の晶析器で結晶となした80メツシユ〜
200メツシユの粒度65重量%を含有する未乾燥SA
(水8重量%含)109gと純水500gを撹拌してい
る容器に未乾燥のKSA(水7重量%含)500gを
少しずつ添加した後、室温下で30分〜1時間撹拌
を行つてからセントルで固液分離を行つた。得ら
れたケーキは260gで(液は840g収得)このケ
ーキを40℃で4時間乾燥して215gの乾燥した製
剤を得た。 得られた製剤をX線回析でしらべると大部分
SA及びSA−KSAの付加物であり、アルコール
−水の混合溶媒に溶解して中和滴定によつてSA
含有量を分析すると付加物の中のSAの部分も含
めて50重量%のSA含有量であつた。 実施例 3 実施例2の液840g(KSA約320g含)を室
温で撹拌しておき、その中に150〜300メツシユの
粒度72重量%を含有する乾燥したSA100gを少し
づつ添加して室温で30分〜1時間撹拌後、セント
ルで過した。得られたケーキは200gであり、
液は730gであつた。ケーキを40℃で4時間真
空乾燥して、165gの乾燥した製剤を得た。 この製剤をX線回析で分析すると大部分がSA
及び付加物であり、又アルコールと水の混合溶媒
によつてこの製剤を溶解し中和滴定でSA含有量
に分析すると、付加物中のSAの部分も含めて、
58重量%のSA含有量であつた。 実施例 4 20重量%KOH1000g(KOH200g、水800g)
に60メツシユの篩を100%通過し、80〜150メツシ
ユの割合が75重量%の粒度であるSA500gを撹拌
しながら投入した。中和反応によつて発熱し、温
度が44℃に達した為、冷却しながら撹拌を30分〜
1時間続けた。室温で過してケーキ約200gを
収得し、このケーキを40℃で4時間真空乾燥して
170gの乾燥した製剤を得た。 この製剤をX線回析で分析すると、大部分SA
及び付加物でありアルコールと水の混合溶媒によ
つてこの製剤を溶解し、中和滴定によつてSA含
有量を分析すると付加物中のSAの部分も含めて
56重量%のSA含有量であつた。 実施例 5 シユガーエステル0.3gを含有する30重量%
KSA水溶液1000g(KSA300g、水700g)に60
メツシユの篩を100重量%通過し、80〜200メツシ
ユの範囲の粒度が65重量%であるSA200gを投入
して室温下30〜60分撹拌した。セントルで過し
て得られたケーキ330gを40℃で4時間真空乾燥
して285gの乾燥した製剤を得た。 この製剤をX線回析で分析すると大部分がSA
及びKSAであり、中和滴定によつてSA含有量を
分析すると付加物の中のSAの部分も含めてSA70
重量%であつた。 参考例 冷凍すり身2000部に食塩60部及び冷水300部を
添加して約20分間擂潰した後、かたくり粉120部、
砂糖10部、調味料20部を混合してさらに15分間擂
潰した。次に250部づつに小分けし、それぞれに
実施例1、2、5で得られた製剤を冷凍すり身に
対してSAとして(KSA中のSAも含む)0.2%を
添加し良く練り合わせた。続いて盛り付けし、座
りを8時間行つた後、95℃で25分間蒸煮してカマ
ボコとなした。比較の為、無添加、SA、KSA及
び付加物を添加したカマボコも製造した。 これらのカマボコについて、各製造工程におけ
るPHの測定及び製品の弾力についての官能的試験
を行つた結果を表−1に示す。
The present invention provides an adduct of sorbic acid-potassium sorbate, or an adduct of potassium sorbate and sorbic acid-potassium sorbate, which is suitable for use as a preservative in the production of meat paste products such as kamaboko and sausages. The present invention relates to a sorbic acid preparation coated with a mixture and a method for producing the same. Sorbic acid and its salts are commonly used as preservatives to increase shelf life when producing meaty paste products such as kamaboko and sausages, but sorbic acid has traditionally been used to control the pH of food dough. It is well known that this decrease causes protein coagulation and dehydration, which reduces the elasticity and flavor of the product.
Therefore, potassium sorbate has traditionally been added as a preservative, but sorbic acid exhibits antibacterial properties well in acidic conditions, and when potassium sorbate is added, it is basic. Antibacterial action is significantly reduced. The present inventor has researched a sorbic acid formulation that does not damage food dough and improves the shelf life of finished products, and has succeeded in developing an additive suitable for producing dough products. The present inventor first attempted a formulation containing powders of sorbic acid (hereinafter sometimes abbreviated as "SA") and potassium sorbate (hereinafter sometimes abbreviated as "KSA"), and found that the sorbic acid content was 40%. It was found that preparations with a concentration of sorbic acid or higher than sorbic acid have the same effect as sorbic acid in terms of the preservability of paste products. However, preparations made by mixing sorbic acid and potassium sorbate tend to separate easily, and protein denaturation is observed in the areas where sorbic acid comes into direct contact with the food dough before steaming, making it less elastic than products using potassium sorbate. However, it was not possible to obtain satisfactory results in terms of flavor and flavor. The inventor of the present invention came up with the idea of creating a preparation in which sorbic acid particles are coated with potassium sorbate in order to prevent sorbic acid particles from coming into direct contact with food dough, and as a result of intensive research, found that sorbic acid , a mixture containing potassium sorbate and water, in which the amount of water exceeds 30% by weight based on the total amount of the sorbic acid and potassium sorbate, and sufficient contact is carried out at around room temperature where most of the sorbic acid is not dissolved. The present invention was achieved by discovering the completely unexpected fact that by carrying out this process, sorbic acid and potassium sorbate react to form a sorbic acid-potassium sorbate adduct. In other words, if a certain amount of water is present, even if most of the SA is undissolved, sufficient contact between sorbic acid and potassium sorbate will occur, and an adduct will be produced by reaction at the contact area, resulting in the formation of sorbic acid and potassium sorbate. This means that a preparation coated with acid particles is produced. The manufacturing method of this preparation will be explained in detail below. This preparation is manufactured by stirring sorbic acid, potassium sorbate, and water.
The quality of the preparation is affected by the size of sorbic acid particles, potassium sorbate concentration, i.e., the ratio of potassium sorbate to the total amount of potassium sorbate and water, the ratio of sorbic acid to potassium sorbate, and other stirring conditions. . The sorbic acid particles used in the present invention are not particularly limited, but they pass through a 60-mesh sieve and have an average particle size of 100
Preferably, it is smaller than the mesh. Particles that can fit through a 60-mesh sieve have the advantage of having a small specific surface area and require less potassium sorbate for coating, but on the other hand, it may be difficult to uniformly disperse the formulation into food dough, and it may be difficult to use for coating. Since the amount of potassium sorbate is low, the average pH decreases, and depending on the food, it may cause denaturation of the food dough, which is undesirable. The concentration of potassium sorbate used in the production of this preparation is preferably 27 to 62% by weight, more preferably 30% by weight.
~58% by weight. When the potassium sorbate concentration is less than 27% by weight, adducts are difficult to form and therefore coverage tends to be incomplete. Industrially, it is often necessary to use a potassium sorbate aqueous solution with a concentration lower than 27% by weight, but in such cases,
It is desirable to evaporate and concentrate water and use it as a raw material. On the other hand, if the concentration of potassium sorbate exceeds 62% by weight, it is difficult to bring the sorbic acid and potassium sorbate into sufficient contact with each other by ordinary stirring, which tends to result in a non-uniform preparation, which is not preferred. The temperature for manufacturing this preparation is 0℃ or higher45
Less than ℃, preferably 0 to 40℃, more preferably 10 to 35℃
℃ is better. The higher the temperature, the higher the solubility of the generated adducts, making it more difficult for them to adhere around the SA crystal. In other words, if the reaction is performed at a temperature higher than 40°C, especially at a temperature higher than 45°C, then cooled, filtered, and solid-liquid separated, there is a strong tendency for the crystals of the precipitated adduct to exist alone without covering the SA. This tends to result in incomplete coating and non-uniform preparations. or
Setting the temperature to 45°C or higher is not preferable from the standpoint of energy costs. Furthermore, considering the circulation of the mother liquor, the higher the temperature, the more intense the coloring of the mother liquor tends to be, which is not preferable. Regarding the ratio of sorbic acid and potassium sorbate in producing this preparation, it is preferable to use 1 part potassium sorbate to 1 part sorbic acid (weight ratio). When the amount of potassium sorbate used is small, such as less than 1, stirring becomes difficult and
The coating is incomplete, making it difficult to manufacture the desired formulation. The stirring process for producing this preparation is carried out using a homomixer, homogenizer, or other general equipment capable of uniform mixing. If a stirring treatment is performed that does not achieve uniform mixing, it is likely that the preparation will form lumps or be incompletely coated. Note that the above potassium sorbate may be produced by neutralizing a portion of sorbic acid dispersed in water with potassium hydroxide or potassium carbonate. Sorbic acid and potassium sorbate are reacted under the above conditions, and after the sorbic acid is coated with the adduct, excess potassium sorbate and water are separated by passing through a conventional method. The desired formulation is produced by evaporating water from the obtained water-containing formulation by vacuum drying, fluidized drying, or the like. When this preparation was analyzed by X-ray diffraction, it was found that it contained mostly sorbic acid and adducts or a small amount of potassium sorbate.This preparation was dissolved in an alcohol-water mixed solvent and decomposed into SA and KSA. When analyzed by neutralization titration, the amount of sorbic acid is 50% to 70% by weight.
A formulation with a content of % by weight is obtained. The preparations produced in this way have the property of being easily dispersed in water, and can be mixed directly into food dough.
Alternatively, even if it is used once dispersed in water, it will not damage food dough and will effectively function as a food preservative. In addition, according to this manufacturing method, a liquid is generated due to evaporation, but it can be reused and there is no industrial disadvantage. In producing the formulation of the present invention, there is no problem in adding known antioxidants such as sodium L-ascorbic acid, erythorbic acid, BHT, etc.
Further, no problem occurs even if a sucrose fatty acid ester or the like is added as a hydrophilic surfactant. The combined use of other organic acid salts, such as sodium citrate, sodium acetate, or phosphate, can also improve the effect in some cases. Example 1 Stirring with a homogenizer at room temperature30
Weight% KSA aqueous solution 1000g (700g water, KSA300
100 g of SA having a particle size that passed 100% through a 60-mesh sieve and 84% remained at a 200-mesh sieve was added little by little to g), and stirring was continued for 30 minutes to 1 hour.
After deliquifying this mixture with a centaur, the cake was
About 165 g of a powder preparation was obtained by vacuum drying at ℃ for 4 hours. The moisture content of the cake is calculated from the difference in weight before and after drying.
It contained 14% by weight. When the preparation obtained by vacuum drying is dissolved in a mixed solvent of alcohol and water and subjected to neutralization titration with N/2KOH,
SA content is 58% by weight. Comparative Example 1 1000g of 25% KSA aqueous solution (750g of water,
The procedure was carried out in the same manner as in Example 1, except that KSA (250 g) was used, and about 95 g of a dry powder preparation was obtained (cake moisture content: 8% by weight). When the SA content was analyzed by neutralization titration, it was found to be 98% by weight (there was almost no coating, and the desired formulation could not be obtained).
Undried SA containing 200 mesh particle size 65% by weight
After gradually adding 500 g of undried KSA (containing 7 wt.% water) to a container in which 109 g (containing 8 wt.% water) and 500 g of pure water were being stirred, the mixture was stirred at room temperature for 30 minutes to 1 hour. Solid-liquid separation was performed using a centrifuge. The resulting cake weighed 260 g (840 g of liquid was obtained) and was dried at 40° C. for 4 hours to obtain 215 g of a dry preparation. When the obtained preparation was examined by X-ray diffraction, most of the
It is an adduct of SA and SA-KSA, and SA is dissolved in a mixed solvent of alcohol and water and determined by neutralization titration.
Analysis of the content revealed that the SA content, including the SA portion in the adduct, was 50% by weight. Example 3 840 g of the liquid of Example 2 (containing about 320 g of KSA) was stirred at room temperature, and 100 g of dried SA containing 72% by weight of particle size of 150 to 300 mesh was added little by little to the mixture. After stirring for minutes to 1 hour, it was filtered through a centrifuge. The resulting cake weighed 200g;
The liquid weighed 730g. The cake was vacuum dried at 40° C. for 4 hours to obtain 165 g of dry formulation. When this preparation was analyzed by X-ray diffraction, most of it was found to be SA.
and adduct, and when this preparation is dissolved in a mixed solvent of alcohol and water and analyzed for SA content by neutralization titration, including the SA portion in the adduct,
The SA content was 58% by weight. Example 4 1000g of 20% KOH (200g of KOH, 800g of water)
While stirring, 500 g of SA having a particle size of 75% by weight that passed through a 60 mesh sieve 100% and a ratio of 80 to 150 mesh was added. The neutralization reaction generated heat and the temperature reached 44℃, so stirring was continued for 30 minutes while cooling.
It lasted for an hour. About 200g of cake was obtained by filtering at room temperature, and this cake was vacuum dried at 40℃ for 4 hours.
170 g of dry formulation was obtained. When this preparation was analyzed by X-ray diffraction, most of the SA
When this preparation is dissolved in a mixed solvent of alcohol and water and the SA content is analyzed by neutralization titration, the SA content in the adduct is also included.
The SA content was 56% by weight. Example 5 30% by weight containing 0.3g of sugar esters
60 to 1000g of KSA aqueous solution (300g of KSA, 700g of water)
200 g of SA having passed 100% by weight through a mesh sieve and having a particle size of 65% by weight in the range of 80 to 200 mesh was added and stirred at room temperature for 30 to 60 minutes. 330 g of the cake obtained by centrifugation was vacuum dried at 40° C. for 4 hours to obtain 285 g of a dry preparation. When this preparation was analyzed by X-ray diffraction, most of it was found to be SA.
and KSA, and when the SA content is analyzed by neutralization titration, it is SA70 including the SA part in the adduct.
It was in weight%. Reference example: Add 60 parts of salt and 300 parts of cold water to 2,000 parts of frozen surimi, mash for about 20 minutes, and then add 120 parts of Katakuri powder.
10 parts of sugar and 20 parts of seasoning were mixed and mashed for an additional 15 minutes. Next, the mixture was divided into 250 parts, and 0.2% of the preparations obtained in Examples 1, 2, and 5 were added to the frozen surimi as SA (including SA in KSA) and kneaded well. Next, it was plated, left to sit for 8 hours, and then steamed at 95℃ for 25 minutes to form kamaboko. For comparison, we also produced kamaboko without additives and with added SA, KSA, and additives. Table 1 shows the results of PH measurements in each manufacturing process and sensory tests on product elasticity for these kamaboko.

【表】 前記カマボコを貯蔵した場合の各製剤の防腐効
果についての試験結果を表−2に示す。この貯蔵
試験は、温度28〜32℃、相対湿度70〜90%で放置
して行つたもので、ネト及びカビの発生を観察し
て防腐効果を比較した。
[Table] Table 2 shows the test results regarding the preservative effect of each preparation when the Kamaboko was stored. In this storage test, the samples were left at a temperature of 28 to 32°C and a relative humidity of 70 to 90%, and the growth of mold and mildew was observed to compare the preservative effects.

【表】【table】

【表】 表−2より本発明製剤はKSA及び付加物より
も防腐効果がすぐれていることがわかる。
[Table] Table 2 shows that the preparation of the present invention has a better preservative effect than KSA and its additives.

Claims (1)

【特許請求の範囲】 1 ソルビン酸をC6H8O2・C6H7O2Kなるソルビ
ン酸とソルビン酸カリウムの付加物(以下「付加
物」という。)又は該付加物とソルビン酸カリウ
ムの混合物によつて被覆したことを特徴とするソ
ルビン酸製剤。 2 第1項に記載のソルビン酸製剤において、次
の式で計算したとき50〜70重量%となることを特
徴とする前記製剤。 {A/(A+B)}×100 但しここにA、Bは次のものを表わす。 A:ソルビン酸と付加物の内のソルビン酸の部
分の和の重量 B:ソルビン酸カリウムと付加物の内のソルビ
ン酸カリウムの部分の和の重量 3 ソルビン酸、ソルビン酸カリウム及び水を含
む混合物であつて、前記ソルビン酸とソルビン酸
カリウムの合計量に対する水の量を30重量%を越
える量としたものを0℃以上45℃未満の温度で撹
拌処理する事を特徴とするソルビン酸を付加物又
は付加物とソルビン酸カリウムの混合物で被覆し
たソルビン酸の製剤の製造方法。 4 第3項に記載の方法において、ソルビン酸の
一部を水酸化カリウムまたは炭酸カリウムで中和
してソルビン酸、ソルビン酸カリウム及び水を含
む混合物を製造することを特徴とする方法。 5 第3項又は第4項に記載の方法においてソル
ビン酸カリウム濃度すなわち、ソルビン酸カリウ
ムと水の合計量に対するソルビン酸カリウムの割
合を27〜62重量%とし、ソルビン酸とソルビン酸
カリウムの重量比をソルビン酸1に対してソルビ
ン酸カリウム1以上として、ソルビン酸、ソルビ
ン酸カリウム及び水の混合物を作り、該混合物を
撹拌処理する事によつて、付加物を生成させた後
に、過によつて、過剰のソルビン酸カリウムの
水溶液を除去することを特徴とする前記方法。 6 第3項、4項又は5項に記載の方法において
原料のソルビン酸の粒度が60メツシユの篩を通過
し、平均粒度が100メツシユ以下であることを特
徴とする前記方法。 7 第3項ないし第6項のいずれかに記載の方法
において、ソルビン酸、ソルビン酸カリウム及び
水の撹拌処理を0〜40℃の温度で行なうことを特
徴とする前記方法。
[Claims] 1. Sorbic acid is an adduct of sorbic acid and potassium sorbate (hereinafter referred to as "adduct") consisting of C 6 H 8 O 2 and C 6 H 7 O 2 K, or the adduct and sorbic acid. A sorbic acid preparation characterized in that it is coated with a mixture of potassium. 2. The sorbic acid preparation according to item 1, wherein the sorbic acid preparation is 50 to 70% by weight when calculated using the following formula. {A/(A+B)}×100 However, here A and B represent the following. A: Weight of the sum of sorbic acid and the sorbic acid portion in the adduct B: Weight of the sum of potassium sorbate and the potassium sorbate portion in the adduct 3 A mixture containing sorbic acid, potassium sorbate, and water Added sorbic acid, characterized in that the amount of water is more than 30% by weight based on the total amount of sorbic acid and potassium sorbate, and the mixture is stirred at a temperature of 0°C or more and less than 45°C. A method for producing a formulation of sorbic acid coated with a mixture of sorbic acid or adduct and potassium sorbate. 4. The method according to item 3, characterized in that part of the sorbic acid is neutralized with potassium hydroxide or potassium carbonate to produce a mixture containing sorbic acid, potassium sorbate, and water. 5 In the method described in Item 3 or 4, the potassium sorbate concentration, that is, the ratio of potassium sorbate to the total amount of potassium sorbate and water is 27 to 62% by weight, and the weight ratio of sorbic acid and potassium sorbate is A mixture of sorbic acid, potassium sorbate and water is prepared by adding 1 part of potassium sorbate to 1 part of potassium sorbate, and the mixture is stirred to form an adduct, and then by filtration. , said method characterized in that the excess aqueous solution of potassium sorbate is removed. 6. The method according to item 3, 4 or 5, wherein the particle size of the raw material sorbic acid passes through a 60 mesh sieve and has an average particle size of 100 mesh or less. 7. The method according to any one of items 3 to 6, characterized in that the stirring treatment of sorbic acid, potassium sorbate, and water is carried out at a temperature of 0 to 40°C.
JP22834785A 1985-10-14 1985-10-14 Sorbic acid preparation and production thereof Granted JPS6287045A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22834785A JPS6287045A (en) 1985-10-14 1985-10-14 Sorbic acid preparation and production thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22834785A JPS6287045A (en) 1985-10-14 1985-10-14 Sorbic acid preparation and production thereof

Publications (2)

Publication Number Publication Date
JPS6287045A JPS6287045A (en) 1987-04-21
JPH0137097B2 true JPH0137097B2 (en) 1989-08-04

Family

ID=16875038

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22834785A Granted JPS6287045A (en) 1985-10-14 1985-10-14 Sorbic acid preparation and production thereof

Country Status (1)

Country Link
JP (1) JPS6287045A (en)

Also Published As

Publication number Publication date
JPS6287045A (en) 1987-04-21

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